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[]
["Environmental Assessment"]
[]
[null,null,"Type of water body","Description","Freshwater Q95 flowrate (m3/s)","Release point","Mean effluent flow rate (m3/s)","Max effluent flow rate (m3/s)","Substance","Release conc (ug/l)","Max release conc (ug/l)","Annual Average Background conc (ug/l)","PC (ug/l)","PEC (ug/l)","Annual EQS (ug/l)","(PEC-BC)/EQS","Test 3 - (PEC-BC)/EQS>10% annual EQS","%PEC EQS %","Test 4a - PEC >100% EQS","MAC EQS","PC (max) (ug/l)","PEC Max (ug/l)","PEC of MAC","Test 4b: PEC>100% MAC"]
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[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL298),INDIRECT(\"F\"&Variables!BL298),INDIRECT(\"I\"&Variables!BL298))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL299),INDIRECT(\"F\"&Variables!BL299),INDIRECT(\"I\"&Variables!BL299))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL300),INDIRECT(\"F\"&Variables!BL300),INDIRECT(\"I\"&Variables!BL300))","v":""}]
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[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL302),INDIRECT(\"F\"&Variables!BL302),INDIRECT(\"I\"&Variables!BL302))","v":""}]
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[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL304),INDIRECT(\"F\"&Variables!BL304),INDIRECT(\"I\"&Variables!BL304))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL305),INDIRECT(\"F\"&Variables!BL305),INDIRECT(\"I\"&Variables!BL305))","v":""}]
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[]
["Environmental Assessment"]
[]
[null,null,"Type of water body","Description","Freshwater Q95 flowrate (m3/s)","Release point","Mean effluent flow rate (m3/s)","Max effluent flow rate (m3/s)","Sewer factor (%)","Substance","Release conc (ug/l)","Annual EQS (ug/l)","Test 1: Release conc <100% EQS avg","Max release conc (ug/l)","MAC (ug/l)","Test 1: Release conc <100% EQS max","Comments","DOC"]
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[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL109),INDIRECT(\"F\"&Variables!BL109),INDIRECT(\"J\"&Variables!BL109))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL110),INDIRECT(\"F\"&Variables!BL110),INDIRECT(\"J\"&Variables!BL110))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL111),INDIRECT(\"F\"&Variables!BL111),INDIRECT(\"J\"&Variables!BL111))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL112),INDIRECT(\"F\"&Variables!BL112),INDIRECT(\"J\"&Variables!BL112))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL113),INDIRECT(\"F\"&Variables!BL113),INDIRECT(\"J\"&Variables!BL113))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL114),INDIRECT(\"F\"&Variables!BL114),INDIRECT(\"J\"&Variables!BL114))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL115),INDIRECT(\"F\"&Variables!BL115),INDIRECT(\"J\"&Variables!BL115))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL116),INDIRECT(\"F\"&Variables!BL116),INDIRECT(\"J\"&Variables!BL116))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL118),INDIRECT(\"F\"&Variables!BL118),INDIRECT(\"J\"&Variables!BL118))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL119),INDIRECT(\"F\"&Variables!BL119),INDIRECT(\"J\"&Variables!BL119))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL120),INDIRECT(\"F\"&Variables!BL120),INDIRECT(\"J\"&Variables!BL120))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL121),INDIRECT(\"F\"&Variables!BL121),INDIRECT(\"J\"&Variables!BL121))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL122),INDIRECT(\"F\"&Variables!BL122),INDIRECT(\"J\"&Variables!BL122))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL123),INDIRECT(\"F\"&Variables!BL123),INDIRECT(\"J\"&Variables!BL123))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL124),INDIRECT(\"F\"&Variables!BL124),INDIRECT(\"J\"&Variables!BL124))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL125),INDIRECT(\"F\"&Variables!BL125),INDIRECT(\"J\"&Variables!BL125))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL126),INDIRECT(\"F\"&Variables!BL126),INDIRECT(\"J\"&Variables!BL126))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL127),INDIRECT(\"F\"&Variables!BL127),INDIRECT(\"J\"&Variables!BL127))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL128),INDIRECT(\"F\"&Variables!BL128),INDIRECT(\"J\"&Variables!BL128))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL129),INDIRECT(\"F\"&Variables!BL129),INDIRECT(\"J\"&Variables!BL129))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL130),INDIRECT(\"F\"&Variables!BL130),INDIRECT(\"J\"&Variables!BL130))","v":""}]
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[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL135),INDIRECT(\"F\"&Variables!BL135),INDIRECT(\"J\"&Variables!BL135))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL136),INDIRECT(\"F\"&Variables!BL136),INDIRECT(\"J\"&Variables!BL136))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL137),INDIRECT(\"F\"&Variables!BL137),INDIRECT(\"J\"&Variables!BL137))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL138),INDIRECT(\"F\"&Variables!BL138),INDIRECT(\"J\"&Variables!BL138))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL139),INDIRECT(\"F\"&Variables!BL139),INDIRECT(\"J\"&Variables!BL139))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL140),INDIRECT(\"F\"&Variables!BL140),INDIRECT(\"J\"&Variables!BL140))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL141),INDIRECT(\"F\"&Variables!BL141),INDIRECT(\"J\"&Variables!BL141))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL142),INDIRECT(\"F\"&Variables!BL142),INDIRECT(\"J\"&Variables!BL142))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL143),INDIRECT(\"F\"&Variables!BL143),INDIRECT(\"J\"&Variables!BL143))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL144),INDIRECT(\"F\"&Variables!BL144),INDIRECT(\"J\"&Variables!BL144))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL145),INDIRECT(\"F\"&Variables!BL145),INDIRECT(\"J\"&Variables!BL145))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL146),INDIRECT(\"F\"&Variables!BL146),INDIRECT(\"J\"&Variables!BL146))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL147),INDIRECT(\"F\"&Variables!BL147),INDIRECT(\"J\"&Variables!BL147))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL148),INDIRECT(\"F\"&Variables!BL148),INDIRECT(\"J\"&Variables!BL148))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL149),INDIRECT(\"F\"&Variables!BL149),INDIRECT(\"J\"&Variables!BL149))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL151),INDIRECT(\"F\"&Variables!BL151),INDIRECT(\"J\"&Variables!BL151))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL152),INDIRECT(\"F\"&Variables!BL152),INDIRECT(\"J\"&Variables!BL152))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL153),INDIRECT(\"F\"&Variables!BL153),INDIRECT(\"J\"&Variables!BL153))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL154),INDIRECT(\"F\"&Variables!BL154),INDIRECT(\"J\"&Variables!BL154))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL155),INDIRECT(\"F\"&Variables!BL155),INDIRECT(\"J\"&Variables!BL155))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL156),INDIRECT(\"F\"&Variables!BL156),INDIRECT(\"J\"&Variables!BL156))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL157),INDIRECT(\"F\"&Variables!BL157),INDIRECT(\"J\"&Variables!BL157))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL158),INDIRECT(\"F\"&Variables!BL158),INDIRECT(\"J\"&Variables!BL158))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL159),INDIRECT(\"F\"&Variables!BL159),INDIRECT(\"J\"&Variables!BL159))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL161),INDIRECT(\"F\"&Variables!BL161),INDIRECT(\"J\"&Variables!BL161))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL162),INDIRECT(\"F\"&Variables!BL162),INDIRECT(\"J\"&Variables!BL162))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL163),INDIRECT(\"F\"&Variables!BL163),INDIRECT(\"J\"&Variables!BL163))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL164),INDIRECT(\"F\"&Variables!BL164),INDIRECT(\"J\"&Variables!BL164))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL165),INDIRECT(\"F\"&Variables!BL165),INDIRECT(\"J\"&Variables!BL165))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL166),INDIRECT(\"F\"&Variables!BL166),INDIRECT(\"J\"&Variables!BL166))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL167),INDIRECT(\"F\"&Variables!BL167),INDIRECT(\"J\"&Variables!BL167))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL168),INDIRECT(\"F\"&Variables!BL168),INDIRECT(\"J\"&Variables!BL168))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL169),INDIRECT(\"F\"&Variables!BL169),INDIRECT(\"J\"&Variables!BL169))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL170),INDIRECT(\"F\"&Variables!BL170),INDIRECT(\"J\"&Variables!BL170))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL171),INDIRECT(\"F\"&Variables!BL171),INDIRECT(\"J\"&Variables!BL171))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL172),INDIRECT(\"F\"&Variables!BL172),INDIRECT(\"J\"&Variables!BL172))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL173),INDIRECT(\"F\"&Variables!BL173),INDIRECT(\"J\"&Variables!BL173))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL174),INDIRECT(\"F\"&Variables!BL174),INDIRECT(\"J\"&Variables!BL174))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL175),INDIRECT(\"F\"&Variables!BL175),INDIRECT(\"J\"&Variables!BL175))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL176),INDIRECT(\"F\"&Variables!BL176),INDIRECT(\"J\"&Variables!BL176))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL177),INDIRECT(\"F\"&Variables!BL177),INDIRECT(\"J\"&Variables!BL177))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL178),INDIRECT(\"F\"&Variables!BL178),INDIRECT(\"J\"&Variables!BL178))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL179),INDIRECT(\"F\"&Variables!BL179),INDIRECT(\"J\"&Variables!BL179))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL180),INDIRECT(\"F\"&Variables!BL180),INDIRECT(\"J\"&Variables!BL180))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL181),INDIRECT(\"F\"&Variables!BL181),INDIRECT(\"J\"&Variables!BL181))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL182),INDIRECT(\"F\"&Variables!BL182),INDIRECT(\"J\"&Variables!BL182))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL183),INDIRECT(\"F\"&Variables!BL183),INDIRECT(\"J\"&Variables!BL183))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL184),INDIRECT(\"F\"&Variables!BL184),INDIRECT(\"J\"&Variables!BL184))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL185),INDIRECT(\"F\"&Variables!BL185),INDIRECT(\"J\"&Variables!BL185))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL186),INDIRECT(\"F\"&Variables!BL186),INDIRECT(\"J\"&Variables!BL186))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL187),INDIRECT(\"F\"&Variables!BL187),INDIRECT(\"J\"&Variables!BL187))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL188),INDIRECT(\"F\"&Variables!BL188),INDIRECT(\"J\"&Variables!BL188))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL189),INDIRECT(\"F\"&Variables!BL189),INDIRECT(\"J\"&Variables!BL189))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL190),INDIRECT(\"F\"&Variables!BL190),INDIRECT(\"J\"&Variables!BL190))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL191),INDIRECT(\"F\"&Variables!BL191),INDIRECT(\"J\"&Variables!BL191))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL192),INDIRECT(\"F\"&Variables!BL192),INDIRECT(\"J\"&Variables!BL192))","v":""}]
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[]
["Environmental Assessment"]
[null,null,null,null,null,null,"Annual avg EQS",null,null,null,null,"MAC EQS"]
[null,null,"Type of water body","Description","Freshwater Q95 flowrate (m3/s)","Substance","Annual EQS (ug/l)","PC (ug/l)","Modelled PC (ug/l)","%PC of EQS%","Test 2: PC<4% of EQS?","MAC EQS (ug/l)","PC (max) (ug/l)","Modelled PC (max) (ug/l)","%PC of MAC","Test 2: PC<4% of MAC?","DOC"]
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[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL102),INDIRECT(\"F\"&Variables!BL102),INDIRECT(\"J\"&Variables!BL102))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL103),INDIRECT(\"F\"&Variables!BL103),INDIRECT(\"J\"&Variables!BL103))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL104),INDIRECT(\"F\"&Variables!BL104),INDIRECT(\"J\"&Variables!BL104))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL105),INDIRECT(\"F\"&Variables!BL105),INDIRECT(\"J\"&Variables!BL105))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL106),INDIRECT(\"F\"&Variables!BL106),INDIRECT(\"J\"&Variables!BL106))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL107),INDIRECT(\"F\"&Variables!BL107),INDIRECT(\"J\"&Variables!BL107))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL108),INDIRECT(\"F\"&Variables!BL108),INDIRECT(\"J\"&Variables!BL108))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL109),INDIRECT(\"F\"&Variables!BL109),INDIRECT(\"J\"&Variables!BL109))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL110),INDIRECT(\"F\"&Variables!BL110),INDIRECT(\"J\"&Variables!BL110))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL111),INDIRECT(\"F\"&Variables!BL111),INDIRECT(\"J\"&Variables!BL111))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL112),INDIRECT(\"F\"&Variables!BL112),INDIRECT(\"J\"&Variables!BL112))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL113),INDIRECT(\"F\"&Variables!BL113),INDIRECT(\"J\"&Variables!BL113))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL114),INDIRECT(\"F\"&Variables!BL114),INDIRECT(\"J\"&Variables!BL114))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL115),INDIRECT(\"F\"&Variables!BL115),INDIRECT(\"J\"&Variables!BL115))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL116),INDIRECT(\"F\"&Variables!BL116),INDIRECT(\"J\"&Variables!BL116))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL118),INDIRECT(\"F\"&Variables!BL118),INDIRECT(\"J\"&Variables!BL118))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL119),INDIRECT(\"F\"&Variables!BL119),INDIRECT(\"J\"&Variables!BL119))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL120),INDIRECT(\"F\"&Variables!BL120),INDIRECT(\"J\"&Variables!BL120))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL121),INDIRECT(\"F\"&Variables!BL121),INDIRECT(\"J\"&Variables!BL121))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL122),INDIRECT(\"F\"&Variables!BL122),INDIRECT(\"J\"&Variables!BL122))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL123),INDIRECT(\"F\"&Variables!BL123),INDIRECT(\"J\"&Variables!BL123))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL124),INDIRECT(\"F\"&Variables!BL124),INDIRECT(\"J\"&Variables!BL124))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL125),INDIRECT(\"F\"&Variables!BL125),INDIRECT(\"J\"&Variables!BL125))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL126),INDIRECT(\"F\"&Variables!BL126),INDIRECT(\"J\"&Variables!BL126))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL127),INDIRECT(\"F\"&Variables!BL127),INDIRECT(\"J\"&Variables!BL127))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL128),INDIRECT(\"F\"&Variables!BL128),INDIRECT(\"J\"&Variables!BL128))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL129),INDIRECT(\"F\"&Variables!BL129),INDIRECT(\"J\"&Variables!BL129))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL130),INDIRECT(\"F\"&Variables!BL130),INDIRECT(\"J\"&Variables!BL130))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL131),INDIRECT(\"F\"&Variables!BL131),INDIRECT(\"J\"&Variables!BL131))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL132),INDIRECT(\"F\"&Variables!BL132),INDIRECT(\"J\"&Variables!BL132))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL133),INDIRECT(\"F\"&Variables!BL133),INDIRECT(\"J\"&Variables!BL133))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL134),INDIRECT(\"F\"&Variables!BL134),INDIRECT(\"J\"&Variables!BL134))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL135),INDIRECT(\"F\"&Variables!BL135),INDIRECT(\"J\"&Variables!BL135))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL136),INDIRECT(\"F\"&Variables!BL136),INDIRECT(\"J\"&Variables!BL136))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL137),INDIRECT(\"F\"&Variables!BL137),INDIRECT(\"J\"&Variables!BL137))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL138),INDIRECT(\"F\"&Variables!BL138),INDIRECT(\"J\"&Variables!BL138))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL139),INDIRECT(\"F\"&Variables!BL139),INDIRECT(\"J\"&Variables!BL139))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL140),INDIRECT(\"F\"&Variables!BL140),INDIRECT(\"J\"&Variables!BL140))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL141),INDIRECT(\"F\"&Variables!BL141),INDIRECT(\"J\"&Variables!BL141))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL142),INDIRECT(\"F\"&Variables!BL142),INDIRECT(\"J\"&Variables!BL142))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL143),INDIRECT(\"F\"&Variables!BL143),INDIRECT(\"J\"&Variables!BL143))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL144),INDIRECT(\"F\"&Variables!BL144),INDIRECT(\"J\"&Variables!BL144))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL145),INDIRECT(\"F\"&Variables!BL145),INDIRECT(\"J\"&Variables!BL145))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL146),INDIRECT(\"F\"&Variables!BL146),INDIRECT(\"J\"&Variables!BL146))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL147),INDIRECT(\"F\"&Variables!BL147),INDIRECT(\"J\"&Variables!BL147))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL148),INDIRECT(\"F\"&Variables!BL148),INDIRECT(\"J\"&Variables!BL148))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL149),INDIRECT(\"F\"&Variables!BL149),INDIRECT(\"J\"&Variables!BL149))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL151),INDIRECT(\"F\"&Variables!BL151),INDIRECT(\"J\"&Variables!BL151))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL152),INDIRECT(\"F\"&Variables!BL152),INDIRECT(\"J\"&Variables!BL152))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL153),INDIRECT(\"F\"&Variables!BL153),INDIRECT(\"J\"&Variables!BL153))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL154),INDIRECT(\"F\"&Variables!BL154),INDIRECT(\"J\"&Variables!BL154))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL155),INDIRECT(\"F\"&Variables!BL155),INDIRECT(\"J\"&Variables!BL155))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL156),INDIRECT(\"F\"&Variables!BL156),INDIRECT(\"J\"&Variables!BL156))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL157),INDIRECT(\"F\"&Variables!BL157),INDIRECT(\"J\"&Variables!BL157))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL158),INDIRECT(\"F\"&Variables!BL158),INDIRECT(\"J\"&Variables!BL158))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL159),INDIRECT(\"F\"&Variables!BL159),INDIRECT(\"J\"&Variables!BL159))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL161),INDIRECT(\"F\"&Variables!BL161),INDIRECT(\"J\"&Variables!BL161))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL162),INDIRECT(\"F\"&Variables!BL162),INDIRECT(\"J\"&Variables!BL162))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL163),INDIRECT(\"F\"&Variables!BL163),INDIRECT(\"J\"&Variables!BL163))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL164),INDIRECT(\"F\"&Variables!BL164),INDIRECT(\"J\"&Variables!BL164))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL165),INDIRECT(\"F\"&Variables!BL165),INDIRECT(\"J\"&Variables!BL165))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL166),INDIRECT(\"F\"&Variables!BL166),INDIRECT(\"J\"&Variables!BL166))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL167),INDIRECT(\"F\"&Variables!BL167),INDIRECT(\"J\"&Variables!BL167))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL168),INDIRECT(\"F\"&Variables!BL168),INDIRECT(\"J\"&Variables!BL168))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL169),INDIRECT(\"F\"&Variables!BL169),INDIRECT(\"J\"&Variables!BL169))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL170),INDIRECT(\"F\"&Variables!BL170),INDIRECT(\"J\"&Variables!BL170))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL171),INDIRECT(\"F\"&Variables!BL171),INDIRECT(\"J\"&Variables!BL171))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL172),INDIRECT(\"F\"&Variables!BL172),INDIRECT(\"J\"&Variables!BL172))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL173),INDIRECT(\"F\"&Variables!BL173),INDIRECT(\"J\"&Variables!BL173))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL174),INDIRECT(\"F\"&Variables!BL174),INDIRECT(\"J\"&Variables!BL174))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL175),INDIRECT(\"F\"&Variables!BL175),INDIRECT(\"J\"&Variables!BL175))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL176),INDIRECT(\"F\"&Variables!BL176),INDIRECT(\"J\"&Variables!BL176))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL177),INDIRECT(\"F\"&Variables!BL177),INDIRECT(\"J\"&Variables!BL177))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL178),INDIRECT(\"F\"&Variables!BL178),INDIRECT(\"J\"&Variables!BL178))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL179),INDIRECT(\"F\"&Variables!BL179),INDIRECT(\"J\"&Variables!BL179))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL180),INDIRECT(\"F\"&Variables!BL180),INDIRECT(\"J\"&Variables!BL180))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL181),INDIRECT(\"F\"&Variables!BL181),INDIRECT(\"J\"&Variables!BL181))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL182),INDIRECT(\"F\"&Variables!BL182),INDIRECT(\"J\"&Variables!BL182))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL183),INDIRECT(\"F\"&Variables!BL183),INDIRECT(\"J\"&Variables!BL183))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL184),INDIRECT(\"F\"&Variables!BL184),INDIRECT(\"J\"&Variables!BL184))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL185),INDIRECT(\"F\"&Variables!BL185),INDIRECT(\"J\"&Variables!BL185))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL186),INDIRECT(\"F\"&Variables!BL186),INDIRECT(\"J\"&Variables!BL186))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL187),INDIRECT(\"F\"&Variables!BL187),INDIRECT(\"J\"&Variables!BL187))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL188),INDIRECT(\"F\"&Variables!BL188),INDIRECT(\"J\"&Variables!BL188))","v":""}]
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[]
["Environmental Assessment"]
[]
[null,null,"Type of water body","Description","Freshwater Q95 flowrate (m3/s)","Substance","Annual Average Background conc (ug/l)","PC (ug/l)","PEC (ug/l)","Annual EQS (ug/l)","(PEC-BC)/EQS","Test 3 - (PEC-BC)/EQS>10% annual EQS","%PEC EQS %","Test 4a - PEC >100% EQS","MAC EQS (ug/l)","PC (max) (ug/l)","PEC Max (ug/l)","%PEC of MAC %","Test 4b: PEC>100% MAC","DOC"]
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[]
["Environmental Assessment"]
[]
[null,null,"Type of water body","Description","Release point","1. Is the discharge to a riverine estuary or direct to a low water channel within an estuary?","2. Is the discharge to a location with restricted dilution/dispersion characteristics?","3. Is the discharge either to a location less than 50m offshore from where the sea-bed is at Chart Datum or to a location where the sea-bed is less than 1m below Chart Datum?","4. Is the discharge buoyant?","Notes"]
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[null,null,null,null,null,null,null,null,null,{"$f":"IF(TRACTest43823[[#This Row],[1. Is the discharge to a riverine estuary or direct to a low water channel within an estuary?]]=\"Yes\",\"Ensure the receiving water is set to TR and complete TRAC tests 2-4 and TRAC test 5b doesn’t need to be completed \",IF(TRACTest43823[[#This Row],[2. Is the discharge to a location with restricted dilution/dispersion characteristics?]]=\"Yes\",\"Proceed to Phase 2: Modelling\",IF(TRACTest43823[[#This Row],[3. Is the discharge either to a location less than 50m offshore from where the sea-bed is at Chart Datum or to a location where the sea-bed is less than 1m below Chart Datum?]]=\"Yes\",\"Proceed to Phase 2, Modelling\",IF(TRACTest43823[[#This Row],[4. Is the discharge buoyant?]]=\"Yes\", \"Proceed to TRAC test 5b\",IF(TRACTest43823[[#This Row],[4. Is the discharge buoyant?]]=\"No\", \"Proceed to Phase 2: Modelling\",\"\")))))","v":""}]
[null,null,null,null,null,null,null,null,null,{"$f":"IF(TRACTest43823[[#This Row],[1. Is the discharge to a riverine estuary or direct to a low water channel within an estuary?]]=\"Yes\",\"Ensure the receiving water is set to TR and complete TRAC tests 2-4 and TRAC test 5b doesn’t need to be completed \",IF(TRACTest43823[[#This Row],[2. Is the discharge to a location with restricted dilution/dispersion characteristics?]]=\"Yes\",\"Proceed to Phase 2: Modelling\",IF(TRACTest43823[[#This Row],[3. Is the discharge either to a location less than 50m offshore from where the sea-bed is at Chart Datum or to a location where the sea-bed is less than 1m below Chart Datum?]]=\"Yes\",\"Proceed to Phase 2, Modelling\",IF(TRACTest43823[[#This Row],[4. Is the discharge buoyant?]]=\"Yes\", \"Proceed to TRAC test 5b\",IF(TRACTest43823[[#This Row],[4. Is the discharge buoyant?]]=\"No\", \"Proceed to Phase 2: Modelling\",\"\")))))","v":""}]
[null,null,null,null,null,null,null,null,null,{"$f":"IF(TRACTest43823[[#This Row],[1. Is the discharge to a riverine estuary or direct to a low water channel within an estuary?]]=\"Yes\",\"Ensure the receiving water is set to TR and complete TRAC tests 2-4 and TRAC test 5b doesn’t need to be completed \",IF(TRACTest43823[[#This Row],[2. Is the discharge to a location with restricted dilution/dispersion characteristics?]]=\"Yes\",\"Proceed to Phase 2: Modelling\",IF(TRACTest43823[[#This Row],[3. Is the discharge either to a location less than 50m offshore from where the sea-bed is at Chart Datum or to a location where the sea-bed is less than 1m below Chart Datum?]]=\"Yes\",\"Proceed to Phase 2, Modelling\",IF(TRACTest43823[[#This Row],[4. Is the discharge buoyant?]]=\"Yes\", \"Proceed to TRAC test 5b\",IF(TRACTest43823[[#This Row],[4. Is the discharge buoyant?]]=\"No\", \"Proceed to Phase 2: Modelling\",\"\")))))","v":""}]

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[]
["Environmental Assessment"]
[]
[null,null,"Type of water body","Description","TRaC water release depth (m)","Release point","Mean effluent flow rate (m3/s)","Max effluent flow rate (m3/s)","Sewer factor (%)","Substance","Release conc (ug/l)","Max release conc (ug/l)","Annual Average Background conc (ug/l)","Annual EQS (ug/l)","EVF (annual)","MAC EQS (ug/l)","EVF (max)","Allowable EVF","Test 5"]
[{"$f":"$C5&F5&J5","v":"TW2Copper - dissolved (Dissolved Organic Carbon (DOC) greater than 1mg/l) "},null,"T","Test for Copper",null,"W2",3.0599999999999999E-2,6.4600000000000005E-2,1,"Copper - dissolved (Dissolved Organic Carbon (DOC) greater than 1mg/l) ",35364.616935483878,6,null,{"$f":"IFERROR(VLOOKUP(TRACTest53924[[#This Row],[Substance]],SubstancesW!$B$6:$U$178,SubstancesW!$L$4,FALSE),\"\")","v":0},{"$f":"IF(ISNUMBER(TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]]),IFERROR(IF(TRACTest53924[[#This Row],[Sewer factor (%)]]=0,((TRACTest53924[[#This Row],[Mean effluent flow rate (m3/s)]]*TRACTest53924[[#This Row],[Release conc (ug/l)]])/(TRACTest53924[[#This Row],[Annual EQS (ug/l)]]-TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]])),IF(TRACTest53924[[#This Row],[Sewer factor (%)]]>0,((TRACTest53924[[#This Row],[Mean effluent flow rate (m3/s)]]*(TRACTest53924[[#This Row],[Release conc (ug/l)]]*(1-TRACTest53924[[#This Row],[Sewer factor (%)]])))/(TRACTest53924[[#This Row],[Annual EQS (ug/l)]]-TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]])),\"error in sewer factor\")),\"\"),\"\")","v":""},{"$f":"IFERROR(VLOOKUP(TRACTest53924[[#This Row],[Substance]],SubstancesW!$B$6:$U$168,SubstancesW!$M$4,FALSE),\"N/A\")","v":0},{"$f":"IFERROR(IF(TRACTest53924[[#This Row],[Sewer factor (%)]]=0,((TRACTest53924[[#This Row],[Max effluent flow rate (m3/s)]]*TRACTest53924[[#This Row],[Max release conc (ug/l)]])/(SUBSTITUTE(SUBSTITUTE(SUBSTITUTE(TRACTest53924[[#This Row],[MAC EQS (ug/l)]],\" (bioavailable)\",\"\"),\" (PNEC)\",\"\"),\" (95th %ile)\",\"\")-TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]])),IF(TRACTest53924[[#This Row],[Sewer factor (%)]]>0,((TRACTest53924[[#This Row],[Max effluent flow rate (m3/s)]]*(TRACTest53924[[#This Row],[Max release conc (ug/l)]]*(1-TRACTest53924[[#This Row],[Sewer factor (%)]])))/(SUBSTITUTE(SUBSTITUTE(SUBSTITUTE(TRACTest53924[[#This Row],[MAC EQS (ug/l)]],\" (bioavailable)\",\"\"),\" (PNEC)\",\"\"),\" (95th %ile)\",\"\")-TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]])),\"error in sewer factor\")),\"\")","v":""},{"$f":"IF(ISNUMBER(TRACTest53924[[#This Row],[TRaC water release depth (m)]]),(IF(TRACTest53924[[#This Row],[TRaC water release depth (m)]]<3.5,TRACTest53924[[#This Row],[TRaC water release depth (m)]],IF(TRACTest53924[[#This Row],[TRaC water release depth (m)]]>=3.5,3.5,\"error in depth\"))),\"Please add a water release depth in the third column\")","v":"Please add a water release depth in the third column"},{"$f":"IF(ISNUMBER(TRACTest53924[[#This Row],[EVF (annual)]]),(IF(OR(TRACTest53924[[#This Row],[EVF (max)]]>TRACTest53924[[#This Row],[Allowable EVF]],TRACTest53924[[#This Row],[EVF (annual)]]>TRACTest53924[[#This Row],[Allowable EVF]]),\"fail\",IF(OR(TRACTest53924[[#This Row],[EVF (max)]]<TRACTest53924[[#This Row],[Allowable EVF]],TRACTest53924[[#This Row],[EVF (annual)]]<TRACTest53924[[#This Row],[Allowable EVF]]),\"pass\",\"error\"))),\"N/A\")","v":"N/A"}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL10),INDIRECT(\"F\"&Variables!BL10),INDIRECT(\"J\"&Variables!BL10))","v":"TW1Arsenic"},null,"T","Horton Brook",null,"W1",3.0599999999999999E-2,6.4600000000000005E-2,1,"Chloride",47209.180327868875,70320,null,{"$f":"IFERROR(VLOOKUP(TRACTest53924[[#This Row],[Substance]],SubstancesW!$B$6:$U$178,SubstancesW!$L$4,FALSE),\"\")","v":250000},{"$f":"IF(ISNUMBER(TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]]),IFERROR(IF(TRACTest53924[[#This Row],[Sewer factor (%)]]=0,((TRACTest53924[[#This Row],[Mean effluent flow rate (m3/s)]]*TRACTest53924[[#This Row],[Release conc (ug/l)]])/(TRACTest53924[[#This Row],[Annual EQS (ug/l)]]-TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]])),IF(TRACTest53924[[#This Row],[Sewer factor (%)]]>0,((TRACTest53924[[#This Row],[Mean effluent flow rate (m3/s)]]*(TRACTest53924[[#This Row],[Release conc (ug/l)]]*(1-TRACTest53924[[#This Row],[Sewer factor (%)]])))/(TRACTest53924[[#This Row],[Annual EQS (ug/l)]]-TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]])),\"error in sewer factor\")),\"\"),\"\")","v":""},{"$f":"IFERROR(VLOOKUP(TRACTest53924[[#This Row],[Substance]],SubstancesW!$B$6:$U$168,SubstancesW!$M$4,FALSE),\"N/A\")","v":0},{"$f":"IFERROR(IF(TRACTest53924[[#This Row],[Sewer factor (%)]]=0,((TRACTest53924[[#This Row],[Max effluent flow rate (m3/s)]]*TRACTest53924[[#This Row],[Max release conc (ug/l)]])/(SUBSTITUTE(SUBSTITUTE(SUBSTITUTE(TRACTest53924[[#This Row],[MAC EQS (ug/l)]],\" (bioavailable)\",\"\"),\" (PNEC)\",\"\"),\" (95th %ile)\",\"\")-TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]])),IF(TRACTest53924[[#This Row],[Sewer factor (%)]]>0,((TRACTest53924[[#This Row],[Max effluent flow rate (m3/s)]]*(TRACTest53924[[#This Row],[Max release conc (ug/l)]]*(1-TRACTest53924[[#This Row],[Sewer factor (%)]])))/(SUBSTITUTE(SUBSTITUTE(SUBSTITUTE(TRACTest53924[[#This Row],[MAC EQS (ug/l)]],\" (bioavailable)\",\"\"),\" (PNEC)\",\"\"),\" (95th %ile)\",\"\")-TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]])),\"error in sewer factor\")),\"\")","v":""},{"$f":"IF(ISNUMBER(TRACTest53924[[#This Row],[TRaC water release depth (m)]]),(IF(TRACTest53924[[#This Row],[TRaC water release depth (m)]]<3.5,TRACTest53924[[#This Row],[TRaC water release depth (m)]],IF(TRACTest53924[[#This Row],[TRaC water release depth (m)]]>=3.5,3.5,\"error in depth\"))),\"Please add a water release depth in the third column\")","v":"Please add a water release depth in the third column"},{"$f":"IF(ISNUMBER(TRACTest53924[[#This Row],[EVF (annual)]]),(IF(OR(TRACTest53924[[#This Row],[EVF (max)]]>TRACTest53924[[#This Row],[Allowable EVF]],TRACTest53924[[#This Row],[EVF (annual)]]>TRACTest53924[[#This Row],[Allowable EVF]]),\"fail\",IF(OR(TRACTest53924[[#This Row],[EVF (max)]]<TRACTest53924[[#This Row],[Allowable EVF]],TRACTest53924[[#This Row],[EVF (annual)]]<TRACTest53924[[#This Row],[Allowable EVF]]),\"pass\",\"error\"))),\"N/A\")","v":"N/A"}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL11),INDIRECT(\"F\"&Variables!BL11),INDIRECT(\"J\"&Variables!BL11))","v":"TW1Cadmium and its compounds (dissolved, water hardness ≥ 200 mg/l CaCO3)"},null,"T","Horton Brook",null,"W1",3.0599999999999999E-2,6.4600000000000005E-2,1,"Sulphate",0.91547131147540928,141000,null,{"$f":"IFERROR(VLOOKUP(TRACTest53924[[#This Row],[Substance]],SubstancesW!$B$6:$U$178,SubstancesW!$L$4,FALSE),\"\")","v":400000},{"$f":"IF(ISNUMBER(TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]]),IFERROR(IF(TRACTest53924[[#This Row],[Sewer factor (%)]]=0,((TRACTest53924[[#This Row],[Mean effluent flow rate (m3/s)]]*TRACTest53924[[#This Row],[Release conc (ug/l)]])/(TRACTest53924[[#This Row],[Annual EQS (ug/l)]]-TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]])),IF(TRACTest53924[[#This Row],[Sewer factor (%)]]>0,((TRACTest53924[[#This Row],[Mean effluent flow rate (m3/s)]]*(TRACTest53924[[#This Row],[Release conc (ug/l)]]*(1-TRACTest53924[[#This Row],[Sewer factor (%)]])))/(TRACTest53924[[#This Row],[Annual EQS (ug/l)]]-TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]])),\"error in sewer factor\")),\"\"),\"\")","v":""},{"$f":"IFERROR(VLOOKUP(TRACTest53924[[#This Row],[Substance]],SubstancesW!$B$6:$U$168,SubstancesW!$M$4,FALSE),\"N/A\")","v":0},{"$f":"IFERROR(IF(TRACTest53924[[#This Row],[Sewer factor (%)]]=0,((TRACTest53924[[#This Row],[Max effluent flow rate (m3/s)]]*TRACTest53924[[#This Row],[Max release conc (ug/l)]])/(SUBSTITUTE(SUBSTITUTE(SUBSTITUTE(TRACTest53924[[#This Row],[MAC EQS (ug/l)]],\" (bioavailable)\",\"\"),\" (PNEC)\",\"\"),\" (95th %ile)\",\"\")-TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]])),IF(TRACTest53924[[#This Row],[Sewer factor (%)]]>0,((TRACTest53924[[#This Row],[Max effluent flow rate (m3/s)]]*(TRACTest53924[[#This Row],[Max release conc (ug/l)]]*(1-TRACTest53924[[#This Row],[Sewer factor (%)]])))/(SUBSTITUTE(SUBSTITUTE(SUBSTITUTE(TRACTest53924[[#This Row],[MAC EQS (ug/l)]],\" (bioavailable)\",\"\"),\" (PNEC)\",\"\"),\" (95th %ile)\",\"\")-TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]])),\"error in sewer factor\")),\"\")","v":""},{"$f":"IF(ISNUMBER(TRACTest53924[[#This Row],[TRaC water release depth (m)]]),(IF(TRACTest53924[[#This Row],[TRaC water release depth (m)]]<3.5,TRACTest53924[[#This Row],[TRaC water release depth (m)]],IF(TRACTest53924[[#This Row],[TRaC water release depth (m)]]>=3.5,3.5,\"error in depth\"))),\"Please add a water release depth in the third column\")","v":"Please add a water release depth in the third column"},{"$f":"IF(ISNUMBER(TRACTest53924[[#This Row],[EVF (annual)]]),(IF(OR(TRACTest53924[[#This Row],[EVF (max)]]>TRACTest53924[[#This Row],[Allowable EVF]],TRACTest53924[[#This Row],[EVF (annual)]]>TRACTest53924[[#This Row],[Allowable EVF]]),\"fail\",IF(OR(TRACTest53924[[#This Row],[EVF (max)]]<TRACTest53924[[#This Row],[Allowable EVF]],TRACTest53924[[#This Row],[EVF (annual)]]<TRACTest53924[[#This Row],[Allowable EVF]]),\"pass\",\"error\"))),\"N/A\")","v":"N/A"}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL12),INDIRECT(\"F\"&Variables!BL12),INDIRECT(\"J\"&Variables!BL12))","v":"TW1Chromium III (95%ile) (dissolved)"},null,"T","Horton Brook",null,"W1",3.0599999999999999E-2,6.4600000000000005E-2,0.89,"Arsenic",6.965709016393444E-2,13.172000000000001,null,{"$f":"IFERROR(VLOOKUP(TRACTest53924[[#This Row],[Substance]],SubstancesW!$B$6:$U$178,SubstancesW!$L$4,FALSE),\"\")","v":50},{"$f":"IF(ISNUMBER(TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]]),IFERROR(IF(TRACTest53924[[#This Row],[Sewer factor (%)]]=0,((TRACTest53924[[#This Row],[Mean effluent flow rate (m3/s)]]*TRACTest53924[[#This Row],[Release conc (ug/l)]])/(TRACTest53924[[#This Row],[Annual EQS (ug/l)]]-TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]])),IF(TRACTest53924[[#This Row],[Sewer factor (%)]]>0,((TRACTest53924[[#This Row],[Mean effluent flow rate (m3/s)]]*(TRACTest53924[[#This Row],[Release conc (ug/l)]]*(1-TRACTest53924[[#This Row],[Sewer factor (%)]])))/(TRACTest53924[[#This Row],[Annual EQS (ug/l)]]-TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]])),\"error in sewer factor\")),\"\"),\"\")","v":""},{"$f":"IFERROR(VLOOKUP(TRACTest53924[[#This Row],[Substance]],SubstancesW!$B$6:$U$168,SubstancesW!$M$4,FALSE),\"N/A\")","v":0},{"$f":"IFERROR(IF(TRACTest53924[[#This Row],[Sewer factor (%)]]=0,((TRACTest53924[[#This Row],[Max effluent flow rate (m3/s)]]*TRACTest53924[[#This Row],[Max release conc (ug/l)]])/(SUBSTITUTE(SUBSTITUTE(SUBSTITUTE(TRACTest53924[[#This Row],[MAC EQS (ug/l)]],\" (bioavailable)\",\"\"),\" (PNEC)\",\"\"),\" (95th %ile)\",\"\")-TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]])),IF(TRACTest53924[[#This Row],[Sewer factor (%)]]>0,((TRACTest53924[[#This Row],[Max effluent flow rate (m3/s)]]*(TRACTest53924[[#This Row],[Max release conc (ug/l)]]*(1-TRACTest53924[[#This Row],[Sewer factor (%)]])))/(SUBSTITUTE(SUBSTITUTE(SUBSTITUTE(TRACTest53924[[#This Row],[MAC EQS (ug/l)]],\" (bioavailable)\",\"\"),\" (PNEC)\",\"\"),\" (95th %ile)\",\"\")-TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]])),\"error in sewer factor\")),\"\")","v":""},{"$f":"IF(ISNUMBER(TRACTest53924[[#This Row],[TRaC water release depth (m)]]),(IF(TRACTest53924[[#This Row],[TRaC water release depth (m)]]<3.5,TRACTest53924[[#This Row],[TRaC water release depth (m)]],IF(TRACTest53924[[#This Row],[TRaC water release depth (m)]]>=3.5,3.5,\"error in depth\"))),\"Please add a water release depth in the third column\")","v":"Please add a water release depth in the third column"},{"$f":"IF(ISNUMBER(TRACTest53924[[#This Row],[EVF (annual)]]),(IF(OR(TRACTest53924[[#This Row],[EVF (max)]]>TRACTest53924[[#This Row],[Allowable EVF]],TRACTest53924[[#This Row],[EVF (annual)]]>TRACTest53924[[#This Row],[Allowable EVF]]),\"fail\",IF(OR(TRACTest53924[[#This Row],[EVF (max)]]<TRACTest53924[[#This Row],[Allowable EVF]],TRACTest53924[[#This Row],[EVF (annual)]]<TRACTest53924[[#This Row],[Allowable EVF]]),\"pass\",\"error\"))),\"N/A\")","v":"N/A"}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL13),INDIRECT(\"F\"&Variables!BL13),INDIRECT(\"J\"&Variables!BL13))","v":"TW2Chromium VI (95%ile) (dissolved)"},null,"T","Horton Brook",null,"W1",3.0599999999999999E-2,6.4600000000000005E-2,0.37,"Cadmium and its compounds (dissolved, water hardness ≥ 200 mg/l CaCO3)",0.34961967213114803,7.3999999999999996E-2,null,{"$f":"IFERROR(VLOOKUP(TRACTest53924[[#This Row],[Substance]],SubstancesW!$B$6:$U$178,SubstancesW!$L$4,FALSE),\"\")","v":0.25},{"$f":"IF(ISNUMBER(TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]]),IFERROR(IF(TRACTest53924[[#This Row],[Sewer factor (%)]]=0,((TRACTest53924[[#This Row],[Mean effluent flow rate (m3/s)]]*TRACTest53924[[#This Row],[Release conc (ug/l)]])/(TRACTest53924[[#This Row],[Annual EQS (ug/l)]]-TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]])),IF(TRACTest53924[[#This Row],[Sewer factor (%)]]>0,((TRACTest53924[[#This Row],[Mean effluent flow rate (m3/s)]]*(TRACTest53924[[#This Row],[Release conc (ug/l)]]*(1-TRACTest53924[[#This Row],[Sewer factor (%)]])))/(TRACTest53924[[#This Row],[Annual EQS (ug/l)]]-TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]])),\"error in sewer factor\")),\"\"),\"\")","v":""},{"$f":"IFERROR(VLOOKUP(TRACTest53924[[#This Row],[Substance]],SubstancesW!$B$6:$U$168,SubstancesW!$M$4,FALSE),\"N/A\")","v":0},{"$f":"IFERROR(IF(TRACTest53924[[#This Row],[Sewer factor (%)]]=0,((TRACTest53924[[#This Row],[Max effluent flow rate (m3/s)]]*TRACTest53924[[#This Row],[Max release conc (ug/l)]])/(SUBSTITUTE(SUBSTITUTE(SUBSTITUTE(TRACTest53924[[#This Row],[MAC EQS (ug/l)]],\" (bioavailable)\",\"\"),\" (PNEC)\",\"\"),\" (95th %ile)\",\"\")-TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]])),IF(TRACTest53924[[#This Row],[Sewer factor (%)]]>0,((TRACTest53924[[#This Row],[Max effluent flow rate (m3/s)]]*(TRACTest53924[[#This Row],[Max release conc (ug/l)]]*(1-TRACTest53924[[#This Row],[Sewer factor (%)]])))/(SUBSTITUTE(SUBSTITUTE(SUBSTITUTE(TRACTest53924[[#This Row],[MAC EQS (ug/l)]],\" (bioavailable)\",\"\"),\" (PNEC)\",\"\"),\" (95th %ile)\",\"\")-TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]])),\"error in sewer factor\")),\"\")","v":""},{"$f":"IF(ISNUMBER(TRACTest53924[[#This Row],[TRaC water release depth (m)]]),(IF(TRACTest53924[[#This Row],[TRaC water release depth (m)]]<3.5,TRACTest53924[[#This Row],[TRaC water release depth (m)]],IF(TRACTest53924[[#This Row],[TRaC water release depth (m)]]>=3.5,3.5,\"error in depth\"))),\"Please add a water release depth in the third column\")","v":"Please add a water release depth in the third column"},{"$f":"IF(ISNUMBER(TRACTest53924[[#This Row],[EVF (annual)]]),(IF(OR(TRACTest53924[[#This Row],[EVF (max)]]>TRACTest53924[[#This Row],[Allowable EVF]],TRACTest53924[[#This Row],[EVF (annual)]]>TRACTest53924[[#This Row],[Allowable EVF]]),\"fail\",IF(OR(TRACTest53924[[#This Row],[EVF (max)]]<TRACTest53924[[#This Row],[Allowable EVF]],TRACTest53924[[#This Row],[EVF (annual)]]<TRACTest53924[[#This Row],[Allowable EVF]]),\"pass\",\"error\"))),\"N/A\")","v":"N/A"}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL14),INDIRECT(\"F\"&Variables!BL14),INDIRECT(\"J\"&Variables!BL14))","v":"TW2Copper (dissolved, bioavailable)"},null,"T","Horton Brook",null,"W1",3.0599999999999999E-2,6.4600000000000005E-2,0.16,"Chromium III (95%ile) (dissolved)",0.15118688524590185,1.1679999999999999,null,{"$f":"IFERROR(VLOOKUP(TRACTest53924[[#This Row],[Substance]],SubstancesW!$B$6:$U$178,SubstancesW!$L$4,FALSE),\"\")","v":4.7},{"$f":"IF(ISNUMBER(TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]]),IFERROR(IF(TRACTest53924[[#This Row],[Sewer factor (%)]]=0,((TRACTest53924[[#This Row],[Mean effluent flow rate (m3/s)]]*TRACTest53924[[#This Row],[Release conc (ug/l)]])/(TRACTest53924[[#This Row],[Annual EQS (ug/l)]]-TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]])),IF(TRACTest53924[[#This Row],[Sewer factor (%)]]>0,((TRACTest53924[[#This Row],[Mean effluent flow rate (m3/s)]]*(TRACTest53924[[#This Row],[Release conc (ug/l)]]*(1-TRACTest53924[[#This Row],[Sewer factor (%)]])))/(TRACTest53924[[#This Row],[Annual EQS (ug/l)]]-TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]])),\"error in sewer factor\")),\"\"),\"\")","v":""},{"$f":"IFERROR(VLOOKUP(TRACTest53924[[#This Row],[Substance]],SubstancesW!$B$6:$U$168,SubstancesW!$M$4,FALSE),\"N/A\")","v":0},{"$f":"IFERROR(IF(TRACTest53924[[#This Row],[Sewer factor (%)]]=0,((TRACTest53924[[#This Row],[Max effluent flow rate (m3/s)]]*TRACTest53924[[#This Row],[Max release conc (ug/l)]])/(SUBSTITUTE(SUBSTITUTE(SUBSTITUTE(TRACTest53924[[#This Row],[MAC EQS (ug/l)]],\" (bioavailable)\",\"\"),\" (PNEC)\",\"\"),\" (95th %ile)\",\"\")-TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]])),IF(TRACTest53924[[#This Row],[Sewer factor (%)]]>0,((TRACTest53924[[#This Row],[Max effluent flow rate (m3/s)]]*(TRACTest53924[[#This Row],[Max release conc (ug/l)]]*(1-TRACTest53924[[#This Row],[Sewer factor (%)]])))/(SUBSTITUTE(SUBSTITUTE(SUBSTITUTE(TRACTest53924[[#This Row],[MAC EQS (ug/l)]],\" (bioavailable)\",\"\"),\" (PNEC)\",\"\"),\" (95th %ile)\",\"\")-TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]])),\"error in sewer factor\")),\"\")","v":""},{"$f":"IF(ISNUMBER(TRACTest53924[[#This Row],[TRaC water release depth (m)]]),(IF(TRACTest53924[[#This Row],[TRaC water release depth (m)]]<3.5,TRACTest53924[[#This Row],[TRaC water release depth (m)]],IF(TRACTest53924[[#This Row],[TRaC water release depth (m)]]>=3.5,3.5,\"error in depth\"))),\"Please add a water release depth in the third column\")","v":"Please add a water release depth in the third column"},{"$f":"IF(ISNUMBER(TRACTest53924[[#This Row],[EVF (annual)]]),(IF(OR(TRACTest53924[[#This Row],[EVF (max)]]>TRACTest53924[[#This Row],[Allowable EVF]],TRACTest53924[[#This Row],[EVF (annual)]]>TRACTest53924[[#This Row],[Allowable EVF]]),\"fail\",IF(OR(TRACTest53924[[#This Row],[EVF (max)]]<TRACTest53924[[#This Row],[Allowable EVF]],TRACTest53924[[#This Row],[EVF (annual)]]<TRACTest53924[[#This Row],[Allowable EVF]]),\"pass\",\"error\"))),\"N/A\")","v":"N/A"}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL15),INDIRECT(\"F\"&Variables!BL15),INDIRECT(\"J\"&Variables!BL15))","v":"TW2Iron (dissolved)"},null,"T","Test for Copper",null,"W2",3.0599999999999999E-2,6.4600000000000005E-2,0.16,"Chromium VI (95%ile) (dissolved)",0.26783016393442649,1.1679999999999999,null,{"$f":"IFERROR(VLOOKUP(TRACTest53924[[#This Row],[Substance]],SubstancesW!$B$6:$U$178,SubstancesW!$L$4,FALSE),\"\")","v":3.4},{"$f":"IF(ISNUMBER(TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]]),IFERROR(IF(TRACTest53924[[#This Row],[Sewer factor (%)]]=0,((TRACTest53924[[#This Row],[Mean effluent flow rate (m3/s)]]*TRACTest53924[[#This Row],[Release conc (ug/l)]])/(TRACTest53924[[#This Row],[Annual EQS (ug/l)]]-TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]])),IF(TRACTest53924[[#This Row],[Sewer factor (%)]]>0,((TRACTest53924[[#This Row],[Mean effluent flow rate (m3/s)]]*(TRACTest53924[[#This Row],[Release conc (ug/l)]]*(1-TRACTest53924[[#This Row],[Sewer factor (%)]])))/(TRACTest53924[[#This Row],[Annual EQS (ug/l)]]-TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]])),\"error in sewer factor\")),\"\"),\"\")","v":""},{"$f":"IFERROR(VLOOKUP(TRACTest53924[[#This Row],[Substance]],SubstancesW!$B$6:$U$168,SubstancesW!$M$4,FALSE),\"N/A\")","v":32},{"$f":"IFERROR(IF(TRACTest53924[[#This Row],[Sewer factor (%)]]=0,((TRACTest53924[[#This Row],[Max effluent flow rate (m3/s)]]*TRACTest53924[[#This Row],[Max release conc (ug/l)]])/(SUBSTITUTE(SUBSTITUTE(SUBSTITUTE(TRACTest53924[[#This Row],[MAC EQS (ug/l)]],\" (bioavailable)\",\"\"),\" (PNEC)\",\"\"),\" (95th %ile)\",\"\")-TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]])),IF(TRACTest53924[[#This Row],[Sewer factor (%)]]>0,((TRACTest53924[[#This Row],[Max effluent flow rate (m3/s)]]*(TRACTest53924[[#This Row],[Max release conc (ug/l)]]*(1-TRACTest53924[[#This Row],[Sewer factor (%)]])))/(SUBSTITUTE(SUBSTITUTE(SUBSTITUTE(TRACTest53924[[#This Row],[MAC EQS (ug/l)]],\" (bioavailable)\",\"\"),\" (PNEC)\",\"\"),\" (95th %ile)\",\"\")-TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]])),\"error in sewer factor\")),\"\")","v":1.980636E-3},{"$f":"IF(ISNUMBER(TRACTest53924[[#This Row],[TRaC water release depth (m)]]),(IF(TRACTest53924[[#This Row],[TRaC water release depth (m)]]<3.5,TRACTest53924[[#This Row],[TRaC water release depth (m)]],IF(TRACTest53924[[#This Row],[TRaC water release depth (m)]]>=3.5,3.5,\"error in depth\"))),\"Please add a water release depth in the third column\")","v":"Please add a water release depth in the third column"},{"$f":"IF(ISNUMBER(TRACTest53924[[#This Row],[EVF (annual)]]),(IF(OR(TRACTest53924[[#This Row],[EVF (max)]]>TRACTest53924[[#This Row],[Allowable EVF]],TRACTest53924[[#This Row],[EVF (annual)]]>TRACTest53924[[#This Row],[Allowable EVF]]),\"fail\",IF(OR(TRACTest53924[[#This Row],[EVF (max)]]<TRACTest53924[[#This Row],[Allowable EVF]],TRACTest53924[[#This Row],[EVF (annual)]]<TRACTest53924[[#This Row],[Allowable EVF]]),\"pass\",\"error\"))),\"N/A\")","v":"N/A"}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL16),INDIRECT(\"F\"&Variables!BL16),INDIRECT(\"J\"&Variables!BL16))","v":"TW2Lead and its compounds (dissolved)"},null,"T","Test for Copper",null,"W2",3.0599999999999999E-2,6.4600000000000005E-2,0.21,"Copper (dissolved, bioavailable)",27.674471311475415,1.89,null,{"$f":"IFERROR(VLOOKUP(TRACTest53924[[#This Row],[Substance]],SubstancesW!$B$6:$U$178,SubstancesW!$L$4,FALSE),\"\")","v":1},{"$f":"IF(ISNUMBER(TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]]),IFERROR(IF(TRACTest53924[[#This Row],[Sewer factor (%)]]=0,((TRACTest53924[[#This Row],[Mean effluent flow rate (m3/s)]]*TRACTest53924[[#This Row],[Release conc (ug/l)]])/(TRACTest53924[[#This Row],[Annual EQS (ug/l)]]-TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]])),IF(TRACTest53924[[#This Row],[Sewer factor (%)]]>0,((TRACTest53924[[#This Row],[Mean effluent flow rate (m3/s)]]*(TRACTest53924[[#This Row],[Release conc (ug/l)]]*(1-TRACTest53924[[#This Row],[Sewer factor (%)]])))/(TRACTest53924[[#This Row],[Annual EQS (ug/l)]]-TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]])),\"error in sewer factor\")),\"\"),\"\")","v":""},{"$f":"IFERROR(VLOOKUP(TRACTest53924[[#This Row],[Substance]],SubstancesW!$B$6:$U$168,SubstancesW!$M$4,FALSE),\"N/A\")","v":0},{"$f":"IFERROR(IF(TRACTest53924[[#This Row],[Sewer factor (%)]]=0,((TRACTest53924[[#This Row],[Max effluent flow rate (m3/s)]]*TRACTest53924[[#This Row],[Max release conc (ug/l)]])/(SUBSTITUTE(SUBSTITUTE(SUBSTITUTE(TRACTest53924[[#This Row],[MAC EQS (ug/l)]],\" (bioavailable)\",\"\"),\" (PNEC)\",\"\"),\" (95th %ile)\",\"\")-TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]])),IF(TRACTest53924[[#This Row],[Sewer factor (%)]]>0,((TRACTest53924[[#This Row],[Max effluent flow rate (m3/s)]]*(TRACTest53924[[#This Row],[Max release conc (ug/l)]]*(1-TRACTest53924[[#This Row],[Sewer factor (%)]])))/(SUBSTITUTE(SUBSTITUTE(SUBSTITUTE(TRACTest53924[[#This Row],[MAC EQS (ug/l)]],\" (bioavailable)\",\"\"),\" (PNEC)\",\"\"),\" (95th %ile)\",\"\")-TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]])),\"error in sewer factor\")),\"\")","v":""},{"$f":"IF(ISNUMBER(TRACTest53924[[#This Row],[TRaC water release depth (m)]]),(IF(TRACTest53924[[#This Row],[TRaC water release depth (m)]]<3.5,TRACTest53924[[#This Row],[TRaC water release depth (m)]],IF(TRACTest53924[[#This Row],[TRaC water release depth (m)]]>=3.5,3.5,\"error in depth\"))),\"Please add a water release depth in the third column\")","v":"Please add a water release depth in the third column"},{"$f":"IF(ISNUMBER(TRACTest53924[[#This Row],[EVF (annual)]]),(IF(OR(TRACTest53924[[#This Row],[EVF (max)]]>TRACTest53924[[#This Row],[Allowable EVF]],TRACTest53924[[#This Row],[EVF (annual)]]>TRACTest53924[[#This Row],[Allowable EVF]]),\"fail\",IF(OR(TRACTest53924[[#This Row],[EVF (max)]]<TRACTest53924[[#This Row],[Allowable EVF]],TRACTest53924[[#This Row],[EVF (annual)]]<TRACTest53924[[#This Row],[Allowable EVF]]),\"pass\",\"error\"))),\"N/A\")","v":"N/A"}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL17),INDIRECT(\"F\"&Variables!BL17),INDIRECT(\"J\"&Variables!BL17))","v":"TW2Manganese"},null,"T","Test for Copper",null,"W2",3.0599999999999999E-2,6.4600000000000005E-2,0.48,"Iron (dissolved)",0.12935999999999986,1670.3999999999999,null,{"$f":"IFERROR(VLOOKUP(TRACTest53924[[#This Row],[Substance]],SubstancesW!$B$6:$U$178,SubstancesW!$L$4,FALSE),\"\")","v":1000},{"$f":"IF(ISNUMBER(TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]]),IFERROR(IF(TRACTest53924[[#This Row],[Sewer factor (%)]]=0,((TRACTest53924[[#This Row],[Mean effluent flow rate (m3/s)]]*TRACTest53924[[#This Row],[Release conc (ug/l)]])/(TRACTest53924[[#This Row],[Annual EQS (ug/l)]]-TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]])),IF(TRACTest53924[[#This Row],[Sewer factor (%)]]>0,((TRACTest53924[[#This Row],[Mean effluent flow rate (m3/s)]]*(TRACTest53924[[#This Row],[Release conc (ug/l)]]*(1-TRACTest53924[[#This Row],[Sewer factor (%)]])))/(TRACTest53924[[#This Row],[Annual EQS (ug/l)]]-TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]])),\"error in sewer factor\")),\"\"),\"\")","v":""},{"$f":"IFERROR(VLOOKUP(TRACTest53924[[#This Row],[Substance]],SubstancesW!$B$6:$U$168,SubstancesW!$M$4,FALSE),\"N/A\")","v":0},{"$f":"IFERROR(IF(TRACTest53924[[#This Row],[Sewer factor (%)]]=0,((TRACTest53924[[#This Row],[Max effluent flow rate (m3/s)]]*TRACTest53924[[#This Row],[Max release conc (ug/l)]])/(SUBSTITUTE(SUBSTITUTE(SUBSTITUTE(TRACTest53924[[#This Row],[MAC EQS (ug/l)]],\" (bioavailable)\",\"\"),\" (PNEC)\",\"\"),\" (95th %ile)\",\"\")-TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]])),IF(TRACTest53924[[#This Row],[Sewer factor (%)]]>0,((TRACTest53924[[#This Row],[Max effluent flow rate (m3/s)]]*(TRACTest53924[[#This Row],[Max release conc (ug/l)]]*(1-TRACTest53924[[#This Row],[Sewer factor (%)]])))/(SUBSTITUTE(SUBSTITUTE(SUBSTITUTE(TRACTest53924[[#This Row],[MAC EQS (ug/l)]],\" (bioavailable)\",\"\"),\" (PNEC)\",\"\"),\" (95th %ile)\",\"\")-TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]])),\"error in sewer factor\")),\"\")","v":""},{"$f":"IF(ISNUMBER(TRACTest53924[[#This Row],[TRaC water release depth (m)]]),(IF(TRACTest53924[[#This Row],[TRaC water release depth (m)]]<3.5,TRACTest53924[[#This Row],[TRaC water release depth (m)]],IF(TRACTest53924[[#This Row],[TRaC water release depth (m)]]>=3.5,3.5,\"error in depth\"))),\"Please add a water release depth in the third column\")","v":"Please add a water release depth in the third column"},{"$f":"IF(ISNUMBER(TRACTest53924[[#This Row],[EVF (annual)]]),(IF(OR(TRACTest53924[[#This Row],[EVF (max)]]>TRACTest53924[[#This Row],[Allowable EVF]],TRACTest53924[[#This Row],[EVF (annual)]]>TRACTest53924[[#This Row],[Allowable EVF]]),\"fail\",IF(OR(TRACTest53924[[#This Row],[EVF (max)]]<TRACTest53924[[#This Row],[Allowable EVF]],TRACTest53924[[#This Row],[EVF (annual)]]<TRACTest53924[[#This Row],[Allowable EVF]]),\"pass\",\"error\"))),\"N/A\")","v":"N/A"}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL18),INDIRECT(\"F\"&Variables!BL18),INDIRECT(\"J\"&Variables!BL18))","v":"TW2Nickel and its compounds (dissolved)"},null,"T","Test for Copper",null,"W2",3.0599999999999999E-2,6.4600000000000005E-2,0.17,"Lead and its compounds (dissolved)",13.236269672131133,1.4382000000000001,null,{"$f":"IFERROR(VLOOKUP(TRACTest53924[[#This Row],[Substance]],SubstancesW!$B$6:$U$178,SubstancesW!$L$4,FALSE),\"\")","v":1.2},{"$f":"IF(ISNUMBER(TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]]),IFERROR(IF(TRACTest53924[[#This Row],[Sewer factor (%)]]=0,((TRACTest53924[[#This Row],[Mean effluent flow rate (m3/s)]]*TRACTest53924[[#This Row],[Release conc (ug/l)]])/(TRACTest53924[[#This Row],[Annual EQS (ug/l)]]-TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]])),IF(TRACTest53924[[#This Row],[Sewer factor (%)]]>0,((TRACTest53924[[#This Row],[Mean effluent flow rate (m3/s)]]*(TRACTest53924[[#This Row],[Release conc (ug/l)]]*(1-TRACTest53924[[#This Row],[Sewer factor (%)]])))/(TRACTest53924[[#This Row],[Annual EQS (ug/l)]]-TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]])),\"error in sewer factor\")),\"\"),\"\")","v":""},{"$f":"IFERROR(VLOOKUP(TRACTest53924[[#This Row],[Substance]],SubstancesW!$B$6:$U$168,SubstancesW!$M$4,FALSE),\"N/A\")","v":14},{"$f":"IFERROR(IF(TRACTest53924[[#This Row],[Sewer factor (%)]]=0,((TRACTest53924[[#This Row],[Max effluent flow rate (m3/s)]]*TRACTest53924[[#This Row],[Max release conc (ug/l)]])/(SUBSTITUTE(SUBSTITUTE(SUBSTITUTE(TRACTest53924[[#This Row],[MAC EQS (ug/l)]],\" (bioavailable)\",\"\"),\" (PNEC)\",\"\"),\" (95th %ile)\",\"\")-TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]])),IF(TRACTest53924[[#This Row],[Sewer factor (%)]]>0,((TRACTest53924[[#This Row],[Max effluent flow rate (m3/s)]]*(TRACTest53924[[#This Row],[Max release conc (ug/l)]]*(1-TRACTest53924[[#This Row],[Sewer factor (%)]])))/(SUBSTITUTE(SUBSTITUTE(SUBSTITUTE(TRACTest53924[[#This Row],[MAC EQS (ug/l)]],\" (bioavailable)\",\"\"),\" (PNEC)\",\"\"),\" (95th %ile)\",\"\")-TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]])),\"error in sewer factor\")),\"\")","v":5.5081005428571439E-3},{"$f":"IF(ISNUMBER(TRACTest53924[[#This Row],[TRaC water release depth (m)]]),(IF(TRACTest53924[[#This Row],[TRaC water release depth (m)]]<3.5,TRACTest53924[[#This Row],[TRaC water release depth (m)]],IF(TRACTest53924[[#This Row],[TRaC water release depth (m)]]>=3.5,3.5,\"error in depth\"))),\"Please add a water release depth in the third column\")","v":"Please add a water release depth in the third column"},{"$f":"IF(ISNUMBER(TRACTest53924[[#This Row],[EVF (annual)]]),(IF(OR(TRACTest53924[[#This Row],[EVF (max)]]>TRACTest53924[[#This Row],[Allowable EVF]],TRACTest53924[[#This Row],[EVF (annual)]]>TRACTest53924[[#This Row],[Allowable EVF]]),\"fail\",IF(OR(TRACTest53924[[#This Row],[EVF (max)]]<TRACTest53924[[#This Row],[Allowable EVF]],TRACTest53924[[#This Row],[EVF (annual)]]<TRACTest53924[[#This Row],[Allowable EVF]]),\"pass\",\"error\"))),\"N/A\")","v":"N/A"}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL19),INDIRECT(\"F\"&Variables!BL19),INDIRECT(\"J\"&Variables!BL19))","v":"TW2Fluoride (> 50mg/l CaCO3) (dissolved)"},null,"T","Test for Copper",null,"W2",3.0599999999999999E-2,6.4600000000000005E-2,1,"Manganese",3.0027663934426232,412,null,{"$f":"IFERROR(VLOOKUP(TRACTest53924[[#This Row],[Substance]],SubstancesW!$B$6:$U$178,SubstancesW!$L$4,FALSE),\"\")","v":123},{"$f":"IF(ISNUMBER(TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]]),IFERROR(IF(TRACTest53924[[#This Row],[Sewer factor (%)]]=0,((TRACTest53924[[#This Row],[Mean effluent flow rate (m3/s)]]*TRACTest53924[[#This Row],[Release conc (ug/l)]])/(TRACTest53924[[#This Row],[Annual EQS (ug/l)]]-TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]])),IF(TRACTest53924[[#This Row],[Sewer factor (%)]]>0,((TRACTest53924[[#This Row],[Mean effluent flow rate (m3/s)]]*(TRACTest53924[[#This Row],[Release conc (ug/l)]]*(1-TRACTest53924[[#This Row],[Sewer factor (%)]])))/(TRACTest53924[[#This Row],[Annual EQS (ug/l)]]-TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]])),\"error in sewer factor\")),\"\"),\"\")","v":""},{"$f":"IFERROR(VLOOKUP(TRACTest53924[[#This Row],[Substance]],SubstancesW!$B$6:$U$168,SubstancesW!$M$4,FALSE),\"N/A\")","v":0},{"$f":"IFERROR(IF(TRACTest53924[[#This Row],[Sewer factor (%)]]=0,((TRACTest53924[[#This Row],[Max effluent flow rate (m3/s)]]*TRACTest53924[[#This Row],[Max release conc (ug/l)]])/(SUBSTITUTE(SUBSTITUTE(SUBSTITUTE(TRACTest53924[[#This Row],[MAC EQS (ug/l)]],\" (bioavailable)\",\"\"),\" (PNEC)\",\"\"),\" (95th %ile)\",\"\")-TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]])),IF(TRACTest53924[[#This Row],[Sewer factor (%)]]>0,((TRACTest53924[[#This Row],[Max effluent flow rate (m3/s)]]*(TRACTest53924[[#This Row],[Max release conc (ug/l)]]*(1-TRACTest53924[[#This Row],[Sewer factor (%)]])))/(SUBSTITUTE(SUBSTITUTE(SUBSTITUTE(TRACTest53924[[#This Row],[MAC EQS (ug/l)]],\" (bioavailable)\",\"\"),\" (PNEC)\",\"\"),\" (95th %ile)\",\"\")-TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]])),\"error in sewer factor\")),\"\")","v":""},{"$f":"IF(ISNUMBER(TRACTest53924[[#This Row],[TRaC water release depth (m)]]),(IF(TRACTest53924[[#This Row],[TRaC water release depth (m)]]<3.5,TRACTest53924[[#This Row],[TRaC water release depth (m)]],IF(TRACTest53924[[#This Row],[TRaC water release depth (m)]]>=3.5,3.5,\"error in depth\"))),\"Please add a water release depth in the third column\")","v":"Please add a water release depth in the third column"},{"$f":"IF(ISNUMBER(TRACTest53924[[#This Row],[EVF (annual)]]),(IF(OR(TRACTest53924[[#This Row],[EVF (max)]]>TRACTest53924[[#This Row],[Allowable EVF]],TRACTest53924[[#This Row],[EVF (annual)]]>TRACTest53924[[#This Row],[Allowable EVF]]),\"fail\",IF(OR(TRACTest53924[[#This Row],[EVF (max)]]<TRACTest53924[[#This Row],[Allowable EVF]],TRACTest53924[[#This Row],[EVF (annual)]]<TRACTest53924[[#This Row],[Allowable EVF]]),\"pass\",\"error\"))),\"N/A\")","v":"N/A"}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL20),INDIRECT(\"F\"&Variables!BL20),INDIRECT(\"J\"&Variables!BL20))","v":"TW2Mercury and its compounds (dissolved)"},null,"T","Test for Copper",null,"W2",3.0599999999999999E-2,6.4600000000000005E-2,0.76,"Nickel and its compounds (dissolved)",331.67666666666662,6.7640000000000002,null,{"$f":"IFERROR(VLOOKUP(TRACTest53924[[#This Row],[Substance]],SubstancesW!$B$6:$U$178,SubstancesW!$L$4,FALSE),\"\")","v":4},{"$f":"IF(ISNUMBER(TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]]),IFERROR(IF(TRACTest53924[[#This Row],[Sewer factor (%)]]=0,((TRACTest53924[[#This Row],[Mean effluent flow rate (m3/s)]]*TRACTest53924[[#This Row],[Release conc (ug/l)]])/(TRACTest53924[[#This Row],[Annual EQS (ug/l)]]-TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]])),IF(TRACTest53924[[#This Row],[Sewer factor (%)]]>0,((TRACTest53924[[#This Row],[Mean effluent flow rate (m3/s)]]*(TRACTest53924[[#This Row],[Release conc (ug/l)]]*(1-TRACTest53924[[#This Row],[Sewer factor (%)]])))/(TRACTest53924[[#This Row],[Annual EQS (ug/l)]]-TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]])),\"error in sewer factor\")),\"\"),\"\")","v":""},{"$f":"IFERROR(VLOOKUP(TRACTest53924[[#This Row],[Substance]],SubstancesW!$B$6:$U$168,SubstancesW!$M$4,FALSE),\"N/A\")","v":34},{"$f":"IFERROR(IF(TRACTest53924[[#This Row],[Sewer factor (%)]]=0,((TRACTest53924[[#This Row],[Max effluent flow rate (m3/s)]]*TRACTest53924[[#This Row],[Max release conc (ug/l)]])/(SUBSTITUTE(SUBSTITUTE(SUBSTITUTE(TRACTest53924[[#This Row],[MAC EQS (ug/l)]],\" (bioavailable)\",\"\"),\" (PNEC)\",\"\"),\" (95th %ile)\",\"\")-TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]])),IF(TRACTest53924[[#This Row],[Sewer factor (%)]]>0,((TRACTest53924[[#This Row],[Max effluent flow rate (m3/s)]]*(TRACTest53924[[#This Row],[Max release conc (ug/l)]]*(1-TRACTest53924[[#This Row],[Sewer factor (%)]])))/(SUBSTITUTE(SUBSTITUTE(SUBSTITUTE(TRACTest53924[[#This Row],[MAC EQS (ug/l)]],\" (bioavailable)\",\"\"),\" (PNEC)\",\"\"),\" (95th %ile)\",\"\")-TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]])),\"error in sewer factor\")),\"\")","v":3.0843839999999999E-3},{"$f":"IF(ISNUMBER(TRACTest53924[[#This Row],[TRaC water release depth (m)]]),(IF(TRACTest53924[[#This Row],[TRaC water release depth (m)]]<3.5,TRACTest53924[[#This Row],[TRaC water release depth (m)]],IF(TRACTest53924[[#This Row],[TRaC water release depth (m)]]>=3.5,3.5,\"error in depth\"))),\"Please add a water release depth in the third column\")","v":"Please add a water release depth in the third column"},{"$f":"IF(ISNUMBER(TRACTest53924[[#This Row],[EVF (annual)]]),(IF(OR(TRACTest53924[[#This Row],[EVF (max)]]>TRACTest53924[[#This Row],[Allowable EVF]],TRACTest53924[[#This Row],[EVF (annual)]]>TRACTest53924[[#This Row],[Allowable EVF]]),\"fail\",IF(OR(TRACTest53924[[#This Row],[EVF (max)]]<TRACTest53924[[#This Row],[Allowable EVF]],TRACTest53924[[#This Row],[EVF (annual)]]<TRACTest53924[[#This Row],[Allowable EVF]]),\"pass\",\"error\"))),\"N/A\")","v":"N/A"}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL21),INDIRECT(\"F\"&Variables!BL21),INDIRECT(\"J\"&Variables!BL21))","v":"TW12,4-Dichlorophenoxyacetic acid (2,4-D) (95%ile)"},null,"T","Test for Copper",null,"W2",3.0599999999999999E-2,6.4600000000000005E-2,0.5,"Fluoride (> 50mg/l CaCO3) (dissolved)",6.592213114754112E-3,500,null,{"$f":"IFERROR(VLOOKUP(TRACTest53924[[#This Row],[Substance]],SubstancesW!$B$6:$U$178,SubstancesW!$L$4,FALSE),\"\")","v":5000},{"$f":"IF(ISNUMBER(TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]]),IFERROR(IF(TRACTest53924[[#This Row],[Sewer factor (%)]]=0,((TRACTest53924[[#This Row],[Mean effluent flow rate (m3/s)]]*TRACTest53924[[#This Row],[Release conc (ug/l)]])/(TRACTest53924[[#This Row],[Annual EQS (ug/l)]]-TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]])),IF(TRACTest53924[[#This Row],[Sewer factor (%)]]>0,((TRACTest53924[[#This Row],[Mean effluent flow rate (m3/s)]]*(TRACTest53924[[#This Row],[Release conc (ug/l)]]*(1-TRACTest53924[[#This Row],[Sewer factor (%)]])))/(TRACTest53924[[#This Row],[Annual EQS (ug/l)]]-TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]])),\"error in sewer factor\")),\"\"),\"\")","v":""},{"$f":"IFERROR(VLOOKUP(TRACTest53924[[#This Row],[Substance]],SubstancesW!$B$6:$U$168,SubstancesW!$M$4,FALSE),\"N/A\")","v":15000},{"$f":"IFERROR(IF(TRACTest53924[[#This Row],[Sewer factor (%)]]=0,((TRACTest53924[[#This Row],[Max effluent flow rate (m3/s)]]*TRACTest53924[[#This Row],[Max release conc (ug/l)]])/(SUBSTITUTE(SUBSTITUTE(SUBSTITUTE(TRACTest53924[[#This Row],[MAC EQS (ug/l)]],\" (bioavailable)\",\"\"),\" (PNEC)\",\"\"),\" (95th %ile)\",\"\")-TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]])),IF(TRACTest53924[[#This Row],[Sewer factor (%)]]>0,((TRACTest53924[[#This Row],[Max effluent flow rate (m3/s)]]*(TRACTest53924[[#This Row],[Max release conc (ug/l)]]*(1-TRACTest53924[[#This Row],[Sewer factor (%)]])))/(SUBSTITUTE(SUBSTITUTE(SUBSTITUTE(TRACTest53924[[#This Row],[MAC EQS (ug/l)]],\" (bioavailable)\",\"\"),\" (PNEC)\",\"\"),\" (95th %ile)\",\"\")-TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]])),\"error in sewer factor\")),\"\")","v":1.0766666666666667E-3},{"$f":"IF(ISNUMBER(TRACTest53924[[#This Row],[TRaC water release depth (m)]]),(IF(TRACTest53924[[#This Row],[TRaC water release depth (m)]]<3.5,TRACTest53924[[#This Row],[TRaC water release depth (m)]],IF(TRACTest53924[[#This Row],[TRaC water release depth (m)]]>=3.5,3.5,\"error in depth\"))),\"Please add a water release depth in the third column\")","v":"Please add a water release depth in the third column"},{"$f":"IF(ISNUMBER(TRACTest53924[[#This Row],[EVF (annual)]]),(IF(OR(TRACTest53924[[#This Row],[EVF (max)]]>TRACTest53924[[#This Row],[Allowable EVF]],TRACTest53924[[#This Row],[EVF (annual)]]>TRACTest53924[[#This Row],[Allowable EVF]]),\"fail\",IF(OR(TRACTest53924[[#This Row],[EVF (max)]]<TRACTest53924[[#This Row],[Allowable EVF]],TRACTest53924[[#This Row],[EVF (annual)]]<TRACTest53924[[#This Row],[Allowable EVF]]),\"pass\",\"error\"))),\"N/A\")","v":"N/A"}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL22),INDIRECT(\"F\"&Variables!BL22),INDIRECT(\"J\"&Variables!BL22))","v":"TW1Benzyl Butyl phthalate"},null,"T","Test for Copper",null,"W2",3.0599999999999999E-2,6.4600000000000005E-2,0.67,"Mercury and its compounds (dissolved)",1.0192793749999998E-2,3.3500000000000002E-2,null,{"$f":"IFERROR(VLOOKUP(TRACTest53924[[#This Row],[Substance]],SubstancesW!$B$6:$U$178,SubstancesW!$L$4,FALSE),\"\")","v":0},{"$f":"IF(ISNUMBER(TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]]),IFERROR(IF(TRACTest53924[[#This Row],[Sewer factor (%)]]=0,((TRACTest53924[[#This Row],[Mean effluent flow rate (m3/s)]]*TRACTest53924[[#This Row],[Release conc (ug/l)]])/(TRACTest53924[[#This Row],[Annual EQS (ug/l)]]-TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]])),IF(TRACTest53924[[#This Row],[Sewer factor (%)]]>0,((TRACTest53924[[#This Row],[Mean effluent flow rate (m3/s)]]*(TRACTest53924[[#This Row],[Release conc (ug/l)]]*(1-TRACTest53924[[#This Row],[Sewer factor (%)]])))/(TRACTest53924[[#This Row],[Annual EQS (ug/l)]]-TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]])),\"error in sewer factor\")),\"\"),\"\")","v":""},{"$f":"IFERROR(VLOOKUP(TRACTest53924[[#This Row],[Substance]],SubstancesW!$B$6:$U$168,SubstancesW!$M$4,FALSE),\"N/A\")","v":7.0000000000000007E-2},{"$f":"IFERROR(IF(TRACTest53924[[#This Row],[Sewer factor (%)]]=0,((TRACTest53924[[#This Row],[Max effluent flow rate (m3/s)]]*TRACTest53924[[#This Row],[Max release conc (ug/l)]])/(SUBSTITUTE(SUBSTITUTE(SUBSTITUTE(TRACTest53924[[#This Row],[MAC EQS (ug/l)]],\" (bioavailable)\",\"\"),\" (PNEC)\",\"\"),\" (95th %ile)\",\"\")-TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]])),IF(TRACTest53924[[#This Row],[Sewer factor (%)]]>0,((TRACTest53924[[#This Row],[Max effluent flow rate (m3/s)]]*(TRACTest53924[[#This Row],[Max release conc (ug/l)]]*(1-TRACTest53924[[#This Row],[Sewer factor (%)]])))/(SUBSTITUTE(SUBSTITUTE(SUBSTITUTE(TRACTest53924[[#This Row],[MAC EQS (ug/l)]],\" (bioavailable)\",\"\"),\" (PNEC)\",\"\"),\" (95th %ile)\",\"\")-TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]])),\"error in sewer factor\")),\"\")","v":1.0202185714285713E-2},{"$f":"IF(ISNUMBER(TRACTest53924[[#This Row],[TRaC water release depth (m)]]),(IF(TRACTest53924[[#This Row],[TRaC water release depth (m)]]<3.5,TRACTest53924[[#This Row],[TRaC water release depth (m)]],IF(TRACTest53924[[#This Row],[TRaC water release depth (m)]]>=3.5,3.5,\"error in depth\"))),\"Please add a water release depth in the third column\")","v":"Please add a water release depth in the third column"},{"$f":"IF(ISNUMBER(TRACTest53924[[#This Row],[EVF (annual)]]),(IF(OR(TRACTest53924[[#This Row],[EVF (max)]]>TRACTest53924[[#This Row],[Allowable EVF]],TRACTest53924[[#This Row],[EVF (annual)]]>TRACTest53924[[#This Row],[Allowable EVF]]),\"fail\",IF(OR(TRACTest53924[[#This Row],[EVF (max)]]<TRACTest53924[[#This Row],[Allowable EVF]],TRACTest53924[[#This Row],[EVF (annual)]]<TRACTest53924[[#This Row],[Allowable EVF]]),\"pass\",\"error\"))),\"N/A\")","v":"N/A"}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL23),INDIRECT(\"F\"&Variables!BL23),INDIRECT(\"J\"&Variables!BL23))","v":"TW1Benzene"},null,"T","Horton Brook",null,"W1",3.0599999999999999E-2,6.4600000000000005E-2,1,"2,4-Dichlorophenoxyacetic acid (2,4-D) (95%ile)",1.3075000000000002E-2,8.8999999999999996E-2,null,{"$f":"IFERROR(VLOOKUP(TRACTest53924[[#This Row],[Substance]],SubstancesW!$B$6:$U$178,SubstancesW!$L$4,FALSE),\"\")","v":0.3},{"$f":"IF(ISNUMBER(TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]]),IFERROR(IF(TRACTest53924[[#This Row],[Sewer factor (%)]]=0,((TRACTest53924[[#This Row],[Mean effluent flow rate (m3/s)]]*TRACTest53924[[#This Row],[Release conc (ug/l)]])/(TRACTest53924[[#This Row],[Annual EQS (ug/l)]]-TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]])),IF(TRACTest53924[[#This Row],[Sewer factor (%)]]>0,((TRACTest53924[[#This Row],[Mean effluent flow rate (m3/s)]]*(TRACTest53924[[#This Row],[Release conc (ug/l)]]*(1-TRACTest53924[[#This Row],[Sewer factor (%)]])))/(TRACTest53924[[#This Row],[Annual EQS (ug/l)]]-TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]])),\"error in sewer factor\")),\"\"),\"\")","v":""},{"$f":"IFERROR(VLOOKUP(TRACTest53924[[#This Row],[Substance]],SubstancesW!$B$6:$U$168,SubstancesW!$M$4,FALSE),\"N/A\")","v":1.3},{"$f":"IFERROR(IF(TRACTest53924[[#This Row],[Sewer factor (%)]]=0,((TRACTest53924[[#This Row],[Max effluent flow rate (m3/s)]]*TRACTest53924[[#This Row],[Max release conc (ug/l)]])/(SUBSTITUTE(SUBSTITUTE(SUBSTITUTE(TRACTest53924[[#This Row],[MAC EQS (ug/l)]],\" (bioavailable)\",\"\"),\" (PNEC)\",\"\"),\" (95th %ile)\",\"\")-TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]])),IF(TRACTest53924[[#This Row],[Sewer factor (%)]]>0,((TRACTest53924[[#This Row],[Max effluent flow rate (m3/s)]]*(TRACTest53924[[#This Row],[Max release conc (ug/l)]]*(1-TRACTest53924[[#This Row],[Sewer factor (%)]])))/(SUBSTITUTE(SUBSTITUTE(SUBSTITUTE(TRACTest53924[[#This Row],[MAC EQS (ug/l)]],\" (bioavailable)\",\"\"),\" (PNEC)\",\"\"),\" (95th %ile)\",\"\")-TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]])),\"error in sewer factor\")),\"\")","v":0},{"$f":"IF(ISNUMBER(TRACTest53924[[#This Row],[TRaC water release depth (m)]]),(IF(TRACTest53924[[#This Row],[TRaC water release depth (m)]]<3.5,TRACTest53924[[#This Row],[TRaC water release depth (m)]],IF(TRACTest53924[[#This Row],[TRaC water release depth (m)]]>=3.5,3.5,\"error in depth\"))),\"Please add a water release depth in the third column\")","v":"Please add a water release depth in the third column"},{"$f":"IF(ISNUMBER(TRACTest53924[[#This Row],[EVF (annual)]]),(IF(OR(TRACTest53924[[#This Row],[EVF (max)]]>TRACTest53924[[#This Row],[Allowable EVF]],TRACTest53924[[#This Row],[EVF (annual)]]>TRACTest53924[[#This Row],[Allowable EVF]]),\"fail\",IF(OR(TRACTest53924[[#This Row],[EVF (max)]]<TRACTest53924[[#This Row],[Allowable EVF]],TRACTest53924[[#This Row],[EVF (annual)]]<TRACTest53924[[#This Row],[Allowable EVF]]),\"pass\",\"error\"))),\"N/A\")","v":"N/A"}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL24),INDIRECT(\"F\"&Variables!BL24),INDIRECT(\"J\"&Variables!BL24))","v":"TW2Toluene (95%ile)"},null,"T","Horton Brook",null,"W1",3.0599999999999999E-2,6.4600000000000005E-2,0.73,"Benzyl Butyl phthalate",0.73,6.9496000000000002E-2,null,{"$f":"IFERROR(VLOOKUP(TRACTest53924[[#This Row],[Substance]],SubstancesW!$B$6:$U$178,SubstancesW!$L$4,FALSE),\"\")","v":7.5},{"$f":"IF(ISNUMBER(TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]]),IFERROR(IF(TRACTest53924[[#This Row],[Sewer factor (%)]]=0,((TRACTest53924[[#This Row],[Mean effluent flow rate (m3/s)]]*TRACTest53924[[#This Row],[Release conc (ug/l)]])/(TRACTest53924[[#This Row],[Annual EQS (ug/l)]]-TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]])),IF(TRACTest53924[[#This Row],[Sewer factor (%)]]>0,((TRACTest53924[[#This Row],[Mean effluent flow rate (m3/s)]]*(TRACTest53924[[#This Row],[Release conc (ug/l)]]*(1-TRACTest53924[[#This Row],[Sewer factor (%)]])))/(TRACTest53924[[#This Row],[Annual EQS (ug/l)]]-TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]])),\"error in sewer factor\")),\"\"),\"\")","v":""},{"$f":"IFERROR(VLOOKUP(TRACTest53924[[#This Row],[Substance]],SubstancesW!$B$6:$U$168,SubstancesW!$M$4,FALSE),\"N/A\")","v":10},{"$f":"IFERROR(IF(TRACTest53924[[#This Row],[Sewer factor (%)]]=0,((TRACTest53924[[#This Row],[Max effluent flow rate (m3/s)]]*TRACTest53924[[#This Row],[Max release conc (ug/l)]])/(SUBSTITUTE(SUBSTITUTE(SUBSTITUTE(TRACTest53924[[#This Row],[MAC EQS (ug/l)]],\" (bioavailable)\",\"\"),\" (PNEC)\",\"\"),\" (95th %ile)\",\"\")-TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]])),IF(TRACTest53924[[#This Row],[Sewer factor (%)]]>0,((TRACTest53924[[#This Row],[Max effluent flow rate (m3/s)]]*(TRACTest53924[[#This Row],[Max release conc (ug/l)]]*(1-TRACTest53924[[#This Row],[Sewer factor (%)]])))/(SUBSTITUTE(SUBSTITUTE(SUBSTITUTE(TRACTest53924[[#This Row],[MAC EQS (ug/l)]],\" (bioavailable)\",\"\"),\" (PNEC)\",\"\"),\" (95th %ile)\",\"\")-TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]])),\"error in sewer factor\")),\"\")","v":1.2121492320000004E-4},{"$f":"IF(ISNUMBER(TRACTest53924[[#This Row],[TRaC water release depth (m)]]),(IF(TRACTest53924[[#This Row],[TRaC water release depth (m)]]<3.5,TRACTest53924[[#This Row],[TRaC water release depth (m)]],IF(TRACTest53924[[#This Row],[TRaC water release depth (m)]]>=3.5,3.5,\"error in depth\"))),\"Please add a water release depth in the third column\")","v":"Please add a water release depth in the third column"},{"$f":"IF(ISNUMBER(TRACTest53924[[#This Row],[EVF (annual)]]),(IF(OR(TRACTest53924[[#This Row],[EVF (max)]]>TRACTest53924[[#This Row],[Allowable EVF]],TRACTest53924[[#This Row],[EVF (annual)]]>TRACTest53924[[#This Row],[Allowable EVF]]),\"fail\",IF(OR(TRACTest53924[[#This Row],[EVF (max)]]<TRACTest53924[[#This Row],[Allowable EVF]],TRACTest53924[[#This Row],[EVF (annual)]]<TRACTest53924[[#This Row],[Allowable EVF]]),\"pass\",\"error\"))),\"N/A\")","v":"N/A"}]
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[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL26),INDIRECT(\"F\"&Variables!BL26),INDIRECT(\"J\"&Variables!BL26))","v":"TW1Nickel and its compounds (dissolved)"},null,"T","Test for Copper",null,"W2",3.0599999999999999E-2,6.4600000000000005E-2,0.04,"Toluene (95%ile)",6.1149999999999996E-4,3.992,null,{"$f":"IFERROR(VLOOKUP(TRACTest53924[[#This Row],[Substance]],SubstancesW!$B$6:$U$178,SubstancesW!$L$4,FALSE),\"\")","v":74},{"$f":"IF(ISNUMBER(TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]]),IFERROR(IF(TRACTest53924[[#This Row],[Sewer factor (%)]]=0,((TRACTest53924[[#This Row],[Mean effluent flow rate (m3/s)]]*TRACTest53924[[#This Row],[Release conc (ug/l)]])/(TRACTest53924[[#This Row],[Annual EQS (ug/l)]]-TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]])),IF(TRACTest53924[[#This Row],[Sewer factor (%)]]>0,((TRACTest53924[[#This Row],[Mean effluent flow rate (m3/s)]]*(TRACTest53924[[#This Row],[Release conc (ug/l)]]*(1-TRACTest53924[[#This Row],[Sewer factor (%)]])))/(TRACTest53924[[#This Row],[Annual EQS (ug/l)]]-TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]])),\"error in sewer factor\")),\"\"),\"\")","v":""},{"$f":"IFERROR(VLOOKUP(TRACTest53924[[#This Row],[Substance]],SubstancesW!$B$6:$U$168,SubstancesW!$M$4,FALSE),\"N/A\")","v":370},{"$f":"IFERROR(IF(TRACTest53924[[#This Row],[Sewer factor (%)]]=0,((TRACTest53924[[#This Row],[Max effluent flow rate (m3/s)]]*TRACTest53924[[#This Row],[Max release conc (ug/l)]])/(SUBSTITUTE(SUBSTITUTE(SUBSTITUTE(TRACTest53924[[#This Row],[MAC EQS (ug/l)]],\" (bioavailable)\",\"\"),\" (PNEC)\",\"\"),\" (95th %ile)\",\"\")-TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]])),IF(TRACTest53924[[#This Row],[Sewer factor (%)]]>0,((TRACTest53924[[#This Row],[Max effluent flow rate (m3/s)]]*(TRACTest53924[[#This Row],[Max release conc (ug/l)]]*(1-TRACTest53924[[#This Row],[Sewer factor (%)]])))/(SUBSTITUTE(SUBSTITUTE(SUBSTITUTE(TRACTest53924[[#This Row],[MAC EQS (ug/l)]],\" (bioavailable)\",\"\"),\" (PNEC)\",\"\"),\" (95th %ile)\",\"\")-TRACTest53924[[#This Row],[Annual Average Background conc (ug/l)]])),\"error in sewer factor\")),\"\")","v":6.6910235675675671E-4},{"$f":"IF(ISNUMBER(TRACTest53924[[#This Row],[TRaC water release depth (m)]]),(IF(TRACTest53924[[#This Row],[TRaC water release depth (m)]]<3.5,TRACTest53924[[#This Row],[TRaC water release depth (m)]],IF(TRACTest53924[[#This Row],[TRaC water release depth (m)]]>=3.5,3.5,\"error in depth\"))),\"Please add a water release depth in the third column\")","v":"Please add a water release depth in the third column"},{"$f":"IF(ISNUMBER(TRACTest53924[[#This Row],[EVF (annual)]]),(IF(OR(TRACTest53924[[#This Row],[EVF (max)]]>TRACTest53924[[#This Row],[Allowable EVF]],TRACTest53924[[#This Row],[EVF (annual)]]>TRACTest53924[[#This Row],[Allowable EVF]]),\"fail\",IF(OR(TRACTest53924[[#This Row],[EVF (max)]]<TRACTest53924[[#This Row],[Allowable EVF]],TRACTest53924[[#This Row],[EVF (annual)]]<TRACTest53924[[#This Row],[Allowable EVF]]),\"pass\",\"error\"))),\"N/A\")","v":"N/A"}]
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[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL34),INDIRECT(\"F\"&Variables!BL34),INDIRECT(\"J\"&Variables!BL34))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL35),INDIRECT(\"F\"&Variables!BL35),INDIRECT(\"J\"&Variables!BL35))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL36),INDIRECT(\"F\"&Variables!BL36),INDIRECT(\"J\"&Variables!BL36))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL37),INDIRECT(\"F\"&Variables!BL37),INDIRECT(\"J\"&Variables!BL37))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL38),INDIRECT(\"F\"&Variables!BL38),INDIRECT(\"J\"&Variables!BL38))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL39),INDIRECT(\"F\"&Variables!BL39),INDIRECT(\"J\"&Variables!BL39))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL40),INDIRECT(\"F\"&Variables!BL40),INDIRECT(\"J\"&Variables!BL40))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL41),INDIRECT(\"F\"&Variables!BL41),INDIRECT(\"J\"&Variables!BL41))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL42),INDIRECT(\"F\"&Variables!BL42),INDIRECT(\"J\"&Variables!BL42))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL43),INDIRECT(\"F\"&Variables!BL43),INDIRECT(\"J\"&Variables!BL43))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL44),INDIRECT(\"F\"&Variables!BL44),INDIRECT(\"J\"&Variables!BL44))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL45),INDIRECT(\"F\"&Variables!BL45),INDIRECT(\"J\"&Variables!BL45))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL46),INDIRECT(\"F\"&Variables!BL46),INDIRECT(\"J\"&Variables!BL46))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL47),INDIRECT(\"F\"&Variables!BL47),INDIRECT(\"J\"&Variables!BL47))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL48),INDIRECT(\"F\"&Variables!BL48),INDIRECT(\"J\"&Variables!BL48))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL49),INDIRECT(\"F\"&Variables!BL49),INDIRECT(\"J\"&Variables!BL49))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL50),INDIRECT(\"F\"&Variables!BL50),INDIRECT(\"J\"&Variables!BL50))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL51),INDIRECT(\"F\"&Variables!BL51),INDIRECT(\"J\"&Variables!BL51))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL52),INDIRECT(\"F\"&Variables!BL52),INDIRECT(\"J\"&Variables!BL52))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL53),INDIRECT(\"F\"&Variables!BL53),INDIRECT(\"J\"&Variables!BL53))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL54),INDIRECT(\"F\"&Variables!BL54),INDIRECT(\"J\"&Variables!BL54))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL55),INDIRECT(\"F\"&Variables!BL55),INDIRECT(\"J\"&Variables!BL55))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL56),INDIRECT(\"F\"&Variables!BL56),INDIRECT(\"J\"&Variables!BL56))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL57),INDIRECT(\"F\"&Variables!BL57),INDIRECT(\"J\"&Variables!BL57))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL58),INDIRECT(\"F\"&Variables!BL58),INDIRECT(\"J\"&Variables!BL58))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL59),INDIRECT(\"F\"&Variables!BL59),INDIRECT(\"J\"&Variables!BL59))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL60),INDIRECT(\"F\"&Variables!BL60),INDIRECT(\"J\"&Variables!BL60))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL61),INDIRECT(\"F\"&Variables!BL61),INDIRECT(\"J\"&Variables!BL61))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL62),INDIRECT(\"F\"&Variables!BL62),INDIRECT(\"J\"&Variables!BL62))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL63),INDIRECT(\"F\"&Variables!BL63),INDIRECT(\"J\"&Variables!BL63))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL64),INDIRECT(\"F\"&Variables!BL64),INDIRECT(\"J\"&Variables!BL64))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL65),INDIRECT(\"F\"&Variables!BL65),INDIRECT(\"J\"&Variables!BL65))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL66),INDIRECT(\"F\"&Variables!BL66),INDIRECT(\"J\"&Variables!BL66))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL67),INDIRECT(\"F\"&Variables!BL67),INDIRECT(\"J\"&Variables!BL67))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL68),INDIRECT(\"F\"&Variables!BL68),INDIRECT(\"J\"&Variables!BL68))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL69),INDIRECT(\"F\"&Variables!BL69),INDIRECT(\"J\"&Variables!BL69))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL70),INDIRECT(\"F\"&Variables!BL70),INDIRECT(\"J\"&Variables!BL70))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL71),INDIRECT(\"F\"&Variables!BL71),INDIRECT(\"J\"&Variables!BL71))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL72),INDIRECT(\"F\"&Variables!BL72),INDIRECT(\"J\"&Variables!BL72))","v":""}]
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{"sheet":"1WatoSigL","index":13,"n_rows":7,"n_cols":8,"rows_kept":7,"cut":false,"hidden":true,"merged":[[0,2,0,3]]}
[]
["Environmental Assessment"]
[]
[null,null,"Type of water body","Description","Substance","Annual rate (kg/yr)","Significant load (PHS only) kg","Significant load test"]
[null,null,"R","Horton Brook","Cadmium and its compounds (dissolved, water hardness ≥ 200 mg/l CaCO3)",0.91184741350819809,{"$f":"IFERROR(VLOOKUP(SigLoadTest14025[[#This Row],[Substance]],SubstancesW!$B$5:$T$204,SubstancesW!$P$4,FALSE),0)","v":5},{"$f":"IF(ISNUMBER(SigLoadTest14025[[#This Row],[Significant load (PHS only) kg]]),IF(SigLoadTest14025[[#This Row],[Significant load (PHS only) kg]]>0.00000000000001,IF(SigLoadTest14025[[#This Row],[Annual rate (kg/yr)]]>SigLoadTest14025[[#This Row],[Significant load (PHS only) kg]],\"Fail\",\"Pass\"),\"\"),\"\")","v":"Pass"}]
[null,null,"T","Test for Copper","Mercury and its compounds (dissolved)",1.4680689965999999E-2,{"$f":"IFERROR(VLOOKUP(SigLoadTest14025[[#This Row],[Substance]],SubstancesW!$B$5:$T$204,SubstancesW!$P$4,FALSE),0)","v":1},{"$f":"IF(ISNUMBER(SigLoadTest14025[[#This Row],[Significant load (PHS only) kg]]),IF(SigLoadTest14025[[#This Row],[Significant load (PHS only) kg]]>0.00000000000001,IF(SigLoadTest14025[[#This Row],[Annual rate (kg/yr)]]>SigLoadTest14025[[#This Row],[Significant load (PHS only) kg]],\"Fail\",\"Pass\"),\"\"),\"\")","v":"Pass"}]
[null,null,"R","Horton Brook","Anthracene",0,{"$f":"IFERROR(VLOOKUP(SigLoadTest14025[[#This Row],[Substance]],SubstancesW!$B$5:$T$204,SubstancesW!$P$4,FALSE),0)","v":1},{"$f":"IF(ISNUMBER(SigLoadTest14025[[#This Row],[Significant load (PHS only) kg]]),IF(SigLoadTest14025[[#This Row],[Significant load (PHS only) kg]]>0.00000000000001,IF(SigLoadTest14025[[#This Row],[Annual rate (kg/yr)]]>SigLoadTest14025[[#This Row],[Significant load (PHS only) kg]],\"Fail\",\"Pass\"),\"\"),\"\")","v":"Pass"}]

{"sheet":"1Ai","index":14,"n_rows":112,"n_cols":308,"rows_kept":112,"cut":false,"hidden":false,"merged":[]}
[]
[]
["Air",null,null,null,{"$f":"IF(ISNUMBER(D3),VLOOKUP(D3,Stackdispersions!$B$6:$E$2006,2,FALSE),\"\")","v":""},{"$f":"IF(ISNUMBER(D3),VLOOKUP(D3,Stackdispersions!$B$6:$E$2006,3,FALSE),\"\")","v":""},null,null,null,null,null,null,{"$f":"L3*$I3*1000/1000000/3600","v":0},null,null,{"$f":"O3*I3*1000/1000000/3600","v":0},null,{"$f":"IFERROR(K3*M3/1000000*31536000,0)","v":0},null,null,null,null,{"$f":"V3:V3*$I3*1000/1000000/3600","v":0},null,null,{"$f":"Y3:Y3*$I3*1000/1000000/3600","v":0},null,{"$f":"IFERROR(U3*W3:W3/1000000*31536000,0)","v":0},null,null,null,null,{"$f":"AF3:AF3*$I3*1000/1000000/3600","v":0},null,null,{"$f":"AI3:AI3*$I3*1000/1000000/3600","v":0},null,{"$f":"IFERROR(AE3*AG3:AG3/1000000*31536000,0)","v":0},null,null,null,null,{"$f":"AP3:AP3*$I3*1000/1000000/3600","v":0},null,null,{"$f":"AS3:AS3*$I3*1000/1000000/3600","v":0},null,{"$f":"IFERROR(AO3*AQ3:AQ3/1000000*31536000,0)","v":0},null,null,null,null,{"$f":"AZ3:AZ3*$I3*1000/1000000/3600","v":0},null,null,{"$f":"BC3:BC3*$I3*1000/1000000/3600","v":0},null,{"$f":"IFERROR(AY3*BA3:BA3/1000000*31536000,0)","v":0},null,null,null,null,{"$f":"BJ3:BJ3*$I3*1000/1000000/3600","v":0},null,null,{"$f":"BM3:BM3*$I3*1000/1000000/3600","v":0},null,{"$f":"IFERROR(BI3*BK3:BK3/1000000*31536000,0)","v":0},null,null,null,null,{"$f":"BT3:BT3*$I3*1000/1000000/3600","v":0},null,null,{"$f":"BW3:BW3*$I3*1000/1000000/3600","v":0},null,{"$f":"IFERROR(BS3*BU3:BU3/1000000*31536000,0)","v":0},null,null,null,null,{"$f":"CD3:CD3*$I3*1000/1000000/3600","v":0},null,null,{"$f":"CG3:CG3*$I3*1000/1000000/3600","v":0},null,{"$f":"IFERROR(CC3*CE3:CE3/1000000*31536000,0)","v":0},null,null,null,null,{"$f":"CN3:CN3*$I3*1000/1000000/3600","v":0},null,null,{"$f":"CQ3:CQ3*$I3*1000/1000000/3600","v":0},null,{"$f":"IFERROR(CM3*CO3:CO3/1000000*31536000,0)","v":0},null,null,null,null,{"$f":"CX3:CX3*$I3*1000/1000000/3600","v":0},null,null,{"$f":"DA3:DA3*$I3*1000/1000000/3600","v":0},null,{"$f":"IFERROR(CW3*CY3:CY3/1000000*31536000,0)","v":0},null,null,null,null,{"$f":"DH3:DH3*$I3*1000/1000000/3600","v":0},null,null,{"$f":"DK3:DK3*$I3*1000/1000000/3600","v":0},null,{"$f":"IFERROR(DG3*DI3:DI3/1000000*31536000,0)","v":0},null,null,null,null,{"$f":"DR3:DR3*$I3*1000/1000000/3600","v":0},null,null,{"$f":"DU3:DU3*$I3*1000/1000000/3600","v":0},null,{"$f":"IFERROR(DQ3*DS3:DS3/1000000*31536000,0)","v":0},null,null,null,null,{"$f":"EB3:EB3*$I3*1000/1000000/3600","v":0},null,null,{"$f":"EE3:EE3*$I3*1000/1000000/3600","v":0},null,{"$f":"IFERROR(EA3*EC3:EC3/1000000*31536000,0)","v":0},null,null,null,null,{"$f":"EL3:EL3*$I3*1000/1000000/3600","v":0},null,null,{"$f":"EO3:EO3*$I3*1000/1000000/3600","v":0},null,{"$f":"IFERROR(EK3*EM3:EM3/1000000*31536000,0)","v":0},null,null,null,null,{"$f":"EV3:EV3*$I3*1000/1000000/3600","v":0},null,null,{"$f":"EY3:EY3*$I3*1000/1000000/3600","v":0},null,{"$f":"IFERROR(EU3*EW3:EW3/1000000*31536000,0)","v":0},null,null,null,null,{"$f":"FF3:FF3*$I3*1000/1000000/3600","v":0},null,null,{"$f":"FI3:FI3*$I3*1000/1000000/3600","v":0},null,{"$f":"IFERROR(FE3*FG3:FG3/1000000*31536000,0)","v":0},null,null,null,null,{"$f":"FP3:FP3*$I3*1000/1000000/3600","v":0},null,null,{"$f":"FS3:FS3*$I3*1000/1000000/3600","v":0},null,{"$f":"IFERROR(FO3*FQ3:FQ3/1000000*31536000,0)","v":0},null,null,null,null,{"$f":"FZ3:FZ3*$I3*1000/1000000/3600","v":0},null,null,{"$f":"GC3:GC3*$I3*1000/1000000/3600","v":0},null,{"$f":"IFERROR(FY3*GA3:GA3/1000000*31536000,0)","v":0},null,null,null,null,{"$f":"GJ3:GJ3*$I3*1000/1000000/3600","v":0},null,null,{"$f":"GM3:GM3*$I3*1000/1000000/3600","v":0},null,{"$f":"IFERROR(GI3*GK3:GK3/1000000*31536000,0)","v":0},null,null,null,null,{"$f":"GT3:GT3*$I3*1000/1000000/3600","v":0},null,null,{"$f":"GW3:GW3*$I3*1000/1000000/3600","v":0},null,{"$f":"IFERROR(GS3*GU3:GU3/1000000*31536000,0)","v":0},null,null,null,null,{"$f":"HD3:HD3*$I3*1000/1000000/3600","v":0},null,null,{"$f":"HG3:HG3*$I3*1000/1000000/3600","v":0},null,{"$f":"IFERROR(HC3*HE3:HE3/1000000*31536000,0)","v":0},null,null,null,null,{"$f":"HN3:HN3*$I3*1000/1000000/3600","v":0},null,null,{"$f":"HQ3:HQ3*$I3*1000/1000000/3600","v":0},null,{"$f":"IFERROR(HM3*HO3:HO3/1000000*31536000,0)","v":0},null,null,null,null,{"$f":"HX3:HX3*$I3*1000/1000000/3600","v":0},null,null,{"$f":"IA3:IA3*$I3*1000/1000000/3600","v":0},null,{"$f":"IFERROR(HW3*HY3:HY3/1000000*31536000,0)","v":0},null,null,null,null,{"$f":"IH3:IH3*$I3*1000/1000000/3600","v":0},null,null,{"$f":"IK3:IK3*$I3*1000/1000000/3600","v":0},null,{"$f":"IFERROR(IG3*II3:II3/1000000*31536000,0)","v":0},null,null,null,null,{"$f":"IR3:IR3*$I3*1000/1000000/3600","v":0},null,null,{"$f":"IU3:IU3*$I3*1000/1000000/3600","v":0},null,{"$f":"IFERROR(IQ3*IS3:IS3/1000000*31536000,0)","v":0},null,null,null,null,{"$f":"JB3:JB3*$I3*1000/1000000/3600","v":0},null,null,{"$f":"JE3:JE3*$I3*1000/1000000/3600","v":0},null,{"$f":"IFERROR(JA3*JC3:JC3/1000000*31536000,0)","v":0},null,null,null,null,{"$f":"JL3:JL3*$I3*1000/1000000/3600","v":0},null,null,{"$f":"JO3:JO3*$I3*1000/1000000/3600","v":0},null,{"$f":"IFERROR(JK3*JM3:JM3/1000000*31536000,0)","v":0},null,null,null,null,{"$f":"JV3:JV3*$I3*1000/1000000/3600","v":0},null,null,{"$f":"JY3:JY3*$I3*1000/1000000/3600","v":0},null,{"$f":"IFERROR(JU3*JW3:JW3/1000000*31536000,0)","v":0},null,null,null,null,{"$f":"KF3:KF3*$I3*1000/1000000/3600","v":0},null,null,{"$f":"KI3:KI3*$I3*1000/1000000/3600","v":0},null,{"$f":"IFERROR(KE3*KG3:KG3/1000000*31536000,0)","v":0},null,null,null,null,{"$f":"KP3:KP3*$I3*1000/1000000/3600","v":0},null,null,{"$f":"KS3:KS3*$I3*1000/1000000/3600","v":0},null,{"$f":"IFERROR(KO3*KQ3:KQ3/1000000*31536000,0)","v":0}]
[null,"Environmental Assessment"]
[]
[]
[{"$f":"COUNTIF(AirReleasePointTopRow1:RP_TopRow,\"<>\"&\"\")-2","v":8},"Release point code","Location or grid reference","Activity/Activities","Effective height (metres)","Dispersion factor (Long term)","Dispersion factor (short term)","Dispersion factor (monthly)","Efflux velocity (m/s)","Total flow (m3/h)"]
[null,"A1",null,null,0,{"$f":"IF(ISNUMBER(E8),VLOOKUP(E8,Stackdispersions!$B$6:$E$2006,2,FALSE),\"\")","v":148},{"$f":"IF(ISNUMBER(E8),VLOOKUP(E8,Stackdispersions!$B$6:$E$2006,3,FALSE),\"\")","v":3900},{"$f":"IF(ISNUMBER(E8),VLOOKUP(E8,Stackdispersions!$B$6:$E$2006,4,FALSE),\"\")","v":529},6.727734878353699,428]
[null,"A2",null,null,0,{"$f":"IF(ISNUMBER(E9),VLOOKUP(E9,Stackdispersions!$B$6:$E$2006,2,FALSE),\"\")","v":148},{"$f":"IF(ISNUMBER(E9),VLOOKUP(E9,Stackdispersions!$B$6:$E$2006,3,FALSE),\"\")","v":3900},{"$f":"IF(ISNUMBER(E9),VLOOKUP(E9,Stackdispersions!$B$6:$E$2006,4,FALSE),\"\")","v":529},6.1755433647636471,1788]
[null,"A6",null,null,0,{"$f":"IF(ISNUMBER(E10),VLOOKUP(E10,Stackdispersions!$B$6:$E$2006,2,FALSE),\"\")","v":148},{"$f":"IF(ISNUMBER(E10),VLOOKUP(E10,Stackdispersions!$B$6:$E$2006,3,FALSE),\"\")","v":3900},{"$f":"IF(ISNUMBER(E10),VLOOKUP(E10,Stackdispersions!$B$6:$E$2006,4,FALSE),\"\")","v":529},1.6897932229509876,430]
[null,"A7",null,null,0,{"$f":"IF(ISNUMBER(E11),VLOOKUP(E11,Stackdispersions!$B$6:$E$2006,2,FALSE),\"\")","v":148},{"$f":"IF(ISNUMBER(E11),VLOOKUP(E11,Stackdispersions!$B$6:$E$2006,3,FALSE),\"\")","v":3900},{"$f":"IF(ISNUMBER(E11),VLOOKUP(E11,Stackdispersions!$B$6:$E$2006,4,FALSE),\"\")","v":529},4.6005725737500995,1332]
[null,"A9",null,null,0,{"$f":"IF(ISNUMBER(E12),VLOOKUP(E12,Stackdispersions!$B$6:$E$2006,2,FALSE),\"\")","v":148},{"$f":"IF(ISNUMBER(E12),VLOOKUP(E12,Stackdispersions!$B$6:$E$2006,3,FALSE),\"\")","v":3900},{"$f":"IF(ISNUMBER(E12),VLOOKUP(E12,Stackdispersions!$B$6:$E$2006,4,FALSE),\"\")","v":529},3.9146853668770083,7997]
[null,"A10",null,null,0,{"$f":"IF(ISNUMBER(E13),VLOOKUP(E13,Stackdispersions!$B$6:$E$2006,2,FALSE),\"\")","v":148},{"$f":"IF(ISNUMBER(E13),VLOOKUP(E13,Stackdispersions!$B$6:$E$2006,3,FALSE),\"\")","v":3900},{"$f":"IF(ISNUMBER(E13),VLOOKUP(E13,Stackdispersions!$B$6:$E$2006,4,FALSE),\"\")","v":529},17.070841303486258,4344]
[null,"A12",null,null,0,{"$f":"IF(ISNUMBER(E14),VLOOKUP(E14,Stackdispersions!$B$6:$E$2006,2,FALSE),\"\")","v":148},{"$f":"IF(ISNUMBER(E14),VLOOKUP(E14,Stackdispersions!$B$6:$E$2006,3,FALSE),\"\")","v":3900},{"$f":"IF(ISNUMBER(E14),VLOOKUP(E14,Stackdispersions!$B$6:$E$2006,4,FALSE),\"\")","v":529},7.4638418407462206,2161]
[null,"A13",null,null,0,{"$f":"IF(ISNUMBER(E15),VLOOKUP(E15,Stackdispersions!$B$6:$E$2006,2,FALSE),\"\")","v":148},{"$f":"IF(ISNUMBER(E15),VLOOKUP(E15,Stackdispersions!$B$6:$E$2006,3,FALSE),\"\")","v":3900},{"$f":"IF(ISNUMBER(E15),VLOOKUP(E15,Stackdispersions!$B$6:$E$2006,4,FALSE),\"\")","v":529},19.027857640764374,2152]
[]
[]
[]
[]
[{"$f":"COUNTIF(RP_TopRow:B242,\"<>\"&\"\")-1","v":48},"Release Point","Substance","Measurement method","Operating mode(%)","Long term conc (mg/m3)","Release rate g/s (long term)","Measurement basis (Long term)","Short term conc (mg/m3)","Release rate g/s  (short term)","Measurement basis (short term)","Annual rate (t/yr)","Long term PC (ug/m3) ","Short term PC (ug/m3) ","Total Flow (m3/h)"]
[null,"A1","Particulates (PM10)",null,0.24,0.99,{"$f":"F21*O21*1000/1000000/3600","v":1.1769999999999997E-4},null,0.99,{"$f":"I21*O21*1000/1000000/3600","v":1.1769999999999997E-4},null,{"$f":"IFERROR(E21*G21/1000000*31536000,0)","v":8.9082892799999974E-4},{"$f":"IF(C21=\"Chloroform\",P21,\nIF(C21=\"Methyl chloroform\",P21,\nIF(C21=\"Naphthalene\",P21,\nIF(C21=\"Tetrachloroethylene\",P21,\nIF(C21=\"Mono-ethanolamine (MEA)\",P21,\nIF(C21=\"Methyl chloride (chloromethane)\",P21,\nIF(C21=\"Chromium (III) compounds (as Cr)\",P21,\nIF(C21=\"Copper and compounds (as Cu)\",P21,\nIF(C21=\"Hydrogen cyanide\",P21,\nIF(C21=\"Mercury and its inorganic compounds (as Hg)\",P21,\nIF(C21=\"Selenium and compounds (as Se), except hydrogen selenide\",P21,\n\nIF(C21=\"Hydrogen fluoride\",R21,\nIF(C21=\"Hydrogen iodide\",R21,\n\nIF(C21=\"Hydrogen fluoride (ecological)\",Q21*0.31,\nIF(C21=\"Styrene\",Q21*0.31,\nIF(C21=\"Toluene\",Q21*0.31,\nP21*E21))))))))))))))))","v":4.1807039999999995E-3},{"$f":"IF(C21=\"1,3-Butadiene\",Q21*0.59,\nIF(C21=\"Benzene\",Q21*0.59,\nIF(C21=\"Cadmium and compounds (as Cd)\",Q21*0.59,\nIF(C21=\"Carbon disulphide\",Q21*0.59,\nIF(C21=\"Methylene chloride (dichloromethane)\",Q21*0.59,\nIF(C21=\"Hydrogen fluoride (ecological)\",Q21*0.59,\nIF(C21=\"Hydrogen sulphide\",Q21*0.59,\nIF(C21=\"Nitrogen oxides (as NO2) (ecological)\",Q21*0.59,\nIF(C21=\"Particulates (PM10)\",Q21*0.59,\nIF(C21=\"Sulphur dioxide (24 hr mean)\",Q21*0.59,\nIF(C21=\"Vanadium and compounds (as V)\",Q21*0.59,\nIF(C21=\"Vinyl chloride\",Q21*0.59,\n\nIF(C21=\"Carbon monoxide\",Q21*0.7,\nIF(C21=\"Ozone\",Q21*0.7,\n\nIF(C21=\"Sulphur dioxide  (15 min mean)\",Q21*1.34,\nIF(C21=\"Formaldehyde\",Q21*1.3,\n\nIF(C21=\"Nitrogen dioxide\",Q21*0.5,\nQ21)))))))))))))))))","v":0.27082769999999989},{"$f":"IFERROR(VLOOKUP(B21,$B$7:J$18,9,FALSE),0)","v":428},{"$f":"IFERROR((VLOOKUP(B21,$B$7:$J$18,5,FALSE))*G21,0)","v":1.7419599999999997E-2},{"$f":"IFERROR(VLOOKUP(B21,$B$7:$J$18,6,FALSE)*J21,0)","v":0.45902999999999988},{"$f":"IFERROR((VLOOKUP(B21,$B$7:$J$18,7,FALSE))*G21,0)","v":6.2263299999999987E-2}]
[null,"A2","Particulates (PM10)",null,0.24,0.94,4.6686666666666661E-4,null,0.94,4.6686666666666661E-4,null,3.5335457279999996E-3,1.6583103999999998E-2,1.0742601999999999,{"$f":"IFERROR(VLOOKUP(B22,$B$7:J$18,9,FALSE),0)","v":1788},6.9096266666666656E-2,1.8207799999999998,0.24697246666666664]
[null,"A6","Particulates (PM10)",null,0.24,0.82,9.7944444444444432E-5,null,0.82,9.7944444444444432E-5,null,7.4130623999999986E-4,3.4789866666666662E-3,0.22537016666666662,{"$f":"IFERROR(VLOOKUP(B23,$B$7:J$18,9,FALSE),0)","v":430},1.4495777777777776E-2,0.38198333333333329,5.1812611111111108E-2]
[null,"A7","Particulates (PM10)",null,0.24,1,3.6999999999999999E-4,null,1,3.6999999999999999E-4,null,2.8003968E-3,1.3142399999999999E-2,0.85136999999999996,{"$f":"IFERROR(VLOOKUP(B24,$B$7:J$18,9,FALSE),0)","v":1332},5.4759999999999996E-2,1.4430000000000001,0.19572999999999999]
[null,"A9","Particulates (PM10)",null,0.24,1.8,3.9985000000000003E-3,null,1.8,3.9985000000000003E-3,null,3.026320704E-2,0.14202672,9.2005485,{"$f":"IFERROR(VLOOKUP(B25,$B$7:J$18,9,FALSE),0)","v":7997},0.59177800000000003,15.594150000000001,2.1152065000000002]
[null,"A10","Particulates (PM10)",null,0.24,11.2,1.3514666666666664E-2,null,11.2,1.3514666666666664E-2,null,0.10228764671999997,0.48004095999999996,31.097247999999993,{"$f":"IFERROR(VLOOKUP(B26,$B$7:J$18,9,FALSE),0)","v":4344},2.0001706666666665,52.707199999999993,7.1492586666666655]
[null,"A12","Particulates (PM10)",null,0.24,9.6999999999999993,5.8226944444444437E-3,null,9.6999999999999993,5.8226944444444437E-3,null,4.4069878079999993E-2,0.20682210666666662,13.398019916666664,{"$f":"IFERROR(VLOOKUP(B27,$B$7:J$18,9,FALSE),0)","v":2161},0.86175877777777765,22.708508333333331,3.0802053611111107]
[null,"A13","Particulates (PM10)",null,0.24,0.6,3.5866666666666664E-4,null,0.6,3.5866666666666664E-4,null,2.7146188799999998E-3,1.2739839999999997E-2,0.8252919999999998,{"$f":"IFERROR(VLOOKUP(B28,$B$7:J$18,9,FALSE),0)","v":2152},5.308266666666666E-2,1.3987999999999998,0.18973466666666666]
[null,"A1","Nitrogen dioxide",null,0.24,3.8,4.5177777777777772E-4,null,3.8,4.5177777777777772E-4,null,3.4193433599999995E-3,1.6047146666666665E-2,0.88096666666666656,{"$f":"IFERROR(VLOOKUP(B29,$B$7:J$18,9,FALSE),0)","v":428},6.6863111111111109E-2,1.7619333333333331,0.23899044444444442]
[null,"A2","Chromium (VI) compounds (as Cr)",null,0.24,2.9000000000000001E-2,1.4403333333333337E-5,null,2.9000000000000001E-2,1.4403333333333337E-5,null,1.0901364480000001E-4,5.1160640000000009E-4,5.6173000000000015E-2,{"$f":"IFERROR(VLOOKUP(B30,$B$7:J$18,9,FALSE),0)","v":1788},2.1316933333333336E-3,5.6173000000000015E-2,7.6193633333333354E-3]
[null,"A12","Chromium (VI) compounds (as Cr)",null,0.24,0.03,1.8008333333333332E-5,null,0.03,1.8008333333333332E-5,null,1.3629859199999999E-4,6.3965599999999995E-4,7.0232499999999989E-2,{"$f":"IFERROR(VLOOKUP(B31,$B$7:J$18,9,FALSE),0)","v":2161},2.6652333333333331E-3,7.0232499999999989E-2,9.5264083333333333E-3]
[null,"A13","Chromium (VI) compounds (as Cr)",null,0.24,4.1000000000000003E-3,2.4508888888888891E-6,null,4.1000000000000003E-3,2.4508888888888891E-6,null,1.8549895679999998E-5,8.7055573333333336E-5,9.5584666666666679E-3,{"$f":"IFERROR(VLOOKUP(B32,$B$7:J$18,9,FALSE),0)","v":2152},3.6273155555555559E-4,9.5584666666666679E-3,1.2965202222222224E-3]
[null,"A1","Sulphur dioxide  (15 min mean)",null,0.24,4.9000000000000002E-2,{"$f":"F33*O33*1000/1000000/3600","v":5.8255555555555558E-6},null,4.9000000000000002E-2,{"$f":"I33*O33*1000/1000000/3600","v":5.8255555555555558E-6},null,{"$f":"IFERROR(E33*G33/1000000*31536000,0)","v":4.4091532800000003E-5},{"$f":"IF(C33=\"Chloroform\",P33,\nIF(C33=\"Methyl chloroform\",P33,\nIF(C33=\"Naphthalene\",P33,\nIF(C33=\"Tetrachloroethylene\",P33,\nIF(C33=\"Mono-ethanolamine (MEA)\",P33,\nIF(C33=\"Methyl chloride (chloromethane)\",P33,\nIF(C33=\"Chromium (III) compounds (as Cr)\",P33,\nIF(C33=\"Copper and compounds (as Cu)\",P33,\nIF(C33=\"Hydrogen cyanide\",P33,\nIF(C33=\"Mercury and its inorganic compounds (as Hg)\",P33,\nIF(C33=\"Selenium and compounds (as Se), except hydrogen selenide\",P33,\n\nIF(C33=\"Hydrogen fluoride\",R33,\nIF(C33=\"Hydrogen iodide\",R33,\n\nIF(C33=\"Hydrogen fluoride (ecological)\",Q33*0.31,\nIF(C33=\"Styrene\",Q33*0.31,\nIF(C33=\"Toluene\",Q33*0.31,\nP33*E33))))))))))))))))","v":2.0692373333333335E-4},{"$f":"IF(C33=\"1,3-Butadiene\",Q33*0.59,\nIF(C33=\"Benzene\",Q33*0.59,\nIF(C33=\"Cadmium and compounds (as Cd)\",Q33*0.59,\nIF(C33=\"Carbon disulphide\",Q33*0.59,\nIF(C33=\"Methylene chloride (dichloromethane)\",Q33*0.59,\nIF(C33=\"Hydrogen fluoride (ecological)\",Q33*0.59,\nIF(C33=\"Hydrogen sulphide\",Q33*0.59,\nIF(C33=\"Nitrogen oxides (as NO2) (ecological)\",Q33*0.59,\nIF(C33=\"Particulates (PM10)\",Q33*0.59,\nIF(C33=\"Sulphur dioxide (24 hr mean)\",Q33*0.59,\nIF(C33=\"Vanadium and compounds (as V)\",Q33*0.59,\nIF(C33=\"Vinyl chloride\",Q33*0.59,\n\nIF(C33=\"Carbon monoxide\",Q33*0.7,\nIF(C33=\"Ozone\",Q33*0.7,\n\nIF(C33=\"Sulphur dioxide  (15 min mean)\",Q33*1.34,\nIF(C33=\"Formaldehyde\",Q33*1.3,\n\nIF(C33=\"Nitrogen dioxide\",Q33*0.5,\nQ33)))))))))))))))))","v":3.0444353333333337E-2},{"$f":"IFERROR(VLOOKUP(B33,$B$7:J$18,9,FALSE),0)","v":428},8.6218222222222225E-4,2.2719666666666669E-2,3.0817188888888889E-3]
[null,"A2","Sulphur dioxide  (15 min mean)",null,0.24,4.2999999999999997E-2,2.1356666666666665E-5,null,4.2999999999999997E-2,2.1356666666666665E-5,null,1.6164092159999999E-4,7.5858879999999987E-4,0.11160993999999999,{"$f":"IFERROR(VLOOKUP(B34,$B$7:J$18,9,FALSE),0)","v":1788},3.1607866666666664E-3,8.329099999999999E-2,1.1297676666666666E-2]
[null,"A6","Sulphur dioxide  (15 min mean)",null,0.24,0.11,1.313888888888889E-5,null,0.11,1.313888888888889E-5,null,9.9443519999999999E-5,4.6669333333333333E-4,6.8663833333333341E-2,{"$f":"IFERROR(VLOOKUP(B35,$B$7:J$18,9,FALSE),0)","v":430},1.9445555555555557E-3,5.1241666666666671E-2,6.9504722222222225E-3]
[null,"A7","Sulphur dioxide  (15 min mean)",null,0.24,0.24,8.8800000000000004E-5,null,0.24,8.8800000000000004E-5,null,6.7209523199999999E-4,3.1541759999999999E-3,0.46406880000000006,{"$f":"IFERROR(VLOOKUP(B36,$B$7:J$18,9,FALSE),0)","v":1332},1.31424E-2,0.34632000000000002,4.6975200000000002E-2]
[null,"A9","Sulphur dioxide  (15 min mean)",null,0.24,7.2999999999999995E-2,1.6216138888888889E-4,null,7.2999999999999995E-2,1.6216138888888889E-4,null,1.2273411743999999E-3,5.7599725333333327E-3,0.84745541833333338,{"$f":"IFERROR(VLOOKUP(B37,$B$7:J$18,9,FALSE),0)","v":7997},2.3999885555555555E-2,0.63242941666666663,8.5783374722222222E-2]
[null,"A10","Sulphur dioxide  (15 min mean)",null,0.24,0.14000000000000001,1.6893333333333336E-4,null,0.14000000000000001,1.6893333333333336E-4,null,1.2785955840000003E-3,6.0005120000000012E-3,0.88284560000000023,{"$f":"IFERROR(VLOOKUP(B38,$B$7:J$18,9,FALSE),0)","v":4344},2.5002133333333339E-2,0.65884000000000009,8.936573333333335E-2]
[null,"A12","Sulphur dioxide  (15 min mean)",null,0.24,0.12,7.2033333333333327E-5,null,0.12,7.2033333333333327E-5,null,5.4519436799999998E-4,2.5586239999999998E-3,0.37644619999999995,{"$f":"IFERROR(VLOOKUP(B39,$B$7:J$18,9,FALSE),0)","v":2161},1.0660933333333332E-2,0.28092999999999996,3.8105633333333333E-2]
[null,"A13","Sulphur dioxide  (15 min mean)",null,0.24,0.17,1.0162222222222224E-4,null,0.17,1.0162222222222224E-4,null,7.6914201600000016E-4,3.6096213333333339E-3,0.53107773333333352,{"$f":"IFERROR(VLOOKUP(B40,$B$7:J$18,9,FALSE),0)","v":2152},1.5040088888888891E-2,0.39632666666666677,5.3758155555555569E-2]
[null,"A1","Sulphur dioxide (24 hr mean)",null,0.24,4.9000000000000002E-2,5.8255555555555558E-6,null,4.9000000000000002E-2,5.8255555555555558E-6,null,4.4091532800000003E-5,2.0692373333333335E-4,1.3404603333333334E-2,{"$f":"IFERROR(VLOOKUP(B41,$B$7:J$18,9,FALSE),0)","v":428},8.6218222222222225E-4,2.2719666666666669E-2,3.0817188888888889E-3]
[null,"A2","Sulphur dioxide (24 hr mean)",null,0.24,4.2999999999999997E-2,2.1356666666666665E-5,null,4.2999999999999997E-2,2.1356666666666665E-5,null,1.6164092159999999E-4,7.5858879999999987E-4,4.9141689999999995E-2,{"$f":"IFERROR(VLOOKUP(B42,$B$7:J$18,9,FALSE),0)","v":1788},3.1607866666666664E-3,8.329099999999999E-2,1.1297676666666666E-2]
[null,"A6","Sulphur dioxide (24 hr mean)",null,0.24,0.11,1.313888888888889E-5,null,0.11,1.313888888888889E-5,null,9.9443519999999999E-5,4.6669333333333333E-4,3.0232583333333334E-2,{"$f":"IFERROR(VLOOKUP(B43,$B$7:J$18,9,FALSE),0)","v":430},1.9445555555555557E-3,5.1241666666666671E-2,6.9504722222222225E-3]
[null,"A7","Sulphur dioxide (24 hr mean)",null,0.24,0.24,8.8800000000000004E-5,null,0.24,8.8800000000000004E-5,null,6.7209523199999999E-4,3.1541759999999999E-3,0.2043288,{"$f":"IFERROR(VLOOKUP(B44,$B$7:J$18,9,FALSE),0)","v":1332},1.31424E-2,0.34632000000000002,4.6975200000000002E-2]
[null,"A9","Sulphur dioxide (24 hr mean)",null,0.24,7.2999999999999995E-2,1.6216138888888889E-4,null,7.2999999999999995E-2,1.6216138888888889E-4,null,1.2273411743999999E-3,5.7599725333333327E-3,0.37313335583333329,{"$f":"IFERROR(VLOOKUP(B45,$B$7:J$18,9,FALSE),0)","v":7997},2.3999885555555555E-2,0.63242941666666663,8.5783374722222222E-2]
[null,"A10","Sulphur dioxide (24 hr mean)",null,0.24,0.14000000000000001,1.6893333333333336E-4,null,0.14000000000000001,1.6893333333333336E-4,null,1.2785955840000003E-3,6.0005120000000012E-3,0.38871560000000005,{"$f":"IFERROR(VLOOKUP(B46,$B$7:J$18,9,FALSE),0)","v":4344},2.5002133333333339E-2,0.65884000000000009,8.936573333333335E-2]
[null,"A12","Sulphur dioxide (24 hr mean)",null,0.24,0.12,7.2033333333333327E-5,null,0.12,7.2033333333333327E-5,null,5.4519436799999998E-4,2.5586239999999998E-3,0.16574869999999997,{"$f":"IFERROR(VLOOKUP(B47,$B$7:J$18,9,FALSE),0)","v":2161},1.0660933333333332E-2,0.28092999999999996,3.8105633333333333E-2]
[null,"A13","Sulphur dioxide (24 hr mean)",null,0.24,0.17,1.0162222222222224E-4,null,0.17,1.0162222222222224E-4,null,7.6914201600000016E-4,3.6096213333333339E-3,0.23383273333333338,{"$f":"IFERROR(VLOOKUP(B48,$B$7:J$18,9,FALSE),0)","v":2152},1.5040088888888891E-2,0.39632666666666677,5.3758155555555569E-2]
[null,"A1","Nickel and compounds (as Ni) except nickel carbonyl",null,0.24,4.1999999999999997E-3,4.9933333333333333E-7,null,4.1999999999999997E-3,4.9933333333333333E-7,null,3.7792742400000001E-6,1.773632E-5,1.9474E-3,{"$f":"IFERROR(VLOOKUP(B49,$B$7:J$18,9,FALSE),0)","v":428},7.390133333333333E-5,1.9474E-3,2.6414733333333332E-4]
[null,"A10","Nickel and compounds (as Ni) except nickel carbonyl",null,0.24,1.5E-3,1.81E-6,null,1.5E-3,1.81E-6,null,1.36992384E-5,6.4291199999999999E-5,7.0590000000000002E-3,{"$f":"IFERROR(VLOOKUP(B50,$B$7:J$18,9,FALSE),0)","v":4344},2.6788000000000002E-4,7.0590000000000002E-3,9.5748999999999997E-4]
[null,"A1","Benzene",null,0.24,2.9,3.4477777777777778E-4,null,2.9,3.4477777777777778E-4,null,2.60949888E-3,1.2246506666666667E-2,0.7933336666666666,{"$f":"IFERROR(VLOOKUP(B51,$B$7:J$18,9,FALSE),0)","v":428},5.1027111111111113E-2,1.3446333333333333,0.18238744444444444]
[null,"A1","Nitrogen oxides (as NO2) (ecological)",null,0.24,3.8,{"$f":"F52*O52*1000/1000000/3600","v":4.5177777777777772E-4},null,3.8,{"$f":"I52*O52*1000/1000000/3600","v":4.5177777777777772E-4},null,{"$f":"IFERROR(E52*G52/1000000*31536000,0)","v":3.4193433599999995E-3},{"$f":"IF(C52=\"Chloroform\",P52,\nIF(C52=\"Methyl chloroform\",P52,\nIF(C52=\"Naphthalene\",P52,\nIF(C52=\"Tetrachloroethylene\",P52,\nIF(C52=\"Mono-ethanolamine (MEA)\",P52,\nIF(C52=\"Methyl chloride (chloromethane)\",P52,\nIF(C52=\"Chromium (III) compounds (as Cr)\",P52,\nIF(C52=\"Copper and compounds (as Cu)\",P52,\nIF(C52=\"Hydrogen cyanide\",P52,\nIF(C52=\"Mercury and its inorganic compounds (as Hg)\",P52,\nIF(C52=\"Selenium and compounds (as Se), except hydrogen selenide\",P52,\n\nIF(C52=\"Hydrogen fluoride\",R52,\nIF(C52=\"Hydrogen iodide\",R52,\n\nIF(C52=\"Hydrogen fluoride (ecological)\",Q52*0.31,\nIF(C52=\"Styrene\",Q52*0.31,\nIF(C52=\"Toluene\",Q52*0.31,\nP52*E52))))))))))))))))","v":1.6047146666666665E-2},{"$f":"IF(C52=\"1,3-Butadiene\",Q52*0.59,\nIF(C52=\"Benzene\",Q52*0.59,\nIF(C52=\"Cadmium and compounds (as Cd)\",Q52*0.59,\nIF(C52=\"Carbon disulphide\",Q52*0.59,\nIF(C52=\"Methylene chloride (dichloromethane)\",Q52*0.59,\nIF(C52=\"Hydrogen fluoride (ecological)\",Q52*0.59,\nIF(C52=\"Hydrogen sulphide\",Q52*0.59,\nIF(C52=\"Nitrogen oxides (as NO2) (ecological)\",Q52*0.59,\nIF(C52=\"Particulates (PM10)\",Q52*0.59,\nIF(C52=\"Sulphur dioxide (24 hr mean)\",Q52*0.59,\nIF(C52=\"Vanadium and compounds (as V)\",Q52*0.59,\nIF(C52=\"Vinyl chloride\",Q52*0.59,\n\nIF(C52=\"Carbon monoxide\",Q52*0.7,\nIF(C52=\"Ozone\",Q52*0.7,\n\nIF(C52=\"Sulphur dioxide  (15 min mean)\",Q52*1.34,\nIF(C52=\"Formaldehyde\",Q52*1.3,\n\nIF(C52=\"Nitrogen dioxide\",Q52*0.5,\nQ52)))))))))))))))))","v":1.0395406666666664},{"$f":"IFERROR(VLOOKUP(B52,$B$7:J$18,9,FALSE),0)","v":428},{"$f":"IFERROR((VLOOKUP(B52,$B$7:$J$18,5,FALSE))*G52,0)","v":6.6863111111111109E-2},{"$f":"IFERROR(VLOOKUP(B52,$B$7:$J$18,6,FALSE)*J52,0)","v":1.7619333333333331},{"$f":"IFERROR((VLOOKUP(B52,$B$7:$J$18,7,FALSE))*G52,0)","v":0.23899044444444442}]
[null,"A1","Sulphur dioxide (ecological-lichens and bryophytes)",null,0.24,4.9000000000000002E-2,5.8255555555555558E-6,null,4.9000000000000002E-2,5.8255555555555558E-6,null,4.4091532800000003E-5,2.0692373333333335E-4,2.2719666666666669E-2,{"$f":"IFERROR(VLOOKUP(B53,$B$7:J$18,9,FALSE),0)","v":428},8.6218222222222225E-4,2.2719666666666669E-2,3.0817188888888889E-3]
[null,"A2","Sulphur dioxide (ecological-lichens and bryophytes)",null,0.24,4.2999999999999997E-2,2.1356666666666665E-5,null,4.2999999999999997E-2,2.1356666666666665E-5,null,1.6164092159999999E-4,7.5858879999999987E-4,8.329099999999999E-2,{"$f":"IFERROR(VLOOKUP(B54,$B$7:J$18,9,FALSE),0)","v":1788},3.1607866666666664E-3,8.329099999999999E-2,1.1297676666666666E-2]
[null,"A6","Sulphur dioxide (ecological-lichens and bryophytes)",null,0.24,0.11,1.313888888888889E-5,null,0.11,1.313888888888889E-5,null,9.9443519999999999E-5,4.6669333333333333E-4,5.1241666666666671E-2,{"$f":"IFERROR(VLOOKUP(B55,$B$7:J$18,9,FALSE),0)","v":430},1.9445555555555557E-3,5.1241666666666671E-2,6.9504722222222225E-3]
[null,"A7","Sulphur dioxide (ecological-lichens and bryophytes)",null,0.24,0.24,8.8800000000000004E-5,null,0.24,8.8800000000000004E-5,null,6.7209523199999999E-4,3.1541759999999999E-3,0.34632000000000002,{"$f":"IFERROR(VLOOKUP(B56,$B$7:J$18,9,FALSE),0)","v":1332},1.31424E-2,0.34632000000000002,4.6975200000000002E-2]
[null,"A9","Sulphur dioxide (ecological-lichens and bryophytes)",null,0.24,7.2999999999999995E-2,1.6216138888888889E-4,null,7.2999999999999995E-2,1.6216138888888889E-4,null,1.2273411743999999E-3,5.7599725333333327E-3,0.63242941666666663,{"$f":"IFERROR(VLOOKUP(B57,$B$7:J$18,9,FALSE),0)","v":7997},2.3999885555555555E-2,0.63242941666666663,8.5783374722222222E-2]
[null,"A10","Sulphur dioxide (ecological-lichens and bryophytes)",null,0.24,0.14000000000000001,1.6893333333333336E-4,null,0.14000000000000001,1.6893333333333336E-4,null,1.2785955840000003E-3,6.0005120000000012E-3,0.65884000000000009,{"$f":"IFERROR(VLOOKUP(B58,$B$7:J$18,9,FALSE),0)","v":4344},2.5002133333333339E-2,0.65884000000000009,8.936573333333335E-2]
[null,"A12","Sulphur dioxide (ecological-lichens and bryophytes)",null,0.24,0.12,7.2033333333333327E-5,null,0.12,7.2033333333333327E-5,null,5.4519436799999998E-4,2.5586239999999998E-3,0.28092999999999996,{"$f":"IFERROR(VLOOKUP(B59,$B$7:J$18,9,FALSE),0)","v":2161},1.0660933333333332E-2,0.28092999999999996,3.8105633333333333E-2]
[null,"A13","Sulphur dioxide (ecological-lichens and bryophytes)",null,0.24,0.17,1.0162222222222224E-4,null,0.17,1.0162222222222224E-4,null,7.6914201600000016E-4,3.6096213333333339E-3,0.39632666666666677,{"$f":"IFERROR(VLOOKUP(B60,$B$7:J$18,9,FALSE),0)","v":2152},1.5040088888888891E-2,0.39632666666666677,5.3758155555555569E-2]
[null,"A1","Sulphur dioxide (ecological-other vegetation)",null,0.24,4.9000000000000002E-2,5.8255555555555558E-6,null,4.9000000000000002E-2,5.8255555555555558E-6,null,4.4091532800000003E-5,2.0692373333333335E-4,2.2719666666666669E-2,{"$f":"IFERROR(VLOOKUP(B61,$B$7:J$18,9,FALSE),0)","v":428},8.6218222222222225E-4,2.2719666666666669E-2,3.0817188888888889E-3]
[null,"A2","Sulphur dioxide (ecological-other vegetation)",null,0.24,4.2999999999999997E-2,2.1356666666666665E-5,null,4.2999999999999997E-2,2.1356666666666665E-5,null,1.6164092159999999E-4,7.5858879999999987E-4,8.329099999999999E-2,{"$f":"IFERROR(VLOOKUP(B62,$B$7:J$18,9,FALSE),0)","v":1788},3.1607866666666664E-3,8.329099999999999E-2,1.1297676666666666E-2]
[null,"A6","Sulphur dioxide (ecological-other vegetation)",null,0.24,0.11,1.313888888888889E-5,null,0.11,1.313888888888889E-5,null,9.9443519999999999E-5,4.6669333333333333E-4,5.1241666666666671E-2,{"$f":"IFERROR(VLOOKUP(B63,$B$7:J$18,9,FALSE),0)","v":430},1.9445555555555557E-3,5.1241666666666671E-2,6.9504722222222225E-3]
[null,"A7","Sulphur dioxide (ecological-other vegetation)",null,0.24,0.24,8.8800000000000004E-5,null,0.24,8.8800000000000004E-5,null,6.7209523199999999E-4,3.1541759999999999E-3,0.34632000000000002,{"$f":"IFERROR(VLOOKUP(B64,$B$7:J$18,9,FALSE),0)","v":1332},1.31424E-2,0.34632000000000002,4.6975200000000002E-2]
[null,"A9","Sulphur dioxide (ecological-other vegetation)",null,0.24,7.2999999999999995E-2,1.6216138888888889E-4,null,7.2999999999999995E-2,1.6216138888888889E-4,null,1.2273411743999999E-3,5.7599725333333327E-3,0.63242941666666663,{"$f":"IFERROR(VLOOKUP(B65,$B$7:J$18,9,FALSE),0)","v":7997},2.3999885555555555E-2,0.63242941666666663,8.5783374722222222E-2]
[null,"A10","Sulphur dioxide (ecological-other vegetation)",null,0.24,0.14000000000000001,1.6893333333333336E-4,null,0.14000000000000001,1.6893333333333336E-4,null,1.2785955840000003E-3,6.0005120000000012E-3,0.65884000000000009,{"$f":"IFERROR(VLOOKUP(B66,$B$7:J$18,9,FALSE),0)","v":4344},2.5002133333333339E-2,0.65884000000000009,8.936573333333335E-2]
[null,"A12","Sulphur dioxide (ecological-other vegetation)",null,0.24,0.12,7.2033333333333327E-5,null,0.12,7.2033333333333327E-5,null,5.4519436799999998E-4,2.5586239999999998E-3,0.28092999999999996,{"$f":"IFERROR(VLOOKUP(B67,$B$7:J$18,9,FALSE),0)","v":2161},1.0660933333333332E-2,0.28092999999999996,3.8105633333333333E-2]
[null,"A13","Sulphur dioxide (ecological-other vegetation)",null,0.24,0.17,1.0162222222222224E-4,null,0.17,1.0162222222222224E-4,null,7.6914201600000016E-4,3.6096213333333339E-3,0.39632666666666677,{"$f":"IFERROR(VLOOKUP(B68,$B$7:J$18,9,FALSE),0)","v":2152},1.5040088888888891E-2,0.39632666666666677,5.3758155555555569E-2]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,{"$f":"IFERROR(VLOOKUP(B69,$B$16:$I$17,6,FALSE)*J69,0)","v":0}]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,0]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,0]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,0]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,0]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,0]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,0]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,0]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,0]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,0]
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[]
[]
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{"sheet":"1Ao1","index":15,"n_rows":95,"n_cols":10,"rows_kept":95,"cut":false,"hidden":false,"merged":[[0,7,0,8]]}
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["Environmental Assessment"]
[]
[null,null,"Number","Substance","Long term EAL (ug/m3)","Long term PC (ug/m3)","Long term modelled PC","Short term EAL (ug/m3)","Short term PC (ug/m3)","Short term modelled PC"]
[null,null,1,"Particulates (PM10)",{"$f":"IFERROR(VLOOKUP(_Air74227[[#This Row],[Substance]],SubstancesA!$B$7:$V$114,2,FALSE),\"\")","v":40},0.8790148213333332,null,{"$f":"IFERROR(VLOOKUP(_Air74227[[#This Row],[Substance]],SubstancesA!$B$7:$V$114,3,FALSE),\"\")","v":50},56.94293648333332]
[null,null,2,"Nitrogen dioxide",{"$f":"IFERROR(VLOOKUP(_Air74227[[#This Row],[Substance]],SubstancesA!$B$7:$V$114,2,FALSE),\"\")","v":40},1.6047146666666665E-2,null,{"$f":"IFERROR(VLOOKUP(_Air74227[[#This Row],[Substance]],SubstancesA!$B$7:$V$114,3,FALSE),\"\")","v":200},0.88096666666666656]
[null,null,3,"Chromium (VI) compounds (as Cr)",{"$f":"IFERROR(VLOOKUP(_Air74227[[#This Row],[Substance]],SubstancesA!$B$7:$V$114,2,FALSE),\"\")","v":2.5000000000000001E-4},1.2383179733333333E-3,null,{"$f":"IFERROR(VLOOKUP(_Air74227[[#This Row],[Substance]],SubstancesA!$B$7:$V$114,3,FALSE),\"\")","v":0},0.13596396666666666]
[null,null,4,"Sulphur dioxide  (15 min mean)",{"$f":"IFERROR(VLOOKUP(_Air74227[[#This Row],[Substance]],SubstancesA!$B$7:$V$114,2,FALSE),\"\")","v":0},2.2515111733333332E-2,null,{"$f":"IFERROR(VLOOKUP(_Air74227[[#This Row],[Substance]],SubstancesA!$B$7:$V$114,3,FALSE),\"\")","v":266},3.3126118783333336]
[null,null,5,"Sulphur dioxide (24 hr mean)",{"$f":"IFERROR(VLOOKUP(_Air74227[[#This Row],[Substance]],SubstancesA!$B$7:$V$114,2,FALSE),\"\")","v":0},2.2515111733333332E-2,null,{"$f":"IFERROR(VLOOKUP(_Air74227[[#This Row],[Substance]],SubstancesA!$B$7:$V$114,3,FALSE),\"\")","v":125},1.4585380658333336]
[null,null,6,"Nickel and compounds (as Ni) except nickel carbonyl",{"$f":"IFERROR(VLOOKUP(_Air74227[[#This Row],[Substance]],SubstancesA!$B$7:$V$114,2,FALSE),\"\")","v":0.02},8.2027520000000002E-5,null,{"$f":"IFERROR(VLOOKUP(_Air74227[[#This Row],[Substance]],SubstancesA!$B$7:$V$114,3,FALSE),\"\")","v":0.7},9.0063999999999995E-3]
[null,null,7,"Benzene",{"$f":"IFERROR(VLOOKUP(_Air74227[[#This Row],[Substance]],SubstancesA!$B$7:$V$114,2,FALSE),\"\")","v":5},1.2246506666666667E-2,null,{"$f":"IFERROR(VLOOKUP(_Air74227[[#This Row],[Substance]],SubstancesA!$B$7:$V$114,3,FALSE),\"\")","v":30},0.7933336666666666]
[null,null,8,"Nitrogen oxides (as NO2) (ecological)",{"$f":"IFERROR(VLOOKUP(_Air74227[[#This Row],[Substance]],SubstancesA!$B$7:$V$114,2,FALSE),\"\")","v":30},1.6047146666666665E-2,null,{"$f":"IFERROR(VLOOKUP(_Air74227[[#This Row],[Substance]],SubstancesA!$B$7:$V$114,3,FALSE),\"\")","v":75},1.0395406666666664]
[null,null,9,"Sulphur dioxide (ecological-lichens and bryophytes)",{"$f":"IFERROR(VLOOKUP(_Air74227[[#This Row],[Substance]],SubstancesA!$B$7:$V$114,2,FALSE),\"\")","v":10},2.2515111733333332E-2,null,{"$f":"IFERROR(VLOOKUP(_Air74227[[#This Row],[Substance]],SubstancesA!$B$7:$V$114,3,FALSE),\"\")","v":0},2.4720984166666669]
[null,null,10,"Sulphur dioxide (ecological-other vegetation)",{"$f":"IFERROR(VLOOKUP(_Air74227[[#This Row],[Substance]],SubstancesA!$B$7:$V$114,2,FALSE),\"\")","v":20},2.2515111733333332E-2,null,{"$f":"IFERROR(VLOOKUP(_Air74227[[#This Row],[Substance]],SubstancesA!$B$7:$V$114,3,FALSE),\"\")","v":0},2.4720984166666669]
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{"sheet":"1Ao2","index":16,"n_rows":98,"n_cols":12,"rows_kept":98,"cut":false,"hidden":false,"merged":[[0,7,0,8]]}
[]
["Environmental Assessment"]
[]
[null,null,"Number","Substance","Long term EAL (ug/m3)","Long term PC (ug/m3)","%PC of EAL (long term)",">1% of EAL? (long term)","Short term EAL (ug/m3)","Short term PC (ug/m3)","%PC of EAL (short term)",">10% of EAL? (short term)"]
[null,null,1,"Particulates (PM10)",{"$f":"IF(_Air7354328[[#This Row],[Substance]]<>\"\",(IFERROR(VLOOKUP(\"*\"&'Reference information'!$E$14&\"*\"&_Air7354328[[#This Row],[Substance]],SubstancesA,3,FALSE),\"\")),\"\")","v":40},0.8790148213333332,{"$f":"IFERROR(_Air7354328[[#This Row],[Long term PC (ug/m3)]]/_Air7354328[[#This Row],[Long term EAL (ug/m3)]],\"\")","v":2.197537053333333E-2},{"$f":"IF(ISNUMBER(_Air7354328[[#This Row],[%PC of EAL (long term)]]),IF(_Air7354328[[#This Row],[%PC of EAL (long term)]]>0.01,\"fail\",\"pass\"),\"\")","v":"fail"},{"$f":"IFERROR(VLOOKUP(_Air7354328[[#This Row],[Substance]],_Air74227[[Substance]:[Short term PC (ug/m3)]],5,FALSE),\"\")","v":50},56.94293648333332,{"$f":"IFERROR(_Air7354328[[#This Row],[Short term PC (ug/m3)]]/_Air7354328[[#This Row],[Short term EAL (ug/m3)]],\"\")","v":1.1388587296666663},{"$f":"IF(ISNUMBER(_Air7354328[[#This Row],[%PC of EAL (short term)]]),IF(_Air7354328[[#This Row],[%PC of EAL (short term)]]>0.1,\"fail\",\"pass\"),\"\")","v":"fail"}]
[null,null,2,"Nitrogen dioxide",{"$f":"IF(_Air7354328[[#This Row],[Substance]]<>\"\",(IFERROR(VLOOKUP(\"*\"&'Reference information'!$E$14&\"*\"&_Air7354328[[#This Row],[Substance]],SubstancesA,3,FALSE),\"\")),\"\")","v":40},1.6047146666666665E-2,{"$f":"IFERROR(_Air7354328[[#This Row],[Long term PC (ug/m3)]]/_Air7354328[[#This Row],[Long term EAL (ug/m3)]],\"\")","v":4.0117866666666661E-4},{"$f":"IF(ISNUMBER(_Air7354328[[#This Row],[%PC of EAL (long term)]]),IF(_Air7354328[[#This Row],[%PC of EAL (long term)]]>0.01,\"fail\",\"pass\"),\"\")","v":"pass"},{"$f":"IFERROR(VLOOKUP(_Air7354328[[#This Row],[Substance]],_Air74227[[Substance]:[Short term PC (ug/m3)]],5,FALSE),\"\")","v":200},0.88096666666666656,{"$f":"IFERROR(_Air7354328[[#This Row],[Short term PC (ug/m3)]]/_Air7354328[[#This Row],[Short term EAL (ug/m3)]],\"\")","v":4.4048333333333326E-3},{"$f":"IF(ISNUMBER(_Air7354328[[#This Row],[%PC of EAL (short term)]]),IF(_Air7354328[[#This Row],[%PC of EAL (short term)]]>0.1,\"fail\",\"pass\"),\"\")","v":"pass"}]
[null,null,3,"Chromium (VI) compounds (as Cr)",{"$f":"IF(_Air7354328[[#This Row],[Substance]]<>\"\",(IFERROR(VLOOKUP(\"*\"&'Reference information'!$E$14&\"*\"&_Air7354328[[#This Row],[Substance]],SubstancesA,3,FALSE),\"\")),\"\")","v":2.5000000000000001E-4},1.2383179733333333E-3,{"$f":"IFERROR(_Air7354328[[#This Row],[Long term PC (ug/m3)]]/_Air7354328[[#This Row],[Long term EAL (ug/m3)]],\"\")","v":4.9532718933333326},{"$f":"IF(ISNUMBER(_Air7354328[[#This Row],[%PC of EAL (long term)]]),IF(_Air7354328[[#This Row],[%PC of EAL (long term)]]>0.01,\"fail\",\"pass\"),\"\")","v":"fail"},{"$f":"IFERROR(VLOOKUP(_Air7354328[[#This Row],[Substance]],_Air74227[[Substance]:[Short term PC (ug/m3)]],5,FALSE),\"\")","v":0},0.13596396666666666,{"$f":"IFERROR(_Air7354328[[#This Row],[Short term PC (ug/m3)]]/_Air7354328[[#This Row],[Short term EAL (ug/m3)]],\"\")","v":""},{"$f":"IF(ISNUMBER(_Air7354328[[#This Row],[%PC of EAL (short term)]]),IF(_Air7354328[[#This Row],[%PC of EAL (short term)]]>0.1,\"fail\",\"pass\"),\"\")","v":""}]
[null,null,4,"Sulphur dioxide  (15 min mean)",{"$f":"IF(_Air7354328[[#This Row],[Substance]]<>\"\",(IFERROR(VLOOKUP(\"*\"&'Reference information'!$E$14&\"*\"&_Air7354328[[#This Row],[Substance]],SubstancesA,3,FALSE),\"\")),\"\")","v":0},2.2515111733333332E-2,{"$f":"IFERROR(_Air7354328[[#This Row],[Long term PC (ug/m3)]]/_Air7354328[[#This Row],[Long term EAL (ug/m3)]],\"\")","v":""},{"$f":"IF(ISNUMBER(_Air7354328[[#This Row],[%PC of EAL (long term)]]),IF(_Air7354328[[#This Row],[%PC of EAL (long term)]]>0.01,\"fail\",\"pass\"),\"\")","v":""},{"$f":"IFERROR(VLOOKUP(_Air7354328[[#This Row],[Substance]],_Air74227[[Substance]:[Short term PC (ug/m3)]],5,FALSE),\"\")","v":266},3.3126118783333336,{"$f":"IFERROR(_Air7354328[[#This Row],[Short term PC (ug/m3)]]/_Air7354328[[#This Row],[Short term EAL (ug/m3)]],\"\")","v":1.2453428114035089E-2},{"$f":"IF(ISNUMBER(_Air7354328[[#This Row],[%PC of EAL (short term)]]),IF(_Air7354328[[#This Row],[%PC of EAL (short term)]]>0.1,\"fail\",\"pass\"),\"\")","v":"pass"}]
[null,null,5,"Sulphur dioxide (24 hr mean)",{"$f":"IF(_Air7354328[[#This Row],[Substance]]<>\"\",(IFERROR(VLOOKUP(\"*\"&'Reference information'!$E$14&\"*\"&_Air7354328[[#This Row],[Substance]],SubstancesA,3,FALSE),\"\")),\"\")","v":0},2.2515111733333332E-2,{"$f":"IFERROR(_Air7354328[[#This Row],[Long term PC (ug/m3)]]/_Air7354328[[#This Row],[Long term EAL (ug/m3)]],\"\")","v":""},{"$f":"IF(ISNUMBER(_Air7354328[[#This Row],[%PC of EAL (long term)]]),IF(_Air7354328[[#This Row],[%PC of EAL (long term)]]>0.01,\"fail\",\"pass\"),\"\")","v":""},{"$f":"IFERROR(VLOOKUP(_Air7354328[[#This Row],[Substance]],_Air74227[[Substance]:[Short term PC (ug/m3)]],5,FALSE),\"\")","v":125},1.4585380658333336,{"$f":"IFERROR(_Air7354328[[#This Row],[Short term PC (ug/m3)]]/_Air7354328[[#This Row],[Short term EAL (ug/m3)]],\"\")","v":1.1668304526666668E-2},{"$f":"IF(ISNUMBER(_Air7354328[[#This Row],[%PC of EAL (short term)]]),IF(_Air7354328[[#This Row],[%PC of EAL (short term)]]>0.1,\"fail\",\"pass\"),\"\")","v":"pass"}]
[null,null,6,"Nickel and compounds (as Ni) except nickel carbonyl",{"$f":"IF(_Air7354328[[#This Row],[Substance]]<>\"\",(IFERROR(VLOOKUP(\"*\"&'Reference information'!$E$14&\"*\"&_Air7354328[[#This Row],[Substance]],SubstancesA,3,FALSE),\"\")),\"\")","v":0.02},8.2027520000000002E-5,{"$f":"IFERROR(_Air7354328[[#This Row],[Long term PC (ug/m3)]]/_Air7354328[[#This Row],[Long term EAL (ug/m3)]],\"\")","v":4.1013760000000003E-3},{"$f":"IF(ISNUMBER(_Air7354328[[#This Row],[%PC of EAL (long term)]]),IF(_Air7354328[[#This Row],[%PC of EAL (long term)]]>0.01,\"fail\",\"pass\"),\"\")","v":"pass"},{"$f":"IFERROR(VLOOKUP(_Air7354328[[#This Row],[Substance]],_Air74227[[Substance]:[Short term PC (ug/m3)]],5,FALSE),\"\")","v":0.7},9.0063999999999995E-3,{"$f":"IFERROR(_Air7354328[[#This Row],[Short term PC (ug/m3)]]/_Air7354328[[#This Row],[Short term EAL (ug/m3)]],\"\")","v":1.2866285714285714E-2},{"$f":"IF(ISNUMBER(_Air7354328[[#This Row],[%PC of EAL (short term)]]),IF(_Air7354328[[#This Row],[%PC of EAL (short term)]]>0.1,\"fail\",\"pass\"),\"\")","v":"pass"}]
[null,null,7,"Benzene",{"$f":"IF(_Air7354328[[#This Row],[Substance]]<>\"\",(IFERROR(VLOOKUP(\"*\"&'Reference information'!$E$14&\"*\"&_Air7354328[[#This Row],[Substance]],SubstancesA,3,FALSE),\"\")),\"\")","v":5},1.2246506666666667E-2,{"$f":"IFERROR(_Air7354328[[#This Row],[Long term PC (ug/m3)]]/_Air7354328[[#This Row],[Long term EAL (ug/m3)]],\"\")","v":2.4493013333333332E-3},{"$f":"IF(ISNUMBER(_Air7354328[[#This Row],[%PC of EAL (long term)]]),IF(_Air7354328[[#This Row],[%PC of EAL (long term)]]>0.01,\"fail\",\"pass\"),\"\")","v":"pass"},{"$f":"IFERROR(VLOOKUP(_Air7354328[[#This Row],[Substance]],_Air74227[[Substance]:[Short term PC (ug/m3)]],5,FALSE),\"\")","v":30},0.7933336666666666,{"$f":"IFERROR(_Air7354328[[#This Row],[Short term PC (ug/m3)]]/_Air7354328[[#This Row],[Short term EAL (ug/m3)]],\"\")","v":2.6444455555555555E-2},{"$f":"IF(ISNUMBER(_Air7354328[[#This Row],[%PC of EAL (short term)]]),IF(_Air7354328[[#This Row],[%PC of EAL (short term)]]>0.1,\"fail\",\"pass\"),\"\")","v":"pass"}]
[null,null,8,"Nitrogen oxides (as NO2) (ecological)",{"$f":"IF(_Air7354328[[#This Row],[Substance]]<>\"\",(IFERROR(VLOOKUP(\"*\"&'Reference information'!$E$14&\"*\"&_Air7354328[[#This Row],[Substance]],SubstancesA,3,FALSE),\"\")),\"\")","v":30},1.6047146666666665E-2,{"$f":"IFERROR(_Air7354328[[#This Row],[Long term PC (ug/m3)]]/_Air7354328[[#This Row],[Long term EAL (ug/m3)]],\"\")","v":5.3490488888888882E-4},{"$f":"IF(ISNUMBER(_Air7354328[[#This Row],[%PC of EAL (long term)]]),IF(_Air7354328[[#This Row],[%PC of EAL (long term)]]>0.01,\"fail\",\"pass\"),\"\")","v":"pass"},{"$f":"IFERROR(VLOOKUP(_Air7354328[[#This Row],[Substance]],_Air74227[[Substance]:[Short term PC (ug/m3)]],5,FALSE),\"\")","v":75},1.0395406666666664,{"$f":"IFERROR(_Air7354328[[#This Row],[Short term PC (ug/m3)]]/_Air7354328[[#This Row],[Short term EAL (ug/m3)]],\"\")","v":1.386054222222222E-2},{"$f":"IF(ISNUMBER(_Air7354328[[#This Row],[%PC of EAL (short term)]]),IF(_Air7354328[[#This Row],[%PC of EAL (short term)]]>0.1,\"fail\",\"pass\"),\"\")","v":"pass"}]
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[]
["Environmental Assessment"]
[]
[null,null,"Number","Substance","Long term EAL (ug/m3)","Long term PC (ug/m3)","Air Background conc (ug/m3)","%PC of headroom (long term)","PEC Long term (µg/m3)","%PEC of EAL% (Long term)","%PEC of EAL>70%? (long term)","Short term EAL (ug/m3)","Short term PC (ug/m3)"," %PC of the EAL-2*background","%PC of headroom >=20%? (short term)"]
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{"sheet":"1Ao5","index":18,"n_rows":198,"n_cols":7,"rows_kept":198,"cut":false,"hidden":false,"merged":[[0,7,0,8]]}
[]
["Environmental Assessment"]
[]
[null,null,"Number","Substance","Annual rate (tonne/yr))","POCP value per tonne","POCP"]
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[null,null,97,"Tetrachloroethylene (24h mean)",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":"No POCP value"},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":""}]
[null,null,98,"Toluene",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":63.7},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":304.33974480000001}]
[null,null,99,"Vanadium (24h mean)",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":"No POCP value"},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":""}]
[null,null,100,"Vinyl chloride (24h mean)",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":"No POCP value"},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":""}]
[null,null,101,"Styrene",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":14.2},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":67.843396799999994}]
[null,null,102,"Sulphur Dioxide  (15 Min Mean)",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":"No POCP value"},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":""}]
[null,null,103,"Tetrachloroethylene (24h mean)",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":"No POCP value"},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":""}]
[null,null,104,"Toluene",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":63.7},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":304.33974480000001}]
[null,null,105,"Vanadium (24h mean)",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":"No POCP value"},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":""}]
[null,null,106,"Vinyl chloride (24h mean)",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":"No POCP value"},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":""}]
[null,null,107,"Styrene",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":14.2},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":67.843396799999994}]
[null,null,108,"Sulphur Dioxide  (15 Min Mean)",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":"No POCP value"},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":""}]
[null,null,109,"Tetrachloroethylene (24h mean)",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":"No POCP value"},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":""}]
[null,null,110,"Toluene",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":63.7},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":304.33974480000001}]
[null,null,111,"Vanadium (24h mean)",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":"No POCP value"},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":""}]
[null,null,112,"Vinyl chloride (24h mean)",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":"No POCP value"},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":""}]
[null,null,113,"Styrene",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":14.2},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":67.843396799999994}]
[null,null,114,"Sulphur Dioxide  (15 Min Mean)",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":"No POCP value"},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":""}]
[null,null,115,"Tetrachloroethylene (24h mean)",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":"No POCP value"},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":""}]
[null,null,116,"Toluene",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":63.7},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":304.33974480000001}]
[null,null,117,"Vanadium (24h mean)",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":"No POCP value"},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":""}]
[null,null,118,"Vinyl chloride (24h mean)",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":"No POCP value"},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":""}]
[null,null,119,"Styrene",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":14.2},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":67.843396799999994}]
[null,null,120,"Sulphur Dioxide  (15 Min Mean)",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":"No POCP value"},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":""}]
[null,null,121,"Tetrachloroethylene (24h mean)",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":"No POCP value"},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":""}]
[null,null,122,"Toluene",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":63.7},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":304.33974480000001}]
[null,null,123,"Vanadium (24h mean)",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":"No POCP value"},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":""}]
[null,null,124,"Vinyl chloride (24h mean)",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":"No POCP value"},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":""}]
[null,null,125,"Styrene",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":14.2},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":67.843396799999994}]
[null,null,126,"Sulphur Dioxide  (15 Min Mean)",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":"No POCP value"},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":""}]
[null,null,127,"Tetrachloroethylene (24h mean)",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":"No POCP value"},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":""}]
[null,null,128,"Toluene",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":63.7},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":304.33974480000001}]
[null,null,129,"Vanadium (24h mean)",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":"No POCP value"},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":""}]
[null,null,130,"Vinyl chloride (24h mean)",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":"No POCP value"},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":""}]
[null,null,131,"Styrene",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":14.2},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":67.843396799999994}]
[null,null,132,"Sulphur Dioxide  (15 Min Mean)",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":"No POCP value"},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":""}]
[null,null,133,"Tetrachloroethylene (24h mean)",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":"No POCP value"},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":""}]
[null,null,134,"Toluene",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":63.7},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":304.33974480000001}]
[null,null,135,"Vanadium (24h mean)",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":"No POCP value"},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":""}]
[null,null,136,"Vinyl chloride (24h mean)",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":"No POCP value"},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":""}]
[null,null,137,"Styrene",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":14.2},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":67.843396799999994}]
[null,null,138,"Sulphur Dioxide  (15 Min Mean)",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":"No POCP value"},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":""}]
[null,null,139,"Tetrachloroethylene (24h mean)",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":"No POCP value"},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":""}]
[null,null,140,"Toluene",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":63.7},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":304.33974480000001}]
[null,null,141,"Vanadium (24h mean)",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":"No POCP value"},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":""}]
[null,null,142,"Vinyl chloride (24h mean)",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":"No POCP value"},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":""}]
[null,null,143,"Styrene",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":14.2},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":67.843396799999994}]
[null,null,144,"Sulphur Dioxide  (15 Min Mean)",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":"No POCP value"},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":""}]
[null,null,145,"Tetrachloroethylene (24h mean)",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":"No POCP value"},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":""}]
[null,null,146,"Toluene",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":63.7},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":304.33974480000001}]
[null,null,147,"Vanadium (24h mean)",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":"No POCP value"},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":""}]
[null,null,148,"Vinyl chloride (24h mean)",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":"No POCP value"},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":""}]
[null,null,149,"Styrene",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":14.2},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":67.843396799999994}]
[null,null,150,"Sulphur Dioxide  (15 Min Mean)",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":"No POCP value"},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":""}]
[null,null,151,"Tetrachloroethylene (24h mean)",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":"No POCP value"},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":""}]
[null,null,152,"Toluene",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":63.7},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":304.33974480000001}]
[null,null,153,"Vanadium (24h mean)",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":"No POCP value"},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":""}]
[null,null,154,"Vinyl chloride (24h mean)",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":"No POCP value"},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":""}]
[null,null,155,"Styrene",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":14.2},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":67.843396799999994}]
[null,null,156,"Sulphur Dioxide  (15 Min Mean)",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":"No POCP value"},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":""}]
[null,null,157,"Tetrachloroethylene (24h mean)",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":"No POCP value"},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":""}]
[null,null,158,"Toluene",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":63.7},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":304.33974480000001}]
[null,null,159,"Vanadium (24h mean)",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":"No POCP value"},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":""}]
[null,null,160,"Vinyl chloride (24h mean)",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":"No POCP value"},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":""}]
[null,null,161,"Styrene",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":14.2},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":67.843396799999994}]
[null,null,162,"Sulphur Dioxide  (15 Min Mean)",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":"No POCP value"},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":""}]
[null,null,163,"Tetrachloroethylene (24h mean)",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":"No POCP value"},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":""}]
[null,null,164,"Toluene",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":63.7},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":304.33974480000001}]
[null,null,165,"Vanadium (24h mean)",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":"No POCP value"},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":""}]
[null,null,166,"Vinyl chloride (24h mean)",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":"No POCP value"},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":""}]
[null,null,167,"Styrene",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":14.2},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":67.843396799999994}]
[null,null,168,"Sulphur Dioxide  (15 Min Mean)",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":"No POCP value"},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":""}]
[null,null,169,"Tetrachloroethylene (24h mean)",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":"No POCP value"},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":""}]
[null,null,170,"Toluene",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":63.7},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":304.33974480000001}]
[null,null,171,"Vanadium (24h mean)",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":"No POCP value"},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":""}]
[null,null,172,"Vinyl chloride (24h mean)",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":"No POCP value"},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":""}]
[null,null,173,"Styrene",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":14.2},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":67.843396799999994}]
[null,null,174,"Sulphur Dioxide  (15 Min Mean)",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":"No POCP value"},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":""}]
[null,null,175,"Tetrachloroethylene (24h mean)",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":"No POCP value"},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":""}]
[null,null,176,"Toluene",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":63.7},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":304.33974480000001}]
[null,null,177,"Vanadium (24h mean)",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":"No POCP value"},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":""}]
[null,null,178,"Vinyl chloride (24h mean)",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":"No POCP value"},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":""}]
[null,null,179,"Styrene",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":14.2},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":67.843396799999994}]
[null,null,180,"Sulphur Dioxide  (15 Min Mean)",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":"No POCP value"},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":""}]
[null,null,181,"Tetrachloroethylene (24h mean)",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":"No POCP value"},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":""}]
[null,null,182,"Toluene",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":63.7},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":304.33974480000001}]
[null,null,183,"Vanadium (24h mean)",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":"No POCP value"},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":""}]
[null,null,184,"Vinyl chloride (24h mean)",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":"No POCP value"},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":""}]
[null,null,185,"Styrene",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":14.2},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":67.843396799999994}]
[null,null,186,"Sulphur Dioxide  (15 Min Mean)",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":"No POCP value"},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":""}]
[null,null,187,"Tetrachloroethylene (24h mean)",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":"No POCP value"},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":""}]
[null,null,188,"Toluene",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":63.7},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":304.33974480000001}]
[null,null,189,"Vanadium (24h mean)",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":"No POCP value"},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":""}]
[null,null,190,"Vinyl chloride (24h mean)",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":"No POCP value"},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":""}]
[null,null,191,"Styrene",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":14.2},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":67.843396799999994}]
[null,null,192,"Sulphur Dioxide  (15 Min Mean)",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":"No POCP value"},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":""}]
[null,null,193,"Tetrachloroethylene (24h mean)",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":"No POCP value"},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":""}]
[null,null,194,"Toluene",4.777704,{"$f":"IF(ISBLANK(_Air735363724637[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE)),VLOOKUP(_Air735363724637[[#This Row],[Substance]],SubstancesA!$B$6:$V$334,6,FALSE),\"No POCP value\"))","v":63.7},{"$f":"IF(ISNUMBER(_Air735363724637[[#This Row],[POCP value per tonne]]),_Air735363724637[[#This Row],[Annual rate (tonne/yr))]]*_Air735363724637[[#This Row],[POCP value per tonne]],\"\")","v":304.33974480000001}]

{"sheet":"1Ao4","index":19,"n_rows":98,"n_cols":7,"rows_kept":98,"cut":false,"hidden":true,"merged":[[0,7,0,8]]}
[]
["Environmental Assessment"]
[]
[null,null,"Number","Substance","%PC of EAL (long term)","Insignificant?","Commentary"]
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[null,null,null,null,null,{"$f":"IF(ISNUMBER(_Air73536374536[[#This Row],[%PC of EAL (long term)]]),IF(_Air73536374536[[#This Row],[%PC of EAL (long term)]]>1,\"No\",\"Yes\"),\"\")","v":""}]
[null,null,null,null,null,{"$f":"IF(ISNUMBER(_Air73536374536[[#This Row],[%PC of EAL (long term)]]),IF(_Air73536374536[[#This Row],[%PC of EAL (long term)]]>1,\"No\",\"Yes\"),\"\")","v":""}]
[null,null,null,null,null,{"$f":"IF(ISNUMBER(_Air73536374536[[#This Row],[%PC of EAL (long term)]]),IF(_Air73536374536[[#This Row],[%PC of EAL (long term)]]>1,\"No\",\"Yes\"),\"\")","v":""}]
[null,null,null,null,null,{"$f":"IF(ISNUMBER(_Air73536374536[[#This Row],[%PC of EAL (long term)]]),IF(_Air73536374536[[#This Row],[%PC of EAL (long term)]]>1,\"No\",\"Yes\"),\"\")","v":""}]
[null,null,null,null,null,{"$f":"IF(ISNUMBER(_Air73536374536[[#This Row],[%PC of EAL (long term)]]),IF(_Air73536374536[[#This Row],[%PC of EAL (long term)]]>1,\"No\",\"Yes\"),\"\")","v":""}]
[null,null,null,null,null,{"$f":"IF(ISNUMBER(_Air73536374536[[#This Row],[%PC of EAL (long term)]]),IF(_Air73536374536[[#This Row],[%PC of EAL (long term)]]>1,\"No\",\"Yes\"),\"\")","v":""}]
[null,null,null,null,null,{"$f":"IF(ISNUMBER(_Air73536374536[[#This Row],[%PC of EAL (long term)]]),IF(_Air73536374536[[#This Row],[%PC of EAL (long term)]]>1,\"No\",\"Yes\"),\"\")","v":""}]
[null,null,null,null,null,{"$f":"IF(ISNUMBER(_Air73536374536[[#This Row],[%PC of EAL (long term)]]),IF(_Air73536374536[[#This Row],[%PC of EAL (long term)]]>1,\"No\",\"Yes\"),\"\")","v":""}]
[null,null,null,null,null,{"$f":"IF(ISNUMBER(_Air73536374536[[#This Row],[%PC of EAL (long term)]]),IF(_Air73536374536[[#This Row],[%PC of EAL (long term)]]>1,\"No\",\"Yes\"),\"\")","v":""}]
[null,null,null,null,null,{"$f":"IF(ISNUMBER(_Air73536374536[[#This Row],[%PC of EAL (long term)]]),IF(_Air73536374536[[#This Row],[%PC of EAL (long term)]]>1,\"No\",\"Yes\"),\"\")","v":""}]
[null,null,null,null,null,{"$f":"IF(ISNUMBER(_Air73536374536[[#This Row],[%PC of EAL (long term)]]),IF(_Air73536374536[[#This Row],[%PC of EAL (long term)]]>1,\"No\",\"Yes\"),\"\")","v":""}]
[null,null,null,null,null,{"$f":"IF(ISNUMBER(_Air73536374536[[#This Row],[%PC of EAL (long term)]]),IF(_Air73536374536[[#This Row],[%PC of EAL (long term)]]>1,\"No\",\"Yes\"),\"\")","v":""}]
[null,null,null,null,null,{"$f":"IF(ISNUMBER(_Air73536374536[[#This Row],[%PC of EAL (long term)]]),IF(_Air73536374536[[#This Row],[%PC of EAL (long term)]]>1,\"No\",\"Yes\"),\"\")","v":""}]
[null,null,null,null,null,{"$f":"IF(ISNUMBER(_Air73536374536[[#This Row],[%PC of EAL (long term)]]),IF(_Air73536374536[[#This Row],[%PC of EAL (long term)]]>1,\"No\",\"Yes\"),\"\")","v":""}]
[null,null,null,null,null,{"$f":"IF(ISNUMBER(_Air73536374536[[#This Row],[%PC of EAL (long term)]]),IF(_Air73536374536[[#This Row],[%PC of EAL (long term)]]>1,\"No\",\"Yes\"),\"\")","v":""}]
[null,null,null,null,null,{"$f":"IF(ISNUMBER(_Air73536374536[[#This Row],[%PC of EAL (long term)]]),IF(_Air73536374536[[#This Row],[%PC of EAL (long term)]]>1,\"No\",\"Yes\"),\"\")","v":""}]
[null,null,null,null,null,{"$f":"IF(ISNUMBER(_Air73536374536[[#This Row],[%PC of EAL (long term)]]),IF(_Air73536374536[[#This Row],[%PC of EAL (long term)]]>1,\"No\",\"Yes\"),\"\")","v":""}]
[null,null,null,null,null,{"$f":"IF(ISNUMBER(_Air73536374536[[#This Row],[%PC of EAL (long term)]]),IF(_Air73536374536[[#This Row],[%PC of EAL (long term)]]>1,\"No\",\"Yes\"),\"\")","v":""}]
[null,null,null,null,null,{"$f":"IF(ISNUMBER(_Air73536374536[[#This Row],[%PC of EAL (long term)]]),IF(_Air73536374536[[#This Row],[%PC of EAL (long term)]]>1,\"No\",\"Yes\"),\"\")","v":""}]
[null,null,null,null,null,{"$f":"IF(ISNUMBER(_Air73536374536[[#This Row],[%PC of EAL (long term)]]),IF(_Air73536374536[[#This Row],[%PC of EAL (long term)]]>1,\"No\",\"Yes\"),\"\")","v":""}]
[null,null,null,null,null,{"$f":"IF(ISNUMBER(_Air73536374536[[#This Row],[%PC of EAL (long term)]]),IF(_Air73536374536[[#This Row],[%PC of EAL (long term)]]>1,\"No\",\"Yes\"),\"\")","v":""}]
[null,null,null,null,null,{"$f":"IF(ISNUMBER(_Air73536374536[[#This Row],[%PC of EAL (long term)]]),IF(_Air73536374536[[#This Row],[%PC of EAL (long term)]]>1,\"No\",\"Yes\"),\"\")","v":""}]
[null,null,null,null,null,{"$f":"IF(ISNUMBER(_Air73536374536[[#This Row],[%PC of EAL (long term)]]),IF(_Air73536374536[[#This Row],[%PC of EAL (long term)]]>1,\"No\",\"Yes\"),\"\")","v":""}]
[null,null,null,null,null,{"$f":"IF(ISNUMBER(_Air73536374536[[#This Row],[%PC of EAL (long term)]]),IF(_Air73536374536[[#This Row],[%PC of EAL (long term)]]>1,\"No\",\"Yes\"),\"\")","v":""}]
[null,null,null,null,null,{"$f":"IF(ISNUMBER(_Air73536374536[[#This Row],[%PC of EAL (long term)]]),IF(_Air73536374536[[#This Row],[%PC of EAL (long term)]]>1,\"No\",\"Yes\"),\"\")","v":""}]
[null,null,null,null,null,{"$f":"IF(ISNUMBER(_Air73536374536[[#This Row],[%PC of EAL (long term)]]),IF(_Air73536374536[[#This Row],[%PC of EAL (long term)]]>1,\"No\",\"Yes\"),\"\")","v":""}]
[null,null,null,null,null,{"$f":"IF(ISNUMBER(_Air73536374536[[#This Row],[%PC of EAL (long term)]]),IF(_Air73536374536[[#This Row],[%PC of EAL (long term)]]>1,\"No\",\"Yes\"),\"\")","v":""}]
[null,null,null,null,null,{"$f":"IF(ISNUMBER(_Air73536374536[[#This Row],[%PC of EAL (long term)]]),IF(_Air73536374536[[#This Row],[%PC of EAL (long term)]]>1,\"No\",\"Yes\"),\"\")","v":""}]
[null,null,null,null,null,{"$f":"IF(ISNUMBER(_Air73536374536[[#This Row],[%PC of EAL (long term)]]),IF(_Air73536374536[[#This Row],[%PC of EAL (long term)]]>1,\"No\",\"Yes\"),\"\")","v":""}]
[null,null,null,null,null,{"$f":"IF(ISNUMBER(_Air73536374536[[#This Row],[%PC of EAL (long term)]]),IF(_Air73536374536[[#This Row],[%PC of EAL (long term)]]>1,\"No\",\"Yes\"),\"\")","v":""}]
[null,null,null,null,null,{"$f":"IF(ISNUMBER(_Air73536374536[[#This Row],[%PC of EAL (long term)]]),IF(_Air73536374536[[#This Row],[%PC of EAL (long term)]]>1,\"No\",\"Yes\"),\"\")","v":""}]
[null,null,null,null,null,{"$f":"IF(ISNUMBER(_Air73536374536[[#This Row],[%PC of EAL (long term)]]),IF(_Air73536374536[[#This Row],[%PC of EAL (long term)]]>1,\"No\",\"Yes\"),\"\")","v":""}]
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{"sheet":"1AWato1","index":20,"n_rows":4,"n_cols":19,"rows_kept":4,"cut":false,"hidden":true,"merged":[[0,7,0,8]]}
[]
["Environmental Assessment"]
[]
[null,null,"Sector","Air/Water?","Release point code","Substance","Long term conc (ug/l)","Short term conc (ug/l)","Product / sub-sector","Sub-Product / sub sub-sector","Plant type","Plant age","Fuel type","Plant capacity","Emission Source","BAT","BAT-AEL units","BAT-AEL lower value","BAT-AEL upper value"]

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["Environmental Assessment"]
[null,null,null,null,null,"Please specify a conversion factor on the right or enter 1",null,null,"Please specify a CO2 factor on the right"]
[]
[null,null,null,null,null,null,null,"Please enter a conversion factor or a value of 1 in column G",null,null,"Please enter a CO2 factor in column J"]
[null,"Number","Energy source","Direct/Indirect emissions","Delivered MWh/yr","Conversion factor","User conv factor","Primary MWh/yr","CO2 factor","User CO2 factor","CO2 tonne/yr"]
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[null,null,null,"Comments:"]
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[null,{"$f":"IF(B63=\"Number\",1,B63+1)","v":1},null,{"$f":"IFERROR(VLOOKUP('1Ei'!C64,Variables!$AH$3:$AI$19,2,FALSE),\"\")","v":""},null,{"$f":"IF(ISNUMBER(VLOOKUP('1Ei'!$C64,Variables!$AH$3:$AK$19,4,FALSE)),VLOOKUP('1Ei'!$C64,Variables!$AH$3:$AK$19,4,FALSE),\"\")","v":""},null,{"$f":"IF(ISNUMBER('1Ei'!$F64),'1Ei'!$E64*'1Ei'!$F64,IF(ISNUMBER('1Ei'!$G64),'1Ei'!$E64*'1Ei'!$G64,\"\"))","v":""},{"$f":"IF(ISNUMBER(VLOOKUP('1Ei'!$C64,Variables!$AH$3:$AK$19,3,FALSE)),VLOOKUP('1Ei'!$C64,Variables!$AH$3:$AK$19,3,FALSE),\"\")","v":""},null,{"$f":"IF(ISNUMBER('1Ei'!$I64),'1Ei'!$H64*'1Ei'!$I64,IF(ISNUMBER('1Ei'!$J64),'1Ei'!$H64*'1Ei'!$I64,\"\"))","v":""}]

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[]
["Raw",{"$f":"B1+1","v":1}]
["Environmental Assessment"]
[]
[]
[]
[{"$f":"COUNTIF(RawMaterials_TopRow:materialLastRow, \"<>\" & \"\")-1","v":1},"Number","Material","Annual consumption","Units"]
[null,{"$f":"IF(B7=\"Number\",1,B7+1)","v":1}]
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[]
[]
[null,{"$f":"IF(B83=\"Number\",1,B83+1)","v":1}]

{"sheet":"1Wastei","index":23,"n_rows":86,"n_cols":6,"rows_kept":86,"cut":false,"hidden":false,"merged":[]}
[]
["Waste",{"$f":"B1+1","v":1}]
["Environmental Assessment"]
[]
[]
[]
[{"$f":"COUNTIF(WasteTopRow:WasteStreamLastRow, \"<>\" & \"\")-1","v":1},"Number","Waste stream","Category of waste","Mass (t/yr)","Disposal/Recovery option"]
[null,{"$f":"IF(B7=\"Number\",1,B7+1)","v":1}]
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[]
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[]
[null,{"$f":"IF(B85=\"Number\",1,B85+1)","v":1}]

{"sheet":"1PIo","index":24,"n_rows":31,"n_cols":13,"rows_kept":31,"cut":false,"hidden":false,"merged":[[6,5,6,12]]}
[]
["Environmental Assessment"]
[]
[]
[]
[]
[]
[]
[]
[]
[null,"Basic consumption data:",null,null,null,null,null,null,{"$f":"\"Specific combustion per \"&F14&\" of \"&F16&\":\"","v":"Specific combustion per  of :"}]
[]
[null,null,null,"Name","Annual quantity","Units"]
[null,"Amount of product:",null,null,null,null,null,null,"Production efficiency:",{"$f":"IFERROR(E14/E16,\"\")","v":""},{"$f":"F14&\"/\"&F16","v":"/"}]
[]
[null,"Main raw material:",null,null,{"$f":"IFERROR(VLOOKUP($D16,'1Ri'!#REF!,2,FALSE),\"\")","v":""},{"$f":"IFERROR(VLOOKUP($D16,'1Ri'!#REF!,3,FALSE),\"\")","v":""}]
[]
[null,{"$f":"IF($F$5=\"Intermediate\",\"Intermediate:\",\"\")","v":""}]
[]
[null,"Potable water",null,null,600,"m3",null,null,"Potable water:",null,null,{"$f":"IFERROR(IF($F$5=\"Product\",E20/$E$14,IF($F$5=\"Raw material\",E20/$E$16,IF($F$5=\"Intermediate\",E20/$E$18,\"\"))),\"\")","v":""},"m3"]
[]
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[null,null,"Can ANY of the options generate a visible plume?",null,null,{"$f":"IF(E6=\"No\",\"Move on to the next page\",\"\")","v":""}]
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[null,null,"Can any of the release points generate a Visible Plume"]
[]
[null,null,"For what percentage of daylight hours per year does the"]
[null,null,"plume extend beyond the facility boundary?",null,null,{"$f":"IF(E8=\"No\",\"You selected that none of the release points generates a visible plume\",\"\")","v":""}]
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[null,null,"Refer to the guidance in Annex A and assign a level of",null,{"$f":"IFERROR(VLOOKUP($E$11,Variables!$BP$3:$BQ$6,2,FALSE),\"\")","v":""}]
[null,null,"significance"]
[]
[]
[null,null,"Provide any supporting evidence below"]

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[null,null,"Yes",null,"Air",null,null,null,null,"Yes"]
[]
[null,null,"No",null,"Deposition from air to land",null,null,null,null,"No"]
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[null,null,"No",null,"Water",null,null,null,null,"No"]
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[null,null,"No",null,"Waste",null,null,null,null,"No"]
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[null,null,"No",null,"Visual",null,null,null,null,"No"]
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[null,null,null,null,"Ozone creation",null,null,null,null,"No"]
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[null,null,null,null,"Global warming",null,null,null,null,"No"]
[]
[null,null,null,null,"BAT-AEL test",null,null,null,null,"No"]
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[null,null,null,null,"Performance indicators",null,null,null,null,"No"]
[]
[]
[null,null,{"$f":"IF(OR(C7=\"Error\",C11=\"Error\"),\"You selected that there are no releases. If you want to run the air tests, please go back to objectives and select Yes\",\"\")","v":""}]

{"sheet":"Outputtables","index":29,"n_rows":16,"n_cols":32,"rows_kept":16,"cut":false,"hidden":false,"merged":[]}
[]
[]
[]
[]
[]
[null,"Option","Substance","Test 1","Test 2",null,"Option","Type of water body","Release point code","Substance","Freshwater test 1","Freshwater test 2","Freshwater test 3","Freshwater test 4a","Freshwater test 4b",null,"Option","Type of water body","Description","Substance","Significant load test",null,"Option","Type of water body","Description","Substance","TRAC test 1","TRAC test 2","TRAC test 3","TRAC test 4a","TRAC test 4b","TRAC test 5b"]
[null,1,"Particulates (PM10)","Fail","Fail"]
[null,1,"Nitrogen dioxide","Pass"]
[null,1,"Chromium (VI) compounds (as Cr)","Fail","Fail"]
[null,1,"Sulphur dioxide  (15 min mean)","Pass"]
[null,1,"Sulphur dioxide (24 hr mean)","Pass"]
[null,1,"Nickel and compounds (as Ni) except nickel carbonyl","Pass"]
[null,1,"Benzene","Pass"]
[null,1,"Nitrogen oxides (as NO2) (ecological)","Pass"]
[null,1,"Sulphur dioxide (ecological-lichens and bryophytes)","Pass"]
[null,1,"Sulphur dioxide (ecological-other vegetation)","Pass"]

{"sheet":"Variables","index":30,"n_rows":431,"n_cols":70,"rows_kept":431,"cut":false,"hidden":false,"merged":[]}
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,1,"Validation for options in performance indicators"]
[null,"Select discharge point",null,null,"Option air/water",null,null,"Other Y/N","No","Yes","Water","Air",null,null,null,null,"Measurement method",null,null,null,null,"Number of options",null,null,null,null,null,null,null,"Sectors",null,null,null,"Energy sources","lookup for energy","CO2 factor","conversion factor",null,null,"Units for raw materials",null,null,"Waste types","Score",null,null,"treatments","Score",null,null,"Performance indicators/parameters to calculate performance",null,null,null,null,null,2,"Option 0i","Option 0o",null,null,null,null,"Row number BREF and others",null,null,null,"Visual impact"]
[null,"R","Riverine",null,"Yes",null,null,"Yes","Yes","Unrequired",null,null,null,null,null,null,"Continuous",null,null,null,null,1,null,null,null,null,null,null,null,"Glass",null,null,null,"Electricity from other source (Specify in comments below)","Indirect emissions",null,null,null,null,"m3 per year",null,null,"Hazardous",10,null,null,"Composting (R3)",2,null,null,"Product",null,null,null,null,null,3,"Non-potable water",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":"Non-potable water"},null,null,null,null,1,null,null,null,"<5%","Insignificant","NA"]
[null,"TR","TraC (Estuary & Coastal)",null,"No",null,null,"No","No",null,"1,1,1-trichloroethane","Ethylene dibromide (1,2-Dibromoethane)","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,"Estimated",null,null,null,null,2,null,null,null,null,null,null,null,"Iron and steel",null,null,null,"Other imported energy (Steam, hot water, etc)","Indirect emissions",null,null,null,null,"Tonnes per year",null,null,"Stable non-reactive hazardous waste",8,null,null,"Other recycling (R3:R4:R5:R11 and R12)",3,null,null,"Raw material",null,null,null,null,null,4,"Potable water",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":"Potable water"},null,null,null,null,{"$f":"BL3+1","v":2},null,null,null,"5% - 25%","Medium"]
[null,"T","TraC Riverine(Upper Estuary)",null,null,null,null,null,null,null,"1,1,2-Trichloroethane","Ethylene dichloride (1,2-Dichloroethane)","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,"Spot",null,null,null,null,3,null,null,null,null,null,null,null,"Tanning of Hides and Skins",null,null,null,"Electricity from public supply","Indirect emissions",0.16600000000000001,2.4,null,null,"Other",null,null,"Biodegradable non-hazardous waste",4,null,null,"Chemical recovery (R2 to R9)",4,null,null,"Intermediate",null,null,null,null,null,5,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,3,null,null,null,">25%","High"]
[null,null,null,null,null,null,null,null,"No ",null,"1,2 Dichloroethane","1,3-Butadiene","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,4,null,null,null,null,null,null,null,"Cement lime and MgO",null,null,null,"Renewable electricity (non-fossil fuel)","Indirect emissions",0,0,null,null,null,null,null,"Other non-hazardous",2,null,null,"Landspreading (R10)",4,null,null,null,null,null,null,null,null,6,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,4,null,null,null,"NA","NA"]
[null,null,null,null,null,null,null,null,null,null,"2,4-Dichlorophenol","1,4-Dioxane","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,5,null,null,null,null,null,null,null,"Chlor Alkali",null,null,null,"Coal","Direct emissions",0.3,1,null,null,null,null,null,"Inert",1,null,null,"Use of waste as fuel (R1)",6,null,null,null,null,null,null,null,null,7,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,5]
[null,null,null,null,null,null,null,null,null,null,"2,4-Dichlorophenoxyacetic acid (2,4-D) (95%ile)","Acetaldehyde","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper",null,null,null,"Coke","Direct emissions",0.43,1,null,null,null,null,null,null,null,null,null,"Biological treatment with energy recovery (D8/R3 and R1)",8,null,null,null,null,null,null,null,null,8,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,6]
[null,null,null,null,null,null,null,null,"Unrequired",null,"2-Chlorophenol","Acetic acid","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Refineries",null,null,null,"Gas oil","Direct emissions",0.25,1,null,null,null,null,null,null,null,null,null,"Incineration with energy recovery D10",10,null,null,null,null,null,null,null,null,9,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,7]
[null,null,null,null,null,null,null,null,"Yes",null,"3,4 - dichloroaniline","Acetic anhydride","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Woodbased Panels Production",null,null,null,"Heavy fuel oil","Direct emissions",0.26,1,null,null,null,null,null,null,null,null,null,"Biological and physico-chemical treatment (D8 and D9)",12,null,null,null,null,null,null,null,null,10,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,8]
[null,null,null,null,null,null,null,null,"No",null,"3-Chlorophenol + 4-chlorophenol (total or individual monochlorophenols)","Acetone","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non ferrous Metals Industries",null,null,null,"Petrol","Direct emissions",0.24,1,null,null,null,null,null,null,null,null,null,"Release into water and lagoons D4:D6 or D7",15,null,null,null,null,null,null,null,null,11,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,9]
[null,null,null,null,null,null,null,null,null,null,"4-chloro-3-methyl-phenol","Acetonitrile","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Common Waste Water and Waste Gas Treatment",null,null,null,"Liquid petroleum gas","Direct emissions",0.23,1,null,null,null,null,null,null,null,null,null,"Permanent storage D10 or D3",17,null,null,null,null,null,null,null,null,12,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,10]
[null,null,null,null,null,null,null,null,"Yes",null,"Abamectin","Acrylamide","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP",null,null,null,"Jet kerosene","Direct emissions",0.24,1,null,null,null,null,null,null,null,null,null,"Incineration without energy recovery (D10)",20,null,null,null,null,null,null,null,null,13,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,11]
[null,null,null,null,null,null,null,null,"No",null,"Aclonifen","Acrylic acid","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Ethane","Direct emissions",0.2,1,null,null,null,null,null,null,null,null,null,"Landfill (D5)",30,null,null,null,null,null,null,null,null,14,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,12]
[null,null,null,null,null,null,null,null,"Unrequired",null,"Alachlor","Acrylonitrile","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Naphtha","Direct emissions",0.26,1,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,15,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,13]
[null,null,null,null,null,null,null,null,null,null,"Ammonia (≤ 50mg/l CaCO3 (90 %ile))","Allyl alcohol","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Refinery gas","Direct emissions",0.2,1,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,16,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,14]
[null,null,null,null,null,null,null,null,null,null,"Ammonia (un-ionised)","Ammonia (ecological-lichens and bryophytes)","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Petroleum coke","Direct emissions",0.34,1,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,17,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,15]
[null,null,null,null,null,null,null,null,null,null,"Ammonia CaCO3 >50mg/l (90 %ile)","Ammonia (ecological-other vegetation)","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Natural gas","Direct emissions",0.19,1,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,18,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,16]
[null,null,null,null,null,null,null,null,null,null,"Ammonia CaCO3 ≤50mg/l (90 %ile)","Ammonia","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Other fuel","Direct emissions",0,1,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,19,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,17]
[null,null,null,null,null,null,null,null,null,null,"Anthracene","Aniline","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,20,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,18]
[null,null,null,null,null,null,null,null,null,null,"Arsenic","Antimony and compounds (as Sb), except antimony trisulphide and antimony trioxide","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,19]
[null,null,null,null,null,null,null,null,null,null,"Atrazine","Arsenic and compounds (as As)","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,21,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,20]
[null,null,null,null,null,null,null,null,null,null,"Azinphos methyl (dissolved)","Arsine","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,22,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,21]
[null,null,null,null,null,null,null,null,null,null,"Bentazone","Benzene","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,23,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,22]
[null,null,null,null,null,null,null,null,null,null,"Benzene","Benzo-a-pyrene","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,24,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,23]
[null,null,null,null,null,null,null,null,null,null,"Benzo (a) pyrene","Benzylchloride","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,25,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,24]
[null,null,null,null,null,null,null,null,null,null,"Benzo (b) fluoranthene","Beryllium and compounds (as Be)","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,26,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,25]
[null,null,null,null,null,null,null,null,null,null,"Benzo (g,h,i) perylene","Boron trifluoride","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,27,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,26]
[null,null,null,null,null,null,null,null,null,null,"Benzo (k) fluoranthene","Bromine","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,28,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,27]
[null,null,null,null,null,null,null,null,null,null,"Benzyl Butyl phthalate","Bromomethane","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,29,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,28]
[null,null,null,null,null,null,null,null,null,null,"Bifenox (Methyl 5-(2,4-dichlorophenoxy)-2-nitrobenzoate)","Methyl ethyl ketone (MEK, 2-Butanone)","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,30,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,29]
[null,null,null,null,null,null,null,null,null,null,"Biphenyl","Butane","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,31,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,30]
[null,null,null,null,null,null,null,null,null,null,"Boron","Cadmium and compounds (as Cd)","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,32,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,31]
[null,null,null,null,null,null,null,null,null,null,"Brominated diphenylether - total PDPE (Polybrominated diphenylether, or congener) numbers 28, 47, 99, 100, 153 and 154","Carbon disulphide","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,33,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,32]
[null,null,null,null,null,null,null,null,null,null,"Bromine","Carbon monoxide","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,34,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,33]
[null,null,null,null,null,null,null,null,null,null,"Bromoxynil","Carbon tetrachloride","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,35,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,{"$f":"BL35+1","v":34}]
[null,null,null,null,null,null,null,null,null,null,"Butylbenzyl phthalate","Chlorine","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,36,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,35]
[null,null,null,null,null,null,null,null,null,null,"C10-13 Chloroalkanes","Chloroform","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,37,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,36]
[null,null,null,null,null,null,null,null,null,null,"Cadmium and its compounds (dissolved, water hardness < 40 mg/l Ca CO3)","Methyl chloride (chloromethane)","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,38,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,37]
[null,null,null,null,null,null,null,null,null,null,"Cadmium and its compounds (dissolved, water hardness ≥ 200 mg/l CaCO3)","Chromium (VI) compounds (as Cr)","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,39,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,38]
[null,null,null,null,null,null,null,null,null,null,"Cadmium and its compounds (dissolved, water hardness 100 - <200 mg/l CaCO3)","Chromium (III) compounds (as Cr)","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,40,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,39]
[null,null,null,null,null,null,null,null,null,null,"Cadmium and its compounds (dissolved, water hardness 40 - < 50 mg/l CaCO3)","Copper and compounds (as Cu)","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,41,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,40]
[null,null,null,null,null,null,null,null,null,null,"Cadmium and its compounds (dissolved, water hardness 50 - <100 mg/l CaCO3)","Dibutyl phthalate (DBP)","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,42,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,41]
[null,null,null,null,null,null,null,null,null,null,"Carbendazim","Methylene chloride (dichloromethane)","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,43,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,42]
[null,null,null,null,null,null,null,null,null,null,"Carbon tetrachloride","Diethyl ether","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,44,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,43]
[null,null,null,null,null,null,null,null,null,null,"Chlorfenvinphos","Diethylketone","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,45,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,44]
[null,null,null,null,null,null,null,null,null,null,"Chloride","Diisopropyl ether","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,46,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,45]
[null,null,null,null,null,null,null,null,null,null,"Chlorine (95%ile concentration of total residual oxidant)","Diisobutyl phthalate","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,47,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,46]
[null,null,null,null,null,null,null,null,null,null,"Chloronitrotoluenes","Dimethyl sulphate","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,48,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,47]
[null,null,null,null,null,null,null,null,null,null,"Chlorothalonil","Dimethylformamide","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,49,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,48]
[null,null,null,null,null,null,null,null,null,null,"Chlorotoluron","Ethyl acrylate","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,50,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,49]
[null,null,null,null,null,null,null,null,null,null,"Chlorpropham","Ethylbenzene","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,51,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,50]
[null,null,null,null,null,null,null,null,null,null,"Chlorpyrifos (chlorpyrifos ethyl)","Ethylene oxide","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,52,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,51]
[null,null,null,null,null,null,null,null,null,null,"Chromium III (95%ile) (dissolved)","Formaldehyde","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,53,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,52]
[null,null,null,null,null,null,null,null,null,null,"Chromium VI (95%ile) (dissolved)","Hydrazine","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,54,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,53]
[null,null,null,null,null,null,null,null,null,null,"Cobalt","Hydrogen bromide","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,55,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,54]
[null,null,null,null,null,null,null,null,null,null,"Cobalt (dissolved)","Hydrogen chloride","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,56,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,55]
[null,null,null,null,null,null,null,null,null,null,"Copper - dissolved (Dissolved Organic Carbon (DOC) greater than 1mg/l) ","Hydrogen cyanide","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,57,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,56]
[null,null,null,null,null,null,null,null,null,null,"Copper - dissolved (Dissolved Organic Carbon (DOC) less than or equal to 1mg/l) ","Hydrogen fluoride (ecological)","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,58,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,57]
[null,null,null,null,null,null,null,null,null,null,"Copper (dissolved, bioavailable)","Hydrogen fluoride","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,59,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,58]
[null,null,null,null,null,null,null,null,null,null,"Coumaphos","Hydrogen iodide","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,60,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,59]
[null,null,null,null,null,null,null,null,null,null,"Cyanide ","Hydrogen sulphide","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,61,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,60]
[null,null,null,null,null,null,null,null,null,null,"Cybutryne","Lead","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,62,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,61]
[null,null,null,null,null,null,null,null,null,null,"Cyclodiene pesticides: Aldrin, Dieldrin, Endrin, Isodrin (Total)","Manganese and compounds (as Mn)","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,63,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,62]
[null,null,null,null,null,null,null,null,null,null,"Cyfluthrin","Mercury and its inorganic compounds (as Hg)","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,64,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,63]
[null,null,null,null,null,null,null,null,null,null,"Cypermethrin (95%ile)","Methanol","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,65,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,64]
[null,null,null,null,null,null,null,null,null,null,"DDT total","Methyl chloroform","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,66,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,65]
[null,null,null,null,null,null,null,null,null,null,"Demetons","Molydenum","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,67,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,{"$f":"BL67+1","v":66}]
[null,null,null,null,null,null,null,null,null,null,"Di(2-ethylhexyl)-phthalate (DEHP)","Mono-ethanolamine (MEA)","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,68,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,67]
[null,null,null,null,null,null,null,null,null,null,"Diazinon (95%ile)","Naphthalene","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,69,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,68]
[null,null,null,null,null,null,null,null,null,null,"Dibutyl phthalate","N-hexane","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,70,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,69]
[null,null,null,null,null,null,null,null,null,null,"Dichlorobenzene (total dichlorobenzene isomers)","Nickel and compounds (as Ni) except nickel carbonyl","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,71,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,70]
[null,null,null,null,null,null,null,null,null,null,"Dichloromethane (DCM, Methylene Chloride)","Nitric acid","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,72,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,71]
[null,null,null,null,null,null,null,null,null,null,"Dichlorvos (insecticide)","Nitrogen dioxide","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,73,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,72]
[null,null,null,null,null,null,null,null,null,null,"Dicofol (insecticide)","Nitrogen oxides (as NO2) (ecological)","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,74,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,73]
[null,null,null,null,null,null,null,null,null,null,"Diethyl phthalate","Nitrogen monoxide (nitric oxide)","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,75,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,74]
[null,null,null,null,null,null,null,null,null,null,"Diflubenzuron","N-nitrosodimethylamine (NDMA)","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,76,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,75]
[null,null,null,null,null,null,null,null,null,null,"Diflubenzuron","Orthophosphoric acid","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,77,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,76]
[null,null,null,null,null,null,null,null,null,null,"Diflubenzuron","Ozone","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,78,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,77]
[null,null,null,null,null,null,null,null,null,null,{"$f":"SubstancesW!B178","v":"Diflubenzuron"},"Para dichlorobenzene","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,79,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,78]
[null,null,null,null,null,null,null,null,null,null,"Dimethoate (95%ile)","Particulates (PM10)","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,80,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,79]
[null,null,null,null,null,null,null,null,null,null,"Dimethyl phthalate","Particulates (PM2.5)","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,81,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,80]
[null,null,null,null,null,null,null,null,null,null,"Dioctyl phthalate","Methyl propyl ketone (MPK, 2-Pentanone)","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,82,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,81]
[null,null,null,null,null,null,null,null,null,null,"Diuron (herbicide)","Diethyl ketone (3-Pentanone)","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,83,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,82]
[null,null,null,null,null,null,null,null,null,null,"Doramectin","Phenol","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,84,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,83]
[null,null,null,null,null,null,null,null,null,null,"EDTA","Phosgene","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,85,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,84]
[null,null,null,null,null,null,null,null,null,null,"Endosulfan","Phosphine","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,86,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,85]
[null,null,null,null,null,null,null,null,null,null,"Fenchlorphos","Polychlorinated biphenyls (PCBs)","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,87,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,86]
[null,null,null,null,null,null,null,null,null,null,"Fenitrothion","1-propanol","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,88,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,87]
[null,null,null,null,null,null,null,null,null,null,"Flocfuron","2-propanol","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,89,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,88]
[null,null,null,null,null,null,null,null,null,null,"Fluoranthene","Propylene oxide","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,90,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,89]
[null,null,null,null,null,null,null,null,null,null,"Fluoride (> 50mg/l CaCO3) (dissolved)","Selenium and compounds (as Se), except hydrogen selenide","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,91,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,90]
[null,null,null,null,null,null,null,null,null,null,"Fluoride (≤ 50mg/l CaCO3) (dissolved)","Sodium hydroxide","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,92,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,91]
[null,null,null,null,null,null,null,null,null,null,"Fluoride >50mg/l CaCO3","Styrene","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,93,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":0},null,null,null,null,92]
[null,null,null,null,null,null,null,null,null,null,"Fluoride ≤50mg/l CaCO3","Sulphur dioxide  (15 min mean)","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,94,0,{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,93]
[null,null,null,null,null,null,null,null,null,null,"Formaldehyde","Sulphur dioxide (24 hr mean)","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,95,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,94]
[null,null,null,null,null,null,null,null,null,null,"Glyphosate","Sulphur dioxide (ecological-lichens and bryophytes)","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,96,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,95]
[null,null,null,null,null,null,null,null,null,null,"Heptachlor & heptachlor epoxide","Sulphur dioxide (ecological-other vegetation)","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,97,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,96]
[null,null,null,null,null,null,null,null,null,null,"Hexabromocyclododecane (HBCDD)","Sulphur hexafluoride","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,98,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,97]
[null,null,null,null,null,null,null,null,null,null,"Hexachlorobenzene","Sulphuric acid","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,99,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,{"$f":"BL99+1","v":98}]
[null,null,null,null,null,null,null,null,null,null,"Hexachlorobutadiene","Tetrachloroethylene","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,100,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,99]
[null,null,null,null,null,null,null,null,null,null,"Hexachlorocyclohexane","Tetrahydrofuran","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,101,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,100]
[null,null,null,null,null,null,null,null,null,null,"Hydrogen sulphide","Toluene","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,102,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,101]
[null,null,null,null,null,null,null,null,null,null,"Indeno (1,2,3-cd) pyrene (see PAHs for AA and biota EQS)","Trichloroethylene","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,103,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,102]
[null,null,null,null,null,null,null,null,null,null,"Ioxynil","1,2,4-Trichlorobenzene","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,104,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,103]
[null,null,null,null,null,null,null,null,null,null,"Iron","Trimethylbenzenes, all isomers or mixtures","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,105,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,104]
[null,null,null,null,null,null,null,null,null,null,"Iron (dissolved)","Vanadium and compounds (as V)","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,106,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,105]
[null,null,null,null,null,null,null,null,null,null,"Isoproturon","Vinyl acetate","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,107,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,106]
[null,null,null,null,null,null,null,null,null,null,"Ivermectin","Vinyl chloride","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,108,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,107]
[null,null,null,null,null,null,null,null,null,null,"Lead and its compounds (dissolved)","Xylene, o-, m-, p- or mixed isomers","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,109,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,108]
[null,null,null,null,null,null,null,null,null,null,"Linuron (95%ile)","Zinc oxide","Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,110,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,109]
[null,null,null,null,null,null,null,null,null,null,"Lithium (I) cation",null,"Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,111,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,110]
[null,null,null,null,null,null,null,null,null,null,"Malachite green",null,"Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,112,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,111]
[null,null,null,null,null,null,null,null,null,null,"Malathion",null,"Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,113,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,112]
[null,null,null,null,null,null,null,null,null,null,"Mancozeb",null,"Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,114,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,113]
[null,null,null,null,null,null,null,null,null,null,"Maneb",null,"Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,115,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,114]
[null,null,null,null,null,null,null,null,null,null,"Manganese",null,"Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,116,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""}]
[null,null,null,null,null,null,null,null,null,null,"MCPA (pH level higher than 7)",null,"Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,117,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,{"$f":"BL116+1","v":115}]
[null,null,null,null,null,null,null,null,null,null,"MCPA (pH level less than 7)",null,"Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,118,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,{"$f":"BL118+1","v":116}]
[null,null,null,null,null,null,null,null,null,null,"Mevinphos",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,119,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,117]
[null,null,null,null,null,null,null,null,null,null,"Naphthalene",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,120,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,118]
[null,null,null,null,null,null,null,null,null,null,"Nickel and its compounds (dissolved)",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,121,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,119]
[null,null,null,null,null,null,null,null,null,null,"Nitrilotriacetic acid (NTA)",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,122,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,120]
[null,null,null,null,null,null,null,null,null,null,"Nonyl phenol (4-Nonylphenol)",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,123,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,121]
[null,null,null,null,null,null,null,null,null,null,"NTA",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,124,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,122]
[null,null,null,null,null,null,null,null,null,null,"Mercury and its compounds (dissolved)","1,1 Dichloroethane ","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,125,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,123]
[null,null,null,null,null,null,null,null,null,null,"Methiocarb","Methyl chloroform","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,126,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,124]
[null,null,null,null,null,null,null,null,null,null,"Octyl phenol ((4-(1,1',3,3',-tetramethylbutyl)-phenol))","1,2-Dichloroethane (Ethylene dichloride)","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,127,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,125]
[null,null,null,null,null,null,null,null,null,null,"Omethoate","1,2,4-Trichlorobenzene","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,128,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,126]
[null,null,null,null,null,null,null,null,null,null,"para-para DDT","1,2-Dibromoethane","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,129,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,127]
[null,null,null,null,null,null,null,null,null,null,"PCSDs","1,3-Butadiene","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,130,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,128]
[null,null,null,null,null,null,null,null,null,null,"Pendimethalin","1,4-Dichlorobenzene","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,131,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,129]
[null,null,null,null,null,null,null,null,null,null,"Pentachlorobenzene","1,4-Dioxane","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,132,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,130]
[null,null,null,null,null,null,null,null,null,null,"Pentachlorophenol","Acetaldehyde","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,133,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,{"$f":"BL133+1","v":131}]
[null,null,null,null,null,null,null,null,null,null,"Perfluoroctane sulphonic acid and its salts (PFOS)","Acetic acid","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,134,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,132]
[null,null,null,null,null,null,null,null,null,null,"Permethrin (95%ile)","Acetic anhydride","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,135,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,133]
[null,null,null,null,null,null,null,null,null,null,"Phenol (95%ile)","Acetone","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,136,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,134]
[null,null,null,null,null,null,null,null,null,null,"Pirimiphos-methyl","Acetonitrile","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,137,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,135]
[null,null,null,null,null,null,null,null,null,null,"Pirmicarb","Acrylamide","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,138,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,136]
[null,null,null,null,null,null,null,null,null,null,"Polyaromatic hydrocarbons - Benzo (b) or (k)fluoranthene","Acrylic acid","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,139,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,137]
[null,null,null,null,null,null,null,null,null,null,"Polyaromatic hydrocarbons (PAH): Benzo (a)pyrene. Polyaromatic hydrocarbons (PAH) - Benzo(a)-pyrene (BaP), Benzo(b)-fluor-anthene, Benzo(k)-fluor-anthene, Benzo(g,h,i)-perylene and Indeno(1,2,3-cd)-pyrene. Benzo(a)pyrene can be  considered as a marker for the other PAHs, hence only benzo(a)pyrene needs to be  monitored for comparison with the biota EQS or the corresponding AA-EQS in water","Acrylonitrile","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,140,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,138]
[null,null,null,null,null,null,null,null,null,null,"Polyaromatic hydrocarbons: Benzo (g,h,i)-perylene / Indeno(1,2,3-cd)-pyrene","Allyl alcohol","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,141,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,139]
[null,null,null,null,null,null,null,null,null,null,"Prochloraz","Ammonia (ecological-lichens and bryophytes)","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,142,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,140]
[null,null,null,null,null,null,null,null,null,null,"Propetamphos","Ammonia (ecological-other vegetation)","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,143,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,141]
[null,null,null,null,null,null,null,null,null,null,"Propyzamide","Ammonia","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,144,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,142]
[null,null,null,null,null,null,null,null,null,null,"Quinoxyfen","Aniline","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,145,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,143]
[null,null,null,null,null,null,null,null,null,null,"Silver","Antimony and compounds (as Sb), except antimony trisulphide and antimony trioxide","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,146,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,144]
[null,null,null,null,null,null,null,null,null,null,"Silver (dissolved)","Arsenic and compounds (as As)","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,147,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,145]
[null,null,null,null,null,null,null,null,null,null,"Simazine","Arsine","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,148,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,146]
[null,null,null,null,null,null,null,null,null,null,"Simazine (+ atrazine)","Benzene","Scottish Environment Protection Agency"]
[null,null,null,null,null,null,null,null,null,null,"Styrene","Benzo-a-pyrene","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,149,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,{"$f":"BL149+1","v":147}]
[null,null,null,null,null,null,null,null,null,null,"Sulcophuron","Benzylchloride","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,150,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,148]
[null,null,null,null,null,null,null,null,null,null,"Sulphate","Beryllium and compounds (as Be)","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,151,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,149]
[null,null,null,null,null,null,null,null,null,null,"Tecnazene (total)","Boron trifluoride","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,152,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,150]
[null,null,null,null,null,null,null,null,null,null,"Terbutryn","Bromine","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,153,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,151]
[null,null,null,null,null,null,null,null,null,null,"Tetrachloroethane","Bromomethane","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,154,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,152]
[null,null,null,null,null,null,null,null,null,null,"Tetrachloroethylene","Butan-2-one (Methylethylketone)","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,155,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,153]
[null,null,null,null,null,null,null,null,null,null,"Thiabendazole","Butane","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,156,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,154]
[null,null,null,null,null,null,null,null,null,null,"Tin (inorganic) - dissolved","Cadmium and compounds (as Cd)","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,157,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,155]
[null,null,null,null,null,null,null,null,null,null,"Toluene (95%ile)","Carbon disulphide","Scottish Environment Protection Agency"]
[null,null,null,null,null,null,null,null,null,null,"Total anions","Carbon monoxide","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,158,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,{"$f":"BL159+1","v":156}]
[null,null,null,null,null,null,null,null,null,null,"Triallate","Carbon tetrachloride","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,159,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,157]
[null,null,null,null,null,null,null,null,null,null,"Triazaphos","Chlorine","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,160,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,158]
[null,null,null,null,null,null,null,null,null,null,"Tributyl phosphate","Chlorobenzene","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,161,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,159]
[null,null,null,null,null,null,null,null,null,null,"Tributyltin compounds (Tributyltin cation)","Chloroform","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,162,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,160]
[null,null,null,null,null,null,null,null,null,null,"Trichlorobenzenes","Methyl chloride (chloromethane)","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,163,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,161]
[null,null,null,null,null,null,null,null,null,null,"Trichloroethylene","Chromium (VI) compounds (as Cr)","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,164,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,162]
[null,null,null,null,null,null,null,null,null,null,"Trichloromethane (chloroform)","Chromium (III) compounds (as Cr)","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,165,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,163]
[null,null,null,null,null,null,null,null,null,null,"Triclosan","Copper and compounds (as Cu)","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,166,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,164]
[null,null,null,null,null,null,null,null,null,null,"Trifluralin","Dibutyl phthalate (DBP)","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,167,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,165]
[null,null,null,null,null,null,null,null,null,null,"Triphenyltin & derivatives","Methylene chloride (dichloromethane)","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,168,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,166]
[null,null,null,null,null,null,null,null,null,null,"Un-ionised ammonia as nitrogen","Diethyl ether","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,169,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,167]
[null,null,null,null,null,null,null,null,null,null,"Vanadium (> 200 mg/l CaCO3)","Di-i-propyl ether","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,170,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,168]
[null,null,null,null,null,null,null,null,null,null,"Vanadium (0 - 200 mg/l CaCO3)","Diisobutyl phthalate","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,171,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,169]
[null,null,null,null,null,null,null,null,null,null,"Xylene","Dimethyl sulphate","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,172,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,170]
[null,null,null,null,null,null,null,null,null,null,"Zinc","Dimethylformamide","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,173,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,171]
[null,null,null,null,null,null,null,null,null,null,"Zinc - dissolved plus ambient background concentration. For saltwater, an ambient background concentration of 1.1ug/l is recommended.","Ethyl acrylate","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,174,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,172]
[null,null,null,null,null,null,null,null,null,null,null,"Ethylbenzene","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,175,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,173]
[null,null,null,null,null,null,null,null,null,null,{"$f":"SubstancesW!B179","v":0},"Ethylene oxide","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,176,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,174]
[null,null,null,null,null,null,null,null,null,null,{"$f":"SubstancesW!B180","v":0},"Formaldehyde","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,177,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,175]
[null,null,null,null,null,null,null,null,null,null,{"$f":"SubstancesW!B181","v":0},"Hydrazine","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,178,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,176]
[null,null,null,null,null,null,null,null,null,null,{"$f":"SubstancesW!B182","v":0},"Hydrogen bromide","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,179,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,177]
[null,null,null,null,null,null,null,null,null,null,{"$f":"SubstancesW!B183","v":0},"Hydrogen chloride","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,180,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,178]
[null,null,null,null,null,null,null,null,null,null,{"$f":"SubstancesW!B184","v":0},"Hydrogen cyanide","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,181,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,179]
[null,null,null,null,null,null,null,null,null,null,{"$f":"SubstancesW!B185","v":0},"Hydrogen fluoride (ecological)","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,182,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,180]
[null,null,null,null,null,null,null,null,null,null,{"$f":"SubstancesW!B186","v":0},"Hydrogen fluoride","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,183,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,181]
[null,null,null,null,null,null,null,null,null,null,{"$f":"SubstancesW!B187","v":0},"Hydrogen iodide","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,184,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,182]
[null,null,null,null,null,null,null,null,null,null,{"$f":"SubstancesW!B188","v":0},"Hydrogen sulphide","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,185,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,183]
[null,null,null,null,null,null,null,null,null,null,{"$f":"SubstancesW!B189","v":0},"Lead","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,186,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,184]
[null,null,null,null,null,null,null,null,null,null,{"$f":"SubstancesW!B190","v":0},"Manganese and compounds (as Mn)","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,187,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,185]
[null,null,null,null,null,null,null,null,null,null,{"$f":"SubstancesW!B191","v":0},"Mercury and its inorganic compounds (as Hg)","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,188,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,186]
[null,null,null,null,null,null,null,null,null,null,{"$f":"SubstancesW!B192","v":0},"Methanol","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,189,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,187]
[null,null,null,null,null,null,null,null,null,null,{"$f":"SubstancesW!B193","v":0},"Mono-ethanolamine (MEA)","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,190,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,188]
[null,null,null,null,null,null,null,null,null,null,{"$f":"SubstancesW!B194","v":0},"Naphthalene","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,191,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,189]
[null,null,null,null,null,null,null,null,null,null,{"$f":"SubstancesW!B195","v":0},"n-Hexane","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,192,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,190]
[null,null,null,null,null,null,null,null,null,null,{"$f":"SubstancesW!B196","v":0},"N-nitrosodimethylamine (NDMA)","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,193,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,191]
[null,null,null,null,null,null,null,null,null,null,{"$f":"SubstancesW!B197","v":0},"Nickel and compounds (as Ni) except nickel carbonyl","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,194,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,192]
[null,null,null,null,null,null,null,null,null,null,{"$f":"SubstancesW!B198","v":0},"Nitric acid","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,195,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,193]
[null,null,null,null,null,null,null,null,null,null,{"$f":"SubstancesW!B199","v":0},"Nitrogen dioxide","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,196,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,194]
[null,null,null,null,null,null,null,null,null,null,{"$f":"SubstancesW!B200","v":0},"Nitrogen oxides (as NO2) (ecological)","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,197,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,{"$f":"BL199+1","v":195}]
[null,null,null,null,null,null,null,null,null,null,{"$f":"SubstancesW!B201","v":0},"Nitrogen monoxide (nitric oxide)","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,198,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,196]
[null,null,null,null,null,null,null,null,null,null,{"$f":"SubstancesW!B202","v":0},"Orthophosphoric acid","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,199,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,197]
[null,null,null,null,null,null,null,null,null,null,{"$f":"SubstancesW!B203","v":0},"Ozone","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,200,"",{"$f":"IF(ROW()-ROW(NoBlanksRange1)+1>ROWS(BlanksRange1)-COUNTBLANK(BlanksRange1),\"\",INDIRECT(ADDRESS(SMALL((IF(BlanksRange1<>\"\",ROW(BlanksRange1),ROW()+ROWS(BlanksRange1))),ROW()-ROW(NoBlanksRange1)+1),COLUMN(BlanksRange1),4)))","v":""},null,null,null,null,198]
[null,null,null,null,null,null,null,null,null,null,null,"Particulates (PM10)","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"",null,null,null,null,null,199]
[null,null,null,null,null,null,null,null,null,null,null,"Particulates (PM2.5)","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"",null,null,null,null,null,200]
[null,null,null,null,null,null,null,null,null,null,null,"Pentan-2-one (Methylpropylketone)","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"",null,null,null,null,null,201]
[null,null,null,null,null,null,null,null,null,null,null,"Pentan-3-one (Diethylketone)","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"",null,null,null,null,null,202]
[null,null,null,null,null,null,null,null,null,null,null,"Phenol","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"",null,null,null,null,null,203]
[null,null,null,null,null,null,null,null,null,null,null,"Phosgene","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"",null,null,null,null,null,204]
[null,null,null,null,null,null,null,null,null,null,null,"Phosphine","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"",null,null,null,null,null,205]
[null,null,null,null,null,null,null,null,null,null,null,"Polychlorinated biphenyls","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"",null,null,null,null,null,206]
[null,null,null,null,null,null,null,null,null,null,null,"Polycyclic aromatic hydrocarbons (PAH)-total content within PM10 fraction","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"",null,null,null,null,null,207]
[null,null,null,null,null,null,null,null,null,null,null,"Propan-1-ol","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"",null,null,null,null,null,208]
[null,null,null,null,null,null,null,null,null,null,null,"Propan-2-ol","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"",null,null,null,null,null,209]
[null,null,null,null,null,null,null,null,null,null,null,"Propionic acid","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"",null,null,null,null,null,210]
[null,null,null,null,null,null,null,null,null,null,null,"Propylene oxide","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"",null,null,null,null,null,211]
[null,null,null,null,null,null,null,null,null,null,null,"Selenium and compounds (as Se), except hydrogen selenide","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"",null,null,null,null,null,212]
[null,null,null,null,null,null,null,null,null,null,null,"Sodium hydroxide","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"",null,null,null,null,null,213]
[null,null,null,null,null,null,null,null,null,null,null,"Styrene","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"",null,null,null,null,null,214]
[null,null,null,null,null,null,null,null,null,null,null,"Sulphur dioxide  (15 min mean)","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"",null,null,null,null,null,215]
[null,null,null,null,null,null,null,null,null,null,null,"Sulphur dioxide (24 hr mean)","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"",null,null,null,null,null,216]
[null,null,null,null,null,null,null,null,null,null,null,"Sulphur dioxide (ecological-lichens and bryophytes)","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"",null,null,null,null,null,217]
[null,null,null,null,null,null,null,null,null,null,null,"Sulphur dioxide (ecological-other vegetation)","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"",null,null,null,null,null,218]
[null,null,null,null,null,null,null,null,null,null,null,"Sulphur dioxide (ecological-crops)","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"",null,null,null,null,null,219]
[null,null,null,null,null,null,null,null,null,null,null,"Sulphur hexafluoride","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"",null,null,null,null,null,220]
[null,null,null,null,null,null,null,null,null,null,null,"Sulphuric acid","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"",null,null,null,null,null,221]
[null,null,null,null,null,null,null,null,null,null,null,"Tetrachloroethylene","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"",null,null,null,null,null,222]
[null,null,null,null,null,null,null,null,null,null,null,"Tetrahydrofuran","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"",null,null,null,null,null,223]
[null,null,null,null,null,null,null,null,null,null,null,"Toluene","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"",null,null,null,null,null,224]
[null,null,null,null,null,null,null,null,null,null,null,"Trichloroethylene","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"",null,null,null,null,null,225]
[null,null,null,null,null,null,null,null,null,null,null,"Trimethylbenzenes, all isomers or mixtures","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"",null,null,null,null,null,226]
[null,null,null,null,null,null,null,null,null,null,null,"Vanadium and compounds (as V)","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"",null,null,null,null,null,227]
[null,null,null,null,null,null,null,null,null,null,null,"Vinyl acetate","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"",null,null,null,null,null,228]
[null,null,null,null,null,null,null,null,null,null,null,"Vinyl chloride","Scottish Environment Protection Agency"]
[null,null,null,null,null,null,null,null,null,null,null,"Xylene, o-, m-, p- or mixed isomers","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"",null,null,null,null,null,{"$f":"BL233+1","v":229}]
[null,null,null,null,null,null,null,null,null,null,null,"Zinc oxide","Scottish Environment Protection Agency",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"",null,null,null,null,null,230]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"",null,null,null,null,null,231]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"",null,null,null,null,null,232]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"",null,null,null,null,null,233]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"",null,null,null,null,null,234]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"",null,null,null,null,null,235]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"",null,null,null,null,null,236]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"",null,null,null,null,null,237]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"",null,null,null,null,null,238]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"",null,null,null,null,null,239]
[]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"",null,null,null,null,null,{"$f":"BL245+1","v":240}]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"",null,null,null,null,null,{"$f":"BL247+1","v":241}]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"",null,null,null,null,null,242]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"",null,null,null,null,null,243]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"",null,null,null,null,null,244]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"",null,null,null,null,null,245]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"",null,null,null,null,null,246]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"",null,null,null,null,null,247]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"",null,null,null,null,null,248]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"",null,null,null,null,null,249]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"",null,null,null,null,null,250]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"",null,null,null,null,null,251]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"",null,null,null,null,null,252]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"",null,null,null,null,null,253]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"",null,null,null,null,null,254]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"",null,null,null,null,null,255]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"",null,null,null,null,null,256]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,257]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,258]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,{"$f":"BL265+1","v":259}]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,260]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,261]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,262]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,263]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,264]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,265]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,266]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,267]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,268]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,269]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,270]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,271]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,272]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,273]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,274]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,275]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,276]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,277]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,278]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,279]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,280]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,281]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,282]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,283]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,284]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,285]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,286]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,287]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,288]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,289]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,290]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,291]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,292]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,293]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,294]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,295]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,296]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,{"$f":"BL303+1","v":297}]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,{"$f":"BL304+1","v":298}]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,{"$f":"BL305+1","v":299}]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,{"$f":"BL306+1","v":300}]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[null,null,null,null,null,null,null,null,null,null,"Mecoprop (95%ile)"]
[null,null,null,null,null,null,null,null,null,null,"Mercury and its compounds (dissolved)"]
[null,null,null,null,null,null,null,null,null,null,"Methiocarb"]
[null,null,null,null,null,null,null,null,null,null,"Mevinphos"]
[null,null,null,null,null,null,null,null,null,null,"Naphthalene"]
[null,null,null,null,null,null,null,null,null,null,"Nickel and its compounds (dissolved)"]
[null,null,null,null,null,null,null,null,null,null,"Nitrilotriacetic acid (NTA)"]
[null,null,null,null,null,null,null,null,null,null,"Nonyl phenol (4-Nonylphenol)"]
[null,null,null,null,null,null,null,null,null,null,"NTA"]
[null,null,null,null,null,null,null,null,null,null,"Octyl phenol ((4-(1,1',3,3',-tetramethylbutyl)-phenol))"]
[null,null,null,null,null,null,null,null,null,null,"Omethoate"]
[null,null,null,null,null,null,null,null,null,null,"para-para DDT"]
[null,null,null,null,null,null,null,null,null,null,"PCSDs"]
[null,null,null,null,null,null,null,null,null,null,"Pendimethalin"]
[null,null,null,null,null,null,null,null,null,null,"Pentachlorobenzene"]
[null,null,null,null,null,null,null,null,null,null,"Pentachlorophenol"]
[null,null,null,null,null,null,null,null,null,null,"Perfluoroctane sulphonic acid and its salts (PFOS)"]
[null,null,null,null,null,null,null,null,null,null,"Permethrin (95%ile)"]
[null,null,null,null,null,null,null,null,null,null,"Phenol (95%ile)"]
[null,null,null,null,null,null,null,null,null,null,"Pirimiphos-methyl"]
[null,null,null,null,null,null,null,null,null,null,"Pirmicarb"]
[null,null,null,null,null,null,null,null,null,null,"Polyaromatic hydrocarbons (PAH): Benzo (a)pyrene. Polyaromatic hydrocarbons (PAH) - Benzo(a)-pyrene (BaP), Benzo(b)-fluor-anthene, Benzo(k)-fluor-anthene, Benzo(g,h,i)-perylene and Indeno(1,2,3-cd)-pyrene. Benzo(a)pyrene can be  considered as a marker for the other PAHs, hence only benzo(a)pyrene needs to be  monitored for comparison with the biota EQS or the corresponding AA-EQS in water"]
[null,null,null,null,null,null,null,null,null,null,"Prochloraz"]
[null,null,null,null,null,null,null,null,null,null,"Propetamphos"]
[null,null,null,null,null,null,null,null,null,null,"Propyzamide"]
[null,null,null,null,null,null,null,null,null,null,"Quinoxyfen"]
[null,null,null,null,null,null,null,null,null,null,"Silver"]
[null,null,null,null,null,null,null,null,null,null,"Silver (dissolved)"]
[null,null,null,null,null,null,null,null,null,null,"Simazine"]
[null,null,null,null,null,null,null,null,null,null,"Simazine (+ atrazine)"]
[null,null,null,null,null,null,null,null,null,null,"Styrene"]
[null,null,null,null,null,null,null,null,null,null,"Sulcophuron"]
[null,null,null,null,null,null,null,null,null,null,"Sulphate"]
[null,null,null,null,null,null,null,null,null,null,"Tecnazene (total)"]
[null,null,null,null,null,null,null,null,null,null,"Terbutryn"]
[null,null,null,null,null,null,null,null,null,null,"Tetrachloroethane"]
[null,null,null,null,null,null,null,null,null,null,"Tetrachloroethylene"]
[null,null,null,null,null,null,null,null,null,null,"Thiabendazole"]
[null,null,null,null,null,null,null,null,null,null,"Tin (inorganic) - dissolved"]
[null,null,null,null,null,null,null,null,null,null,"Toluene (95%ile)"]
[null,null,null,null,null,null,null,null,null,null,"Total anions"]
[null,null,null,null,null,null,null,null,null,null,"Triallate"]
[null,null,null,null,null,null,null,null,null,null,"Triazaphos"]
[null,null,null,null,null,null,null,null,null,null,"Tributyl phosphate"]
[null,null,null,null,null,null,null,null,null,null,"Tributyltin compounds (Tributyltin cation)"]
[null,null,null,null,null,null,null,null,null,null,"Trichlorobenzenes"]
[null,null,null,null,null,null,null,null,null,null,"Trichloroethylene"]
[null,null,null,null,null,null,null,null,null,null,"Trichloromethane (chloroform)"]
[null,null,null,null,null,null,null,null,null,null,"Triclosan"]
[null,null,null,null,null,null,null,null,null,null,"Trifluralin"]
[null,null,null,null,null,null,null,null,null,null,"Triphenyltin & derivatives"]
[null,null,null,null,null,null,null,null,null,null,"Un-ionised ammonia as nitrogen"]
[null,null,null,null,null,null,null,null,null,null,"Vanadium (> 200 mg/l CaCO3)"]
[null,null,null,null,null,null,null,null,null,null,"Vanadium (0 - 200 mg/l CaCO3)"]
[null,null,null,null,null,null,null,null,null,null,"Xylene"]
[null,null,null,null,null,null,null,null,null,null,"Zinc"]
[null,null,null,null,null,null,null,null,null,null,"Zinc - dissolved plus ambient background concentration. For saltwater, an ambient background concentration of 1.1ug/l is recommended."]

{"sheet":"SubstancesA","index":31,"n_rows":365,"n_cols":23,"rows_kept":365,"cut":false,"hidden":false,"merged":[]}
[]
[]
[]
[null,1,{"$f":"B4+1","v":2},{"$f":"C4+1","v":3},4,5,6,7,8,9,10,11,12,13,14,15,16,17,18,19,20,21]
[null,"SUBSubstance","SUBLongTermAirEAL","SUBShortTermAirEAL","SUBAirToLandDepositionRate","SUBGlobalWarmingFactor","SUBOzoneCreationFactor","SUBReleaseType","SUBUserAdded","SUBOtherPeriodValue","SUBFreshWaterMAC","SUBFreshWaterAnnual","SUBSaltWaterMAC","SubSaltWaterAnnual","SUBPriorityWaterEQS","SUBSigAnnualLoad","SUBOPRAName","SUBOPRAConvFromGram","SUBOPRAThreshold_Air","SUBOtherPeriod",null,null,{"$f":"IF(D6+E6>0,\"yes\",\"no\")","v":{"$error":"#VALUE!"}}]
["Country","SUBSubstance","SUBLongTermAirEAL","SUBShortTermAirEAL","SUBAirToLandDepositionRate","SUBGlobalWarmingFactor","SUBOzoneCreationFactor","SUBReleaseType","SUBUserAdded","SUBOtherPeriodValue","SUBFreshWaterMAC","SUBFreshWaterAnnual","SUBSaltWaterMAC","SubSaltWaterAnnual","SUBPriorityWaterEQS","SUBSigAnnualLoad","SUBOPRAName","SUBOPRAConvFromGram","SUBOPRAThreshold_Air"]
[{"$f":"\"Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency\"&B7","v":"Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyEthylene dibromide (1,2-Dibromoethane)"},"Ethylene dibromide (1,2-Dibromoethane)",7.8,234,null,null,null,"Air",false,0,null,null,null,null,false,null,null,null,null,null,null,null,{"$f":"IF(D8+E8>0,\"yes\",\"no\")","v":"no"}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyEthylene dichloride (1,2-Dichloroethane)","Ethylene dichloride (1,2-Dichloroethane)",3,null,null,null,null,"Air",false,0,null,10,null,10,false,null,"1,2-Dichloroethane",1000,100,null,null,null,{"$f":"IF(D9+E9>0,\"yes\",\"no\")","v":"yes"}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency1,3-Butadiene","1,3-Butadiene",2.25,2.25,null,null,85.1,"Air",false,0,null,null,null,null,false,null,"1,3-butadiene",1000,100,null,null,null,{"$f":"IF(#REF!+#REF!>0,\"yes\",\"no\")","v":{"$error":"#REF!"}}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency1,4-Dioxane","1,4-Dioxane",910,36600,null,null,null,"Air",false,0,null,null,null,null,false,null,"1,4-dioxane",1000,100,null,null,null,{"$f":"IF(#REF!+#REF!>0,\"yes\",\"no\")","v":{"$error":"#REF!"}}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyAcetaldehyde","Acetaldehyde",370,9200,null,null,64.099999999999994,"Air",false,0,null,null,null,null,false,null,"Acetaldehyde",1000,100,null,null,null,{"$f":"IF(D12+E12>0,\"yes\",\"no\")","v":"yes"}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyAcetic acid","Acetic acid",250,3700,null,null,9.6999999999999993,"Air",false,0,null,null,null,null,false,null,null,null,null,null,null,null,{"$f":"IF(D13+E13>0,\"yes\",\"no\")","v":"yes"}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyAcetic anhydride","Acetic anhydride",1,40,null,null,null,"Air",false,0,null,null,null,null,false,null,null,null,null,null,null,null,{"$f":"IF(D14+E14>0,\"yes\",\"no\")","v":"yes"}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyAcetone","Acetone",18100,362000,null,null,9.4,"Air",false,0,null,null,null,null,false,null,"Other VOCs Specify",null,null,null,null,null,{"$f":"IF(D15+E15>0,\"yes\",\"no\")","v":"yes"}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyAcetonitrile","Acetonitrile",680,10200,null,null,null,"Air",false,0,null,null,null,null,false,null,"Acetonitrile",1000,100,null,null,null,{"$f":"IF(#REF!+#REF!>0,\"yes\",\"no\")","v":{"$error":"#REF!"}}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyAcrylamide","Acrylamide",0.05,null,null,null,null,"Air",false,0,null,null,null,null,false,null,null,null,null,null,null,null,{"$f":"IF(D17+E17>0,\"yes\",\"no\")","v":"yes"}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyAcrylic acid","Acrylic acid",300,6000,null,null,null,"Air",false,0,null,null,null,null,false,null,null,null,null,null,null,null,"yes"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyAcrylonitrile","Acrylonitrile",8.8000000000000007,264,null,null,null,"Air",false,0,null,null,null,null,false,null,"Acrylonitrile",1000,10,null,null,null,"yes"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyAllyl alcohol","Allyl alcohol",48,970,null,null,null,"Air",false,0,null,null,null,null,false,null,"Allyl alcohol",1000,10,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyAmmonia (ecological-lichens and bryophytes)","Ammonia (ecological-lichens and bryophytes)",1,null,null,null,null,"Air",false,0,null,null,null,null,false,null,"Ammonia",1000,100,null,null,null,{"$f":"IF(D22+E22>0,\"yes\",\"no\")","v":"yes"}]
[{"$f":"\"Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency\"&B21","v":"Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyAmmonia (ecological-other vegetation)"},"Ammonia (ecological-other vegetation)",3,null,null,null,null,"Air",false,0,null,null,null,null,false,null,"Ammonia",1000,100,null,null,null,{"$f":"IF(D23+E23>0,\"yes\",\"no\")","v":"yes"}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyAmmonia","Ammonia",180,2500,null,null,null,"Air",false,0,null,null,null,null,false,null,"Ammonia",1000,100,null,null,null,"yes"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyAniline","Aniline",8,240,null,null,null,"Air",false,0,null,null,null,null,false,null,"Aniline",1000,10,null,null,null,"yes"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyAntimony and compounds (as Sb), except antimony trisulphide and antimony trioxide","Antimony and compounds (as Sb), except antimony trisulphide and antimony trioxide",5,150,null,null,null,"Air",false,0,null,null,null,null,false,null,"Antimony",1000,10,null,null,null,"yes"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyArsenic and compounds (as As)","Arsenic and compounds (as As)",6.0000000000000001E-3,null,0.02,null,null,"Air",false,0,null,null,null,null,false,null,"Arsenic",1000,10,null,null,null,"yes"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyArsine","Arsine",1.6,48,null,null,null,"Air",false,0,null,null,null,null,false,null,null,null,null,null,null,null,{"$f":"IF(#REF!+#REF!>0,\"yes\",\"no\")","v":{"$error":"#REF!"}}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyBenzene","Benzene",5,30,null,null,21.8,"Both",false,0,50,10,50,8,false,null,"Benzene",1000,10,null,null,null,{"$f":"IF(D28+E28>0,\"yes\",\"no\")","v":"no"}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyBenzo-a-pyrene","Benzo-a-pyrene",2.5000000000000001E-4,null,null,null,323,"Air",false,0,0.27,1.7000000000000001E-4,0.27,1.7000000000000001E-4,false,null,"Benzo(a)pyrene",1000,1,null,null,null,"yes"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyBenzylchloride","Benzylchloride",5.2,158,null,null,null,"Air",false,0,null,null,null,null,false,null,"Benzyl Chloride",1000,10,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyBeryllium and compounds (as Be)","Beryllium and compounds (as Be)",2.0000000000000001E-4,null,null,null,null,"Air",false,0,null,null,null,null,false,null,"Beryllium",1000,1,null,null,null,"yes"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyBoron trifluoride","Boron trifluoride",null,280,null,null,null,"Air",false,0,null,null,null,null,false,null,null,null,null,null,null,null,"yes"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyBromine","Bromine",null,70,null,null,null,"Both",false,0,5,2,10,null,false,null,null,null,null,null,null,null,"yes"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyBromomethane","Bromomethane",200,5900,null,null,null,"Air",false,0,null,null,null,null,false,null,null,null,null,null,null,null,{"$f":"IF(#REF!+#REF!>0,\"yes\",\"no\")","v":{"$error":"#REF!"}}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyMethyl ethyl ketone (MEK, 2-Butanone)","Methyl ethyl ketone (MEK, 2-Butanone)",6000,89900,null,null,null,"Air",false,0,null,null,null,null,false,null,null,null,null,null,null,null,{"$f":"IF(D35+E35>0,\"yes\",\"no\")","v":"yes"}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyButane","Butane",14500,181000,null,null,null,"Air",false,0,null,null,null,null,false,null,"Other VOCs Specify",1000,1000,null,null,null,{"$f":"IF(#REF!+#REF!>0,\"yes\",\"no\")","v":{"$error":"#REF!"}}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyCadmium and compounds (as Cd)","Cadmium and compounds (as Cd)",5.0000000000000001E-3,0.03,8.9999999999999993E-3,null,null,"Air",false,0,null,null,null,null,false,null,"Cadmium",1000,1,null,null,null,{"$f":"IF(#REF!+#REF!>0,\"yes\",\"no\")","v":{"$error":"#REF!"}}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyCarbon disulphide","Carbon disulphide",64,100,null,null,null,"Air",false,0,null,null,null,null,false,null,"Carbon Disulphide",1000,100,null,null,null,{"$f":"IF(D38+E38>0,\"yes\",\"no\")","v":"yes"}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyCarbon monoxide","Carbon monoxide",null,10000,null,null,2.7,"Air",false,0,null,null,null,null,false,null,"Carbon Monoxide",1000000,1000,null,null,null,{"$f":"IF(D39+E39>0,\"yes\",\"no\")","v":"yes"}]
[{"$f":"\"Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency\"&B39","v":"Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyCarbon tetrachloride"},"Carbon tetrachloride",130,3900,null,1400,null,"Both",false,0,null,12,null,12,false,null,"Carbon Tetrachloride",1000,1.0000000000000001E-5,null,null,null,{"$f":"IF(#REF!+#REF!>0,\"yes\",\"no\")","v":{"$error":"#REF!"}}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyChlorine","Chlorine",null,290,null,null,null,"Air",false,0,null,null,null,null,false,null,"Chlorine",1000,10,null,null,null,{"$f":"IF(D41+E41>0,\"yes\",\"no\")","v":"no"}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyChloroform","Chloroform",100,null,null,4,1.7,"Air",false,0,null,null,null,null,false,null,"Chloroform",1000,10,null,null,null,{"$f":"IF(D42+E42>0,\"yes\",\"no\")","v":"no"}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyMethyl chloride (chloromethane)","Methyl chloride (chloromethane)",18,null,null,null,0.5,"Air",false,0,null,null,null,null,false,null,"Chloromethane",1000,500,null,null,null,{"$f":"IF(D43+E43>0,\"yes\",\"no\")","v":"no"}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyChromium (VI) compounds (as Cr)","Chromium (VI) compounds (as Cr)",2.5000000000000001E-4,null,null,null,null,"Air",false,0,null,null,null,null,false,null,"Chromium",1000,10,null,null,null,{"$f":"IF(D44+E44>0,\"yes\",\"no\")","v":"yes"}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyChromium (III) compounds (as Cr)","Chromium (III) compounds (as Cr)",2,null,1.5,null,null,"Air",false,0,null,null,null,null,false,null,"Chromium",1000,10,null,null,null,{"$f":"IF(#REF!+#REF!>0,\"yes\",\"no\")","v":{"$error":"#REF!"}}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyCopper and compounds (as Cu)","Copper and compounds (as Cu)",0.05,null,0.25,null,null,"Air",false,0,null,null,null,null,false,null,"Other Metals Specify",1000,100,null,null,null,{"$f":"IF(#REF!+#REF!>0,\"yes\",\"no\")","v":{"$error":"#REF!"}}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyDibutyl phthalate (DBP)","Dibutyl phthalate (DBP)",50,1000,null,null,null,"Air",false,0,null,null,null,null,false,null,null,null,null,null,null,null,{"$f":"IF(D47+E47>0,\"yes\",\"no\")","v":"yes"}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyMethylene chloride (dichloromethane)","Methylene chloride (dichloromethane)",770,2100,null,9,6.8,"Both",false,0,null,20,null,20,false,null,null,null,null,null,null,null,{"$f":"IF(D48+E48>0,\"yes\",\"no\")","v":"yes"}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyDiethyl ether","Diethyl ether",12300,154000,null,null,44.52,"Air",false,0,null,null,null,null,false,null,null,null,null,null,null,null,{"$f":"IF(D49+E49>0,\"yes\",\"no\")","v":"yes"}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyDiethylketone","Diethylketone",7160,89500,null,null,41.4,"Air",false,0,null,null,null,null,false,null,null,null,null,null,null,null,{"$f":"IF(D50+E50>0,\"yes\",\"no\")","v":"yes"}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyDiisopropyl ether","Diisopropyl ether",10600,131000,null,null,39.82,"Air",false,0,null,null,null,null,false,null,null,null,null,null,null,null,{"$f":"IF(D51+E51>0,\"yes\",\"no\")","v":"yes"}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyDiisobutyl phthalate","Diisobutyl phthalate",50,1500,null,null,null,"Air",false,0,null,null,null,null,false,null,null,null,null,null,null,null,{"$f":"IF(#REF!+#REF!>0,\"yes\",\"no\")","v":{"$error":"#REF!"}}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyDimethyl sulphate","Dimethyl sulphate",0.52,15.6,null,null,null,"Air",false,0,null,null,null,null,false,null,"Di-methyl sulphate",1000,1,null,null,null,{"$f":"IF(D53+E53>0,\"yes\",\"no\")","v":"yes"}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyDimethylformamide","Dimethylformamide",300,6100,null,null,null,"Air",false,0,null,null,null,null,false,null,"Dimethylformamide",1000,100,null,null,null,{"$f":"IF(#REF!+#REF!>0,\"yes\",\"no\")","v":{"$error":"#REF!"}}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyEthyl acrylate","Ethyl acrylate",210,6200,null,null,null,"Air",false,0,null,null,null,null,false,null,"Ethyl acrylate",1000,100,null,null,null,{"$f":"IF(D55+E55>0,\"yes\",\"no\")","v":"yes"}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyEthylbenzene","Ethylbenzene",4410,55200,null,null,73,"Air",false,0,null,null,null,null,false,null,"Other VOCs Specify",1000,1000,null,null,null,{"$f":"IF(#REF!+#REF!>0,\"yes\",\"no\")","v":{"$error":"#REF!"}}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyEthylene oxide","Ethylene oxide",2E-3,null,null,null,null,"Air",false,0,null,null,null,null,false,null,"Ethylene oxide",1000,10,null,null,null,{"$f":"IF(#REF!+#REF!>0,\"yes\",\"no\")","v":{"$error":"#REF!"}}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyFormaldehyde","Formaldehyde",5,100,null,null,51.9,"Both",false,0,50,5,null,null,false,null,null,null,null,null,null,null,{"$f":"IF(#REF!+#REF!>0,\"yes\",\"no\")","v":{"$error":"#REF!"}}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyHydrazine","Hydrazine",0.06,2.6,null,null,null,"Air",false,0,null,null,null,null,false,null,null,null,null,null,null,null,{"$f":"IF(D59+E59>0,\"yes\",\"no\")","v":"yes"}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyHydrogen bromide","Hydrogen bromide",null,700,null,null,null,"Air",false,0,null,null,null,null,false,null,"Hydrogen Bromide",1000,10,null,null,null,"yes"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyHydrogen chloride","Hydrogen chloride",null,750,null,null,null,"Air",false,0,null,null,null,null,false,null,"Hydrogen Chloride",1000,1000,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyHydrogen cyanide","Hydrogen cyanide",2,null,null,null,null,"Air",false,0,null,null,null,null,false,null,null,null,null,null,null,"Daily Average","yes"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyHydrogen fluoride (ecological)","Hydrogen fluoride (ecological)",0.5,5,null,null,null,"Air",false,0,null,null,null,null,false,null,"Hydrogen Fluoride",1000,10,null,null,"Weekly Average",{"$f":"IF(#REF!+#REF!>0,\"yes\",\"no\")","v":{"$error":"#REF!"}}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyHydrogen fluoride","Hydrogen fluoride",16,160,2.1,null,null,"Air",false,0,null,null,null,null,false,null,"Hydrogen Fluoride",1000,10,null,null,"Monthly Average","yes"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyHydrogen iodide","Hydrogen iodide",5,520,null,null,null,"Air",false,0,null,null,null,null,false,null,"Hydrogen Iodide",1000,10,null,null,null,"yes"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyHydrogen sulphide","Hydrogen sulphide",140,150,null,null,null,"Both",false,0,1,0.25,10,null,false,null,null,null,null,null,null,null,{"$f":"IF(#REF!+#REF!>0,\"yes\",\"no\")","v":{"$error":"#REF!"}}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyLead","Lead",0.25,null,1.1000000000000001,null,null,"Air",false,0,null,null,null,null,false,null,"Lead",1000,1,null,null,null,{"$f":"IF(D67+E67>0,\"yes\",\"no\")","v":"yes"}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyManganese and compounds (as Mn)","Manganese and compounds (as Mn)",0.15,1500,null,null,null,"Air",false,0,null,123,null,null,false,null,"Other Metals Specify",1000,100,null,null,null,{"$f":"IF(D68+E68>0,\"yes\",\"no\")","v":"yes"}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyMercury and its inorganic compounds (as Hg)","Mercury and its inorganic compounds (as Hg)",0.06,0.6,4.0000000000000001E-3,null,null,"Air",false,0,null,null,null,null,false,null,"Mercury",1000,1,null,null,null,{"$f":"IF(#REF!+#REF!>0,\"yes\",\"no\")","v":{"$error":"#REF!"}}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyMethanol","Methanol",2660,33300,null,null,14.02,"Air",false,0,null,null,null,null,false,null,null,null,null,null,null,null,{"$f":"IF(#REF!+#REF!>0,\"yes\",\"no\")","v":{"$error":"#REF!"}}]
[{"$f":"\"Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency\"&B70","v":"Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyMethyl chloroform"},"Methyl chloroform",5000,null,null,110,0.9,"Air",false,0,null,null,null,null,false,null,null,null,null,null,null,null,{"$f":"IF(#REF!+#REF!>0,\"yes\",\"no\")","v":{"$error":"#REF!"}}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyMolydenum","Molydenum",null,null,1.6E-2,null,null,"Air",false,0,null,null,null,null,false,null,"Other Metals Specify",1000,100,null,null,"",{"$f":"IF(D72+E72>0,\"yes\",\"no\")","v":"yes"}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyMono-ethanolamine (MEA)","Mono-ethanolamine (MEA)",100,400,null,null,null,"",null,null,null,null,null,null,null,"","",null,null,"","","",{"$f":"IF(#REF!+#REF!>0,\"yes\",\"no\")","v":{"$error":"#REF!"}}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyNaphthalene","Naphthalene",3,null,null,null,null,"Both",false,0,130,2,130,2,false,null,"Napthalene",1000,1.0000000000000001E-5,null,null,null,{"$f":"IF(#REF!+#REF!>0,\"yes\",\"no\")","v":{"$error":"#REF!"}}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyN-hexane","N-hexane",720,21600,null,null,48.2,"Air",false,0,null,null,null,null,false,null,"Other VOCs Specify",1000,1000,null,null,null,{"$f":"IF(D75+E75>0,\"yes\",\"no\")","v":"yes"}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyNickel and compounds (as Ni) except nickel carbonyl","Nickel and compounds (as Ni) except nickel carbonyl",0.02,0.7,0.11,null,null,"Air",false,0,null,null,null,null,false,null,"Nickel",1000,10,null,null,null,{"$f":"IF(D76+E76>0,\"yes\",\"no\")","v":"yes"}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyNitric acid","Nitric acid",52,1000,null,null,null,"Air",false,0,null,null,null,null,false,null,null,null,null,null,null,null,{"$f":"IF(D77+E77>0,\"yes\",\"no\")","v":"yes"}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyNitrogen dioxide","Nitrogen dioxide",40,200,null,null,2.8,"Air",false,0,null,null,null,null,false,null,"Oxides of Nitrogen",1000000,10,null,null,"Daily Mean",{"$f":"IF(D78+E78>0,\"yes\",\"no\")","v":"yes"}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyNitrogen oxides (as NO2) (ecological)","Nitrogen oxides (as NO2) (ecological)",30,75,null,null,2.8,"Air",false,0,null,null,null,null,false,null,"Oxides of Nitrogen",1000000,10,null,null,null,{"$f":"IF(D79+E79>0,\"yes\",\"no\")","v":"yes"}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyNitrogen monoxide (nitric oxide)","Nitrogen monoxide (nitric oxide)",310,4400,null,null,-42.7,"Air",false,0,null,null,null,null,false,null,"Oxides of Nitrogen",1000000,10,null,null,"",{"$f":"IF(#REF!+#REF!>0,\"yes\",\"no\")","v":{"$error":"#REF!"}}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyN-nitrosodimethylamine (NDMA)","N-nitrosodimethylamine (NDMA)",2.0000000000000001E-4,null,null,null,null,"",null,null,null,null,null,null,null,"","",null,null,"","",null,{"$f":"IF(#REF!+#REF!>0,\"yes\",\"no\")","v":{"$error":"#REF!"}}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyOrthophosphoric acid","Orthophosphoric acid",null,200,null,null,null,"Air",false,0,null,null,null,null,false,null,null,null,null,null,null,null,{"$f":"IF(#REF!+#REF!>0,\"yes\",\"no\")","v":{"$error":"#REF!"}}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyOzone","Ozone",null,100,null,null,null,"Air",false,0,null,null,null,null,false,null,null,null,null,null,null,"8 hr Mean",{"$f":"IF(D84+E84>0,\"yes\",\"no\")","v":"yes"}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyPara dichlorobenzene","Para dichlorobenzene",1530,30600,null,null,null,"Air",false,0,null,null,null,null,false,null,null,null,null,null,null,null,{"$f":"IF(#REF!+#REF!>0,\"yes\",\"no\")","v":{"$error":"#REF!"}}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyParticulates (PM10)","Particulates (PM10)",40,50,null,null,null,"Air",false,0,null,null,null,null,false,null,"Particulates",1000,100,null,null,"24 hr Mean",{"$f":"IF(#REF!+#REF!>0,\"yes\",\"no\")","v":{"$error":"#REF!"}}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyParticulates (PM2.5)","Particulates (PM2.5)",20,null,null,null,null,"Air",false,0,null,null,null,null,false,null,"Particulates",1000,100,null,null,null,{"$f":"IF(#REF!+#REF!>0,\"yes\",\"no\")","v":{"$error":"#REF!"}}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyMethyl propyl ketone (MPK, 2-Pentanone)","Methyl propyl ketone (MPK, 2-Pentanone)",7160,89500,null,null,null,"Air",false,0,null,null,null,null,false,null,null,null,null,null,null,null,{"$f":"IF(D87+E87>0,\"yes\",\"no\")","v":"yes"}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyDiethyl ketone (3-Pentanone)","Diethyl ketone (3-Pentanone)",7160,89500,null,null,null,"Air",false,0,null,null,null,null,false,null,null,null,null,null,null,null,{"$f":"IF(#REF!+#REF!>0,\"yes\",\"no\")","v":{"$error":"#REF!"}}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyPhenol","Phenol",200,3900,null,null,null,"Air",false,0,null,null,null,null,false,null,"Phenol",1000,100,null,null,null,{"$f":"IF(D89+E89>0,\"yes\",\"no\")","v":"yes"}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyPhosgene","Phosgene",0.8,25,null,null,null,"Air",false,0,null,null,null,null,false,null,"Phosgene",1000,1,null,null,null,"yes"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyPhosphine","Phosphine",null,42,null,null,null,"Air",false,0,null,null,null,null,false,null,null,null,null,null,null,null,"yes"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyPolychlorinated biphenyls (PCBs)","Polychlorinated biphenyls (PCBs)",0.2,6,null,null,null,"Air",false,0,null,null,null,null,false,null,"PCBs",1E-3,0.1,null,null,null,{"$f":"IF(#REF!+#REF!>0,\"yes\",\"no\")","v":{"$error":"#REF!"}}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency1-propanol","1-propanol",5000,62500,null,null,56.12,"Air",false,0,null,null,null,null,false,null,null,null,null,null,null,null,"yes"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency2-propanol","2-propanol",9990,125000,null,null,18.82,"Air",false,0,null,null,null,null,false,null,null,null,null,null,null,null,{"$f":"IF(#REF!+#REF!>0,\"yes\",\"no\")","v":{"$error":"#REF!"}}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyPropylene oxide","Propylene oxide",24,720,null,null,null,"Air",false,0,null,null,null,null,false,null,"Propylene oxide",1000,100,null,null,null,{"$f":"IF(#REF!+#REF!>0,\"yes\",\"no\")","v":{"$error":"#REF!"}}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencySelenium and compounds (as Se), except hydrogen selenide","Selenium and compounds (as Se), except hydrogen selenide",2,null,1.2E-2,null,null,"Air",false,0,null,null,null,null,false,null,"Selenium",1000,10,null,null,null,{"$f":"IF(D96+E96>0,\"yes\",\"no\")","v":"yes"}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencySodium hydroxide","Sodium hydroxide",null,200,null,null,null,"Air",false,0,null,null,null,null,false,null,null,null,null,null,null,null,{"$f":"IF(D97+E97>0,\"yes\",\"no\")","v":"yes"}]
[{"$f":"\"Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency\"&B97","v":"Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyStyrene"},"Styrene",260,800,null,null,14.2,"Both",false,0,500,50,500,50,false,null,"Styrene",1000,500,null,null,"",{"$f":"IF(#REF!+#REF!>0,\"yes\",\"no\")","v":{"$error":"#REF!"}}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencySulphur dioxide  (15 min mean)","Sulphur dioxide  (15 min mean)",null,266,null,null,4.8,"Air",false,0,null,null,null,null,false,null,"Oxides of Sulphur",1000000,10,null,null,"15 Min Mean",{"$f":"IF(#REF!+#REF!>0,\"yes\",\"no\")","v":{"$error":"#REF!"}}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencySulphur dioxide (24 hr mean)","Sulphur dioxide (24 hr mean)",null,125,null,null,4.8,"Air",false,0,null,null,null,null,false,null,"Oxides of Sulphur",1000000,10,null,null,"24 Hr Mean",{"$f":"IF(D100+E100>0,\"yes\",\"no\")","v":"no"}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencySulphur dioxide (ecological-lichens and bryophytes)","Sulphur dioxide (ecological-lichens and bryophytes)",10,null,null,null,4.8,"Air",false,0,null,null,null,null,false,null,"Oxides of Sulphur",1000000,10,null,null,null,{"$f":"IF(#REF!+#REF!>0,\"yes\",\"no\")","v":{"$error":"#REF!"}}]
[{"$f":"\"Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency\"&B101","v":"Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencySulphur dioxide (ecological-other vegetation)"},"Sulphur dioxide (ecological-other vegetation)",20,null,null,null,4.8,"Air",false,0,null,null,null,null,false,null,"Oxides of Sulphur",1000000,10,null,null,null,{"$f":"IF(#REF!+#REF!>0,\"yes\",\"no\")","v":{"$error":"#REF!"}}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencySulphur hexafluoride","Sulphur hexafluoride",60700,759000,null,23900,null,"Air",false,0,null,null,null,null,false,null,null,null,null,null,null,null,"yes"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencySulphuric acid","Sulphuric acid",10,300,null,null,null,"Air",false,0,null,null,null,null,false,null,null,null,null,null,null,null,{"$f":"IF(#REF!+#REF!>0,\"yes\",\"no\")","v":{"$error":"#REF!"}}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyTetrachloroethylene","Tetrachloroethylene",40,null,null,null,2.9,"Both",false,0,null,10,null,10,false,null,"Tetrachloroethylene",1000,500,null,null,null,{"$f":"IF(D105+E105>0,\"yes\",\"no\")","v":"yes"}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyTetrahydrofuran","Tetrahydrofuran",3000,59900,null,null,null,"Air",false,0,null,null,null,null,false,null,"Dioxins and Furans",1E-3,0.1,null,null,null,{"$f":"IF(D106+E106>0,\"yes\",\"no\")","v":"yes"}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyToluene","Toluene",260,8000,null,null,63.7,"Air",false,0,null,null,null,null,false,null,null,null,null,null,null,"",{"$f":"IF(#REF!+#REF!>0,\"yes\",\"no\")","v":{"$error":"#REF!"}}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyTrichloroethylene","Trichloroethylene",2,null,null,null,32.5,"Both",false,0,null,10,null,10,false,null,"Trichloroethylene",1000,500,null,null,null,{"$f":"IF(D109+E109>0,\"yes\",\"no\")","v":"yes"}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency1,2,4-Trichlorobenzene","1,2,4-Trichlorobenzene",76,2280,null,null,null,"air",false,0,null,null,null,null,false]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyTrimethylbenzenes, all isomers or mixtures","Trimethylbenzenes, all isomers or mixtures",1250,37500,null,null,null,"Air",false,0,null,null,null,null,false,null,"Trimethylbenzene",1000,500,null,null,null,{"$f":"IF(D110+E110>0,\"yes\",\"no\")","v":"yes"}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyVanadium and compounds (as V)","Vanadium and compounds (as V)",null,1,null,null,null,"Air",false,0,null,null,null,null,false,null,"Other Metals Specify",1000,100,null,null,null,"yes"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyVinyl acetate","Vinyl acetate",360,7200,null,null,null,"Air",false,0,null,null,null,null,false,null,null,null,null,null,null,null,"yes"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyVinyl chloride","Vinyl chloride",10,1300,null,null,27.21,"Air",false,0,null,null,null,null,false,null,null,null,null,null,null,null,"yes"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyXylene, o-, m-, p- or mixed isomers","Xylene, o-, m-, p- or mixed isomers",4410,66200,null,null,null,"Air",false,0,null,null,null,null,false,null,"Xylene",1000,500,null,null,null,"yes"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment AgencyZinc oxide","Zinc oxide",50,1000,0.48,null,null,"Air",false,0,null,null,null,null,false,null,null,null,null,null,null,"","no"]
[{"$f":"\"Scottish Environment Protection Agency\"&B115","v":"Scottish Environment Protection Agency1,1 Dichloroethane "},"1,1 Dichloroethane ",null,null,null,null,23.21,"Air",false,0,null,null,null,null,false,"","",null,null,"","",null,"no"]
[{"$f":"\"Scottish Environment Protection Agency\"&B116","v":"Scottish Environment Protection AgencyMethyl chloroform"},"Methyl chloroform",5000,null,null,110,0.9,"Air",false,0,null,null,null,null,false,"","1,1,1-trichloroethane",1000,500,"","","","no"]
["Scottish Environment Protection Agency1,2,3-trimethylbenzene","1,2,3-trimethylbenzene",null,null,null,null,126.7,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"yes"]
["Scottish Environment Protection Agency1,2,4-Trichlorobenzene","1,2,4-Trichlorobenzene",76,2280,null,null,null,"Air",false,0,null,null,null,null,false,"","",null,null,"","","","no"]
["Scottish Environment Protection Agency1,2,4-trimethylbenzene","1,2,4-trimethylbenzene",null,null,null,null,127.8,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,"","yes"]
["Scottish Environment Protection Agency1,2-Dibromoethane","1,2-Dibromoethane",7.8,234,null,null,null,"Air",false,0,null,null,null,null,false,"","",null,null,"","","","no"]
["Scottish Environment Protection Agency1,2-Dichloroethane (Ethylene dichloride)","1,2-Dichloroethane (Ethylene dichloride)",3,null,null,null,null,"Both",false,0,null,10,null,10,false,"","1,2-Dichloroethane",1000,100,"","","","yes"]
["Scottish Environment Protection Agency1,3-Butadiene","1,3-Butadiene",2.25,2.25,null,null,85.1,"Air",false,0,null,null,null,null,false,"","1,3-butadiene",1000,100,"","",null,"no"]
["Scottish Environment Protection Agency1,3,5-trimethylbenzene","1,3,5-trimethylbenzene",null,null,null,null,138.1,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"yes"]
["Scottish Environment Protection Agency1,4-Dichlorobenzene","1,4-Dichlorobenzene",120,6000,null,null,null,"Air",false,0,null,null,null,null,false,"","1,4-dichlorobenzene",1000,500,"","","","yes"]
["Scottish Environment Protection Agency1,4-Dioxane","1,4-Dioxane",730,36600,null,null,null,"Air",false,0,null,null,null,null,false,"","1,4-dioxane",1000,100,"","","","no"]
["Scottish Environment Protection Agency1-butoxy-2-propanol","1-butoxy-2-propanol",null,null,null,null,46.32,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection Agency1-Methoxypropan-2-ol","1-Methoxypropan-2-ol",null,null,null,null,35.520000000000003,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection Agency2,2-dimethylbutane","2,2-dimethylbutane",null,null,null,null,24.1,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection Agency2,3-dimethylbutane","2,3-dimethylbutane",null,null,null,null,54.1,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection Agency2-Butoxyethanol","2-Butoxyethanol",null,null,null,null,48.32,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection Agency2-Ethoxyethanol","2-Ethoxyethanol",null,null,null,null,38.619999999999997,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection Agency2-Methoxyethanol","2-Methoxyethanol",null,null,null,null,30.72,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection Agency2-methyl-1-butanol","2-methyl-1-butanol",null,null,null,null,48.92,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection Agency2-methyl-2-butanol","2-methyl-2-butanol",null,null,null,null,22.82,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection Agency2-methylbut-1-ene","2-methylbut-1-ene",null,null,null,null,77.099999999999994,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection Agency2-methylbut-2-ene","2-methylbut-2-ene",null,null,null,null,84.2,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection Agency2-methylhexane","2-methylhexane",null,null,null,null,41.1,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection Agency2-methylnonane","2-methylnonane",null,null,null,null,65.709999999999994,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection Agency2-methyloctane","2-methyloctane",null,null,null,null,70.61,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection Agency2-methylpentane","2-methylpentane",null,null,null,null,42,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection Agency2-Methylpropan-1-ol","2-Methylpropan-1-ol",null,null,null,null,36.020000000000003,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection Agency2-Methylpropan-2-ol","2-Methylpropan-2-ol",null,null,null,null,10.62,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection Agency3,5-diethyltoluene","3,5-diethyltoluene",null,null,null,null,129.5,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection Agency3,5-dimethylethylbenzene","3,5-dimethylethylbenzene",null,null,null,null,132,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection Agency3-methyl-1-butanol","3-methyl-1-butanol",null,null,null,null,43.32,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection Agency3-methyl-2-butanol","3-methyl-2-butanol",null,null,null,null,40.619999999999997,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection Agency3-methylbut-1-ene","3-methylbut-1-ene",null,null,null,null,67.099999999999994,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection Agency3-methylhexane","3-methylhexane",null,null,null,null,36.4,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection Agency3-methylpentane","3-methylpentane",null,null,null,null,47.9,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection Agency3-pentanol","3-pentanol",null,null,null,null,59.52,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection Agency4-Hydroxy-4-methyl-pentan-2-one","4-Hydroxy-4-methyl-pentan-2-one",null,null,null,null,30.72,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"yes"]
["Scottish Environment Protection AgencyAcetaldehyde","Acetaldehyde",370,9200,null,null,64.099999999999994,"Air",false,0,null,null,null,null,false,"","Acetaldehyde",1000,100,"","","","yes"]
["Scottish Environment Protection AgencyAcetic acid","Acetic acid",250,3700,null,null,9.6999999999999993,"Air",false,0,null,null,null,null,false,"","",null,null,"","","","yes"]
["Scottish Environment Protection AgencyAcetic anhydride","Acetic anhydride",1,40,null,null,null,"Air",false,0,null,null,null,null,false,"","",null,null,"","","","yes"]
["Scottish Environment Protection AgencyAcetone","Acetone",12100,362000,null,null,9.4,"Air",false,0,null,null,null,null,false,"","Other VOCs Specify",null,null,"","","","yes"]
["Scottish Environment Protection AgencyAcetonitrile","Acetonitrile",680,10200,null,null,null,"Air",false,0,null,null,null,null,false,"","Acetonitrile",1000,100,"","","","no"]
["Scottish Environment Protection AgencyAcetylene","Acetylene",null,null,null,null,8.5,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,"","no"]
["Scottish Environment Protection AgencyAcrylamide","Acrylamide",0.05,null,null,null,null,"Air",false,0,null,null,null,null,false,"","",null,null,"","","","yes"]
["Scottish Environment Protection AgencyAcrylic acid","Acrylic acid",290,5900,null,null,null,"Air",false,0,null,null,null,null,false,"","",null,null,"","","","yes"]
["Scottish Environment Protection AgencyAcrylonitrile","Acrylonitrile",8.8000000000000007,264,null,null,null,"Air",false,0,null,null,null,null,false,"","Acrylonitrile",1000,10,"","","","yes"]
["Scottish Environment Protection AgencyAllyl alcohol","Allyl alcohol",48,970,null,null,null,"Air",false,0,null,null,null,null,false,"","Allyl alcohol",1000,10,"","","","no"]
["Scottish Environment Protection AgencyAmmonia (ecological-lichens and bryophytes)","Ammonia (ecological-lichens and bryophytes)",1,null,null,null,null,"Air",false,0,null,null,null,null,false,"","Ammonia",1000,100,"","",null,{"$f":"IF(D164+E164>0,\"yes\",\"no\")","v":"yes"}]
[{"$f":"\"Scottish Environment Protection Agency\"&B163","v":"Scottish Environment Protection AgencyAmmonia (ecological-other vegetation)"},"Ammonia (ecological-other vegetation)",3,null,null,null,null,"Air",false,0,null,null,null,null,false,"","Ammonia",1000,100,"","",null,{"$f":"IF(D165+E165>0,\"yes\",\"no\")","v":"yes"}]
["Scottish Environment Protection AgencyAmmonia (human health receptor)","Ammonia (human health receptor)",180,2500,null,null,null,"Air",false,0,null,null,null,null,false,"","Ammonia",1000,100,"","","","yes"]
["Scottish Environment Protection AgencyAniline","Aniline",8,240,null,null,null,"Air",false,0,null,null,null,null,false,"","Aniline",1000,10,"","","","yes"]
["Scottish Environment Protection AgencyAntimony and compounds (as Sb), except antimony trisulphide and antimony trioxide","Antimony and compounds (as Sb), except antimony trisulphide and antimony trioxide",5,150,null,null,null,"Air",false,0,null,null,null,null,false,"","Antimony",1000,10,"","","","yes"]
["Scottish Environment Protection AgencyArsenic and compounds (as As)","Arsenic and compounds (as As)",6.0000000000000001E-3,null,0.02,null,null,"Air",false,0,null,null,null,null,false,"","Arsenic",1000,10,"","","","yes"]
["Scottish Environment Protection AgencyArsine","Arsine",1.6,48,null,null,null,"Air",false,0,null,null,null,null,false,"","",null,null,"","","","no"]
["Scottish Environment Protection AgencyBenzaldehyde","Benzaldehyde",null,null,null,null,-9.1999999999999993,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,"","yes"]
["Scottish Environment Protection AgencyBenzene","Benzene",3.25,30,null,null,21.8,"Both",false,0,50,10,50,8,false,"","Benzene",1000,10,"","","","no"]
["Scottish Environment Protection AgencyBenzo-a-pyrene","Benzo-a-pyrene",2.5000000000000001E-4,null,null,null,323,"Air",false,0,0.27,1.7000000000000001E-4,0.27,1.7000000000000001E-4,false,"","Benzo(a)pyrene",1000,1,"","","","yes"]
["Scottish Environment Protection AgencyBenzylchloride","Benzylchloride",5.2,158,null,null,null,"Air",false,0,null,null,null,null,false,"","Benzyl Chloride",1000,10,"","","","no"]
["Scottish Environment Protection AgencyBeryllium and compounds (as Be)","Beryllium and compounds (as Be)",2.0000000000000001E-4,null,null,null,null,"Air",false,0,null,null,null,null,false,"","Beryllium",1000,1,"","",null,{"$f":"IF(D174+E174>0,\"yes\",\"no\")","v":"yes"}]
["Scottish Environment Protection AgencyBoron trifluoride","Boron trifluoride",null,280,null,null,null,"Air",false,0,null,null,null,null,false,"","",null,null,"","","","yes"]
["Scottish Environment Protection AgencyBromine","Bromine",null,70,null,null,null,"Both",false,0,5,2,10,null,false,"","",null,null,"","","","yes"]
["Scottish Environment Protection AgencyBromomethane","Bromomethane",200,5900,null,null,null,"Air",false,0,null,null,null,null,false,"","",null,null,"","","","no"]
["Scottish Environment Protection AgencyBut -1- ene","But -1- ene",null,null,null,null,107.9,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection AgencyButa-1,3-diene","Buta-1,3-diene",null,null,null,null,85.1,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection AgencyButan-1-ol","Butan-1-ol",null,null,null,null,62.02,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection AgencyButan-2-ol","Butan-2-ol",null,null,null,null,44.72,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"yes"]
[{"$f":"\"Scottish Environment Protection Agency\"&B181","v":"Scottish Environment Protection AgencyButan-2-one (Methylethylketone)"},"Butan-2-one (Methylethylketone)",6000,89900,null,null,null,"Air",false,0,null,null,null,null,false,"","",null,null,"","","","yes"]
["Scottish Environment Protection AgencyButane","Butane",14500,181000,null,null,null,"Air",false,0,null,null,null,null,false,"","Other VOCs Specify",1000,1000,"","","","no"]
["Scottish Environment Protection AgencyButyraldehyde","Butyraldehyde",null,null,null,null,79.5,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"yes"]
["Scottish Environment Protection AgencyCadmium and compounds (as Cd)","Cadmium and compounds (as Cd)",5.0000000000000001E-3,0.03,8.9999999999999993E-3,null,null,"Air",false,0,null,null,null,null,false,"","Cadmium",1000,1,"","","","no"]
["Scottish Environment Protection AgencyCarbon dioxide","Carbon dioxide",null,null,null,1,null,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"yes"]
["Scottish Environment Protection AgencyCarbon disulphide","Carbon disulphide",64,100,null,null,null,"Air",false,0,null,null,null,null,false,"","Carbon Disulphide",1000,100,"","","","yes"]
["Scottish Environment Protection AgencyCarbon monoxide","Carbon monoxide",null,10000,null,null,2.7,"Air",false,0,null,null,null,null,false,"","Carbon Monoxide",1000000,1000,"","","","yes"]
["Scottish Environment Protection AgencyCarbon tetrachloride","Carbon tetrachloride",64,3200,null,1400,null,"Both",false,0,null,12,null,12,false,"","Carbon Tetrachloride",1000,1.0000000000000001E-5,"","","","no"]
["Scottish Environment Protection AgencyCFC-11","CFC-11",null,null,null,4000,null,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection AgencyCFC-113","CFC-113",null,null,null,5000,null,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection AgencyCFC-114","CFC-114",null,null,null,9300,null,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection AgencyCFC-115","CFC-115",null,null,null,9300,null,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection AgencyCFC-12","CFC-12",null,null,null,85000,null,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection AgencyCFC-13","CFC-13",null,null,null,11700,null,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,"","yes"]
["Scottish Environment Protection AgencyChlorine","Chlorine",null,290,null,null,null,"Air",false,0,null,null,null,null,false,"","Chlorine",1000,10,"","","","yes"]
["Scottish Environment Protection AgencyChlorobenzene","Chlorobenzene",47,1400,null,null,null,"",null,null,null,null,null,null,null,"","",null,null,"","","","no"]
["Scottish Environment Protection AgencyChloroform","Chloroform",100,null,null,4,1.7,"Air",false,0,null,null,null,null,false,"","Chloroform",1000,10,"","","","no"]
["Scottish Environment Protection AgencyMethyl chloride (chloromethane)","Methyl chloride (chloromethane)",18,null,null,null,0.5,"Air",false,0,null,null,null,null,false,"","Chloromethane",1000,500,"","","","no"]
["Scottish Environment Protection AgencyChromium (VI) compounds (as Cr)","Chromium (VI) compounds (as Cr)",2.5000000000000001E-4,null,null,null,null,"Air",false,0,null,null,null,null,false,"","Chromium",1000,10,"","",null,"yes"]
["Scottish Environment Protection AgencyChromium (III) compounds (as Cr)","Chromium (III) compounds (as Cr)",2,null,1.5,null,null,"Air",false,0,null,null,null,null,false,"","Chromium",1000,10,"","","","no"]
["Scottish Environment Protection Agencycis - but -2- ene","cis - but -2- ene",null,null,null,null,114.6,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection Agencycis - dichloroethylene","cis - dichloroethylene",null,null,null,null,44.7,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection Agencycis - hex -2- ene","cis - hex -2- ene",null,null,null,null,106.9,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection Agencycis - pent -2- ene","cis - pent -2- ene",null,null,null,null,112.1,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"yes"]
["Scottish Environment Protection AgencyCopper and compounds (as Cu)","Copper and compounds (as Cu)",0.05,null,0.25,null,null,"Air",false,0,null,null,null,null,false,"","Other Metals Specify",1000,100,"","","","no"]
["Scottish Environment Protection AgencyCyclohexane","Cyclohexane",null,null,null,null,29,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection AgencyCyclohexanol","Cyclohexanol",null,null,null,null,51.82,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection AgencyCyclohexanone","Cyclohexanone",null,null,null,null,29.9,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection AgencyDiacetone alcohol","Diacetone alcohol",null,null,null,null,26.2,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"yes"]
["Scottish Environment Protection AgencyDibutyl phthalate (DBP)","Dibutyl phthalate (DBP)",50,1000,null,null,null,"Air",false,0,null,null,null,null,false,"","",null,null,"","","","yes"]
["Scottish Environment Protection AgencyMethylene chloride (dichloromethane)","Methylene chloride (dichloromethane)",770,2100,null,9,6.8,"Both",false,0,null,20,null,20,false,"","",null,null,"","","","yes"]
["Scottish Environment Protection AgencyDiethyl ether","Diethyl ether",3100,62000,null,null,44.52,"Air",false,0,null,null,null,null,false,"","",null,null,"","","","no"]
["Scottish Environment Protection AgencyDiethylketone","Diethylketone",null,null,null,null,41.4,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"yes"]
["Scottish Environment Protection AgencyDi-i-propyl ether","Di-i-propyl ether",10600,131000,null,null,39.82,"Air",false,0,null,null,null,null,false,"","",null,null,"","","","yes"]
["Scottish Environment Protection AgencyDiisobutyl phthalate","Diisobutyl phthalate",50,1500,null,null,null,"Air",false,0,null,null,null,null,false,"","",null,null,"","","","no"]
["Scottish Environment Protection AgencyDimethoxymethane","Dimethoxymethane",null,null,null,null,16.420000000000002,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection AgencyDimethyl carbonate","Dimethyl carbonate",null,null,null,null,2.52,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection AgencyDimethyl ether","Dimethyl ether",null,null,null,null,18.920000000000002,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"yes"]
["Scottish Environment Protection AgencyDimethyl sulphate","Dimethyl sulphate",0.52,15.6,null,null,null,"Air",false,0,null,null,null,null,false,"","Di-methyl sulphate",1000,1,"","","","yes"]
["Scottish Environment Protection AgencyDimethylformamide","Dimethylformamide",300,6100,null,null,null,"Air",false,0,null,null,null,null,false,"","Dimethylformamide",1000,100,"","","","no"]
["Scottish Environment Protection AgencyEthane","Ethane",null,null,null,null,12.3,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection AgencyEthane-1,2-diol vapour","Ethane-1,2-diol vapour",null,null,null,null,37.32,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection AgencyEthanol","Ethanol",null,null,null,null,39.92,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection AgencyEthyl acetate","Ethyl acetate",null,null,null,null,20.92,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"yes"]
["Scottish Environment Protection AgencyEthyl acrylate","Ethyl acrylate",210,4200,null,null,null,"Air",false,0,null,null,null,null,false,"","Ethyl acrylate",1000,100,"","","","yes"]
["Scottish Environment Protection AgencyEthylbenzene","Ethylbenzene",4410,55200,null,null,73,"Air",false,0,null,null,null,null,false,"","Other VOCs Specify",1000,1000,"","","","no"]
["Scottish Environment Protection AgencyEthylene","Ethylene",null,null,null,null,100,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection AgencyEthylene oxide","Ethylene oxide",2E-3,null,null,null,null,"Air",false,0,null,null,null,null,false,"","Ethylene oxide",1000,10,"","","","no"]
["Scottish Environment Protection AgencyEthyl-t-butyl ether","Ethyl-t-butyl ether",null,null,null,null,24.22,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"yes"]
["Scottish Environment Protection AgencyFormaldehyde","Formaldehyde",5,100,null,null,51.9,"Both",false,0,50,5,null,null,false,"","",null,null,"","","","no"]
["Scottish Environment Protection AgencyFormic Acid","Formic Acid",null,null,null,null,3.2,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection AgencyH-1301","H-1301",null,null,null,5600,null,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection AgencyHCFC-123","HCFC-123",null,null,null,93,null,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection AgencyHCFC-124","HCFC-124",null,null,null,480,null,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection AgencyHCFC-141b","HCFC-141b",null,null,null,630,null,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection AgencyHCFC-142b","HCFC-142b",null,null,null,2000,null,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection AgencyHCFC-225ca","HCFC-225ca",null,null,null,170,null,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,{"$f":"IF(D238+E238>0,\"yes\",\"no\")","v":"no"}]
["Scottish Environment Protection AgencyHCFC-225cb","HCFC-225cb",null,null,null,530,null,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection AgencyHCFFC-22","HCFFC-22",null,null,null,1700,null,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection AgencyHex -1- ene","Hex -1- ene",null,null,null,null,87.4,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection AgencyHexan -3- one","Hexan -3- one",null,null,null,null,59.9,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection AgencyHexan-2-one","Hexan-2-one",null,null,null,null,57.2,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection AgencyHFC-125","HFC-125",null,null,null,3400,null,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection AgencyHFC-134","HFC-134",null,null,null,1100,null,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
[{"$f":"\"Scottish Environment Protection Agency\"&B245","v":"Scottish Environment Protection AgencyHFC-134a"},"HFC-134a",null,null,null,1300,null,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection AgencyHFC-143","HFC-143",null,null,null,330,null,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection AgencyHFC-143a","HFC-143a",null,null,null,4300,null,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection AgencyHFC-152a","HFC-152a",null,null,null,120,null,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection AgencyHFC-227ea","HFC-227ea",null,null,null,3500,null,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection AgencyHFC-23","HFC-23",null,null,null,12000,null,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection AgencyHFC-236fa","HFC-236fa",null,null,null,6300,null,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection AgencyHFC-245ca","HFC-245ca",null,null,null,640,null,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection AgencyHFC-32","HFC-32",null,null,null,550,null,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection AgencyHFC-41","HFC-41",null,null,null,97,null,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection AgencyHFC-43-10mee","HFC-43-10mee",null,null,null,1500,null,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"yes"]
["Scottish Environment Protection AgencyHydrazine","Hydrazine",0.06,2.6,null,null,null,"Air",false,0,null,null,null,null,false,"","",null,null,"","","","yes"]
["Scottish Environment Protection AgencyHydrogen bromide","Hydrogen bromide",null,700,null,null,null,"Air",false,0,null,null,null,null,false,"","Hydrogen Bromide",1000,10,"","","","yes"]
["Scottish Environment Protection AgencyHydrogen chloride","Hydrogen chloride",null,750,null,null,null,"Air",false,0,null,null,null,null,false,"","Hydrogen Chloride",1000,1000,"","","","no"]
["Scottish Environment Protection AgencyHydrogen cyanide","Hydrogen cyanide",2,null,null,null,null,"Air",false,0,null,null,null,null,false,"","",null,null,"","","Daily Average","yes"]
["Scottish Environment Protection AgencyHydrogen fluoride (ecological)","Hydrogen fluoride (ecological)",0.5,5,null,null,null,"Air",false,0,null,null,null,null,false,"","Hydrogen Fluoride",1000,10,"","","Weekly Average",{"$f":"IF(#REF!+#REF!>0,\"yes\",\"no\")","v":{"$error":"#REF!"}}]
["Scottish Environment Protection AgencyHydrogen fluoride","Hydrogen fluoride",16,160,2.1,null,null,"Air",false,0,null,null,null,null,false,"","Hydrogen Fluoride",1000,10,"","","Monthly Average","yes"]
["Scottish Environment Protection AgencyHydrogen iodide","Hydrogen iodide",5,520,null,null,null,"Air",false,0,null,null,null,null,false,"","Hydrogen Iodide",1000,10,"","","","yes"]
["Scottish Environment Protection AgencyHydrogen sulphide","Hydrogen sulphide",70,150,null,null,null,"Both",false,0,1,0.25,10,null,false,"","",null,null,"","","","no"]
["Scottish Environment Protection Agencyi-butane","i-butane",null,null,null,null,30.7,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection Agencyi-butyraldehyde","i-butyraldehyde",null,null,null,null,51.4,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection Agencyi-pentane","i-pentane",null,null,null,null,40.5,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection Agencyi-propyl acetate","i-propyl acetate",null,null,null,null,21.12,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection Agencyi-propylbenzene","i-propylbenzene",null,null,null,null,50,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection AgencyIsoprene","Isoprene",null,null,null,null,109.2,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"yes"]
["Scottish Environment Protection AgencyLead","Lead",0.25,null,1.1000000000000001,null,null,"Air",false,0,null,null,null,null,false,"","Lead",1000,1,"","","","yes"]
["Scottish Environment Protection AgencyManganese and compounds (as Mn)","Manganese and compounds (as Mn)",0.15,1500,null,null,null,"Air",false,0,null,123,null,null,false,"","Other Metals Specify",1000,100,"","","","yes"]
["Scottish Environment Protection AgencyMercury and its inorganic compounds (as Hg)","Mercury and its inorganic compounds (as Hg)",0.06,0.6,4.0000000000000001E-3,null,null,"Air",false,0,null,null,null,null,false,"","Mercury",1000,1,"","","","no"]
["Scottish Environment Protection AgencyMethane","Methane",null,null,null,21,0.6,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"yes"]
["Scottish Environment Protection AgencyMethanol","Methanol",2660,33300,null,null,14.02,"Air",false,0,null,null,null,null,false,"","",null,null,"","",null,"no"]
["Scottish Environment Protection AgencyMethyl - i - propylketone","Methyl - i - propylketone",null,null,null,null,36.4,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection AgencyMethyl acetate","Methyl acetate",null,null,null,null,5.92,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection AgencyMethyl formate","Methyl formate",null,null,null,null,2.72,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection AgencyMethyl -t- butylketone","Methyl -t- butylketone",null,null,null,null,32.299999999999997,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,{"$f":"IF(#REF!+#REF!>0,\"yes\",\"no\")","v":{"$error":"#REF!"}}]
["Scottish Environment Protection AgencyMethylethylketone","Methylethylketone",null,null,null,null,37.299999999999997,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection AgencyMethyl-i-butylketone","Methyl-i-butylketone",null,null,null,null,49,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection AgencyMethylpropene","Methylpropene",null,null,null,null,62.7,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection AgencyMethylpropylketone","Methylpropylketone",null,null,null,null,54.8,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection AgencyMethyl-t-butyl-ether","Methyl-t-butyl-ether",null,null,null,null,17.52,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection Agencym-ethyltoluene","m-ethyltoluene",null,null,null,null,101.9,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"yes"]
["Scottish Environment Protection AgencyMolydenum","Molydenum",null,null,1.6E-2,null,null,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,"","yes"]
["Scottish Environment Protection AgencyMono-ethanolamine (MEA)","Mono-ethanolamine (MEA)",100,400,null,null,null,"",null,null,null,null,null,null,null,"","",null,null,"","","",{"$f":"IF(#REF!+#REF!>0,\"yes\",\"no\")","v":{"$error":"#REF!"}}]
["Scottish Environment Protection Agencym-xylene","m-xylene",null,null,null,null,110.8,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection AgencyNaphthalene","Naphthalene",3,null,null,null,null,"Both",false,0,130,2,130,2,false,"","Napthalene",1000,1.0000000000000001E-5,"","","","no"]
["Scottish Environment Protection Agencyn-butane","n-butane",null,null,null,null,35.200000000000003,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection Agencyn-butyl acetate","n-butyl acetate",null,null,null,null,26.92,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection Agencyn-decane","n-decane",null,null,null,null,38.4,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection Agencyn-dodecane","n-dodecane",null,null,null,null,35.700000000000003,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection AgencyNeopentane","Neopentane",null,null,null,null,17.3,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection Agencyn-heptane","n-heptane",null,null,null,null,49.4,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"yes"]
["Scottish Environment Protection Agencyn-Hexane","n-Hexane",720,21600,null,null,48.2,"Air",false,0,null,null,null,null,false,"","Other VOCs Specify",1000,1000,"","","","yes"]
["Scottish Environment Protection AgencyNickel and compounds (as Ni) except nickel carbonyl","Nickel and compounds (as Ni) except nickel carbonyl",0.02,0.7,0.11,null,null,"Air",false,0,null,null,null,null,false,"","Nickel",1000,10,"","","","yes"]
["Scottish Environment Protection AgencyNitric acid","Nitric acid",52,260,null,null,null,"Air",false,0,null,null,null,null,false,"","",null,null,"","","","yes"]
["Scottish Environment Protection AgencyNitrogen dioxide","Nitrogen dioxide",40,200,null,null,2.8,"Air",false,0,null,null,null,null,false,"","Oxides of Nitrogen",1000000,10,"","","Daily Mean",{"$f":"IF(D299+E299>0,\"yes\",\"no\")","v":"yes"}]
["Scottish Environment Protection AgencyNitrogen oxides (as NO2) (ecological)","Nitrogen oxides (as NO2) (ecological)",30,75,null,null,2.8,"Air",false,0,null,null,null,null,false,"","Oxides of Nitrogen",1000000,10,"","","","yes"]
["Scottish Environment Protection AgencyNitrogen monoxide (nitric oxide)","Nitrogen monoxide (nitric oxide)",25,4400,null,null,-42.7,"Air",false,0,null,null,null,null,false,"","Oxides of Nitrogen",1000000,10,"","","","no"]
["Scottish Environment Protection AgencyNitrous oxide","Nitrous oxide",null,null,null,310,null,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection AgencyN-nitrosodimethylamine (NDMA)","N-nitrosodimethylamine (NDMA)",2.0000000000000001E-4,null,null,null,null,"",null,null,null,null,null,null,null,"","",null,null,"","","","no"]
["Scottish Environment Protection Agencyn-nonane","n-nonane",null,null,null,null,41.4,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection Agencyn-octane","n-octane",null,null,null,null,45.3,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection Agencyn-pentane","n-pentane",null,null,null,null,39.5,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
[{"$f":"\"Scottish Environment Protection Agency\"&B306","v":"Scottish Environment Protection Agencyn-Propyl acetate"},"n-Propyl acetate",null,null,null,null,28.22,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection Agencyn-propylbenzene","n-propylbenzene",null,null,null,null,63.6,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection Agencyn-undecane","n-undecane",null,null,null,null,38.4,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection Agencyo-ethyltoluene","o-ethyltoluene",null,null,null,null,89.8,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"yes"]
["Scottish Environment Protection AgencyOrthophosphoric acid","Orthophosphoric acid",10,200,null,null,null,"Air",false,0,null,null,null,null,false,"","",null,null,"","","","no"]
["Scottish Environment Protection Agencyo-xylene","o-xylene",null,null,null,null,105.3,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,"24 hr Mean",{"$f":"IF(#REF!+#REF!>0,\"yes\",\"no\")","v":{"$error":"#REF!"}}]
["Scottish Environment Protection AgencyOzone","Ozone",null,100,null,null,null,"Air",false,0,null,null,null,null,false,"","",null,null,"","","24 hr Mean","yes"]
["Scottish Environment Protection AgencyParticulates (PM10)","Particulates (PM10)",18,50,null,null,null,"Air",false,0,null,null,null,null,false,"","Particulates",1000,100,"","","",{"$f":"IF(#REF!+#REF!>0,\"yes\",\"no\")","v":{"$error":"#REF!"}}]
["Scottish Environment Protection AgencyParticulates (PM2.5)","Particulates (PM2.5)",10,null,null,null,null,"Air",false,0,null,null,null,null,false,"","Particulates",1000,100,"","",null,"no"]
["Scottish Environment Protection AgencyPent - 1 - ene","Pent - 1 - ene",null,null,null,null,97.7,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"yes"]
["Scottish Environment Protection AgencyPentan-2-one (Methylpropylketone)","Pentan-2-one (Methylpropylketone)",7160,89500,null,null,null,"Air",false,0,null,null,null,null,false,"","",null,null,"","","","yes"]
["Scottish Environment Protection AgencyPentan-3-one (Diethylketone)","Pentan-3-one (Diethylketone)",7160,89500,null,null,null,"Air",false,0,null,null,null,null,false,"","",null,null,"","","","no"]
["Scottish Environment Protection AgencyPentanaldehyde","Pentanaldehyde",null,null,null,null,76.5,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection AgencyPerfluorocyclobutane","Perfluorocyclobutane",null,null,null,10000,null,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection AgencyPerfluoroethane","Perfluoroethane",null,null,null,11900,null,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection AgencyPerfluorohexane","Perfluorohexane",null,null,null,9000,null,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection AgencyPerfluoromethane","Perfluoromethane",null,null,null,5700,null,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection AgencyPerfluoropentane","Perfluoropentane",null,null,null,8900,null,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection Agencyp-ethyltoluene","p-ethyltoluene",null,null,null,null,90.6,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,"","yes"]
["Scottish Environment Protection AgencyPhenol","Phenol",78,1600,null,null,null,"Air",false,0,null,null,null,null,false,"","Phenol",1000,100,"","","","yes"]
["Scottish Environment Protection AgencyPhosgene","Phosgene",0.8,25,null,null,null,"Air",false,0,null,null,null,null,false,"","Phosgene",1000,1,"","","","yes"]
["Scottish Environment Protection AgencyPhosphine","Phosphine",1.4000000000000001,28.000000000000004,null,null,null,"Air",false,0,null,null,null,null,false,"","",null,null,"","","","yes"]
["Scottish Environment Protection AgencyPolychlorinated biphenyls","Polychlorinated biphenyls",0.2,6,null,null,null,"Air",false,0,null,null,null,null,false,"","PCBs",1E-3,0.1,"","","","no"]
["Scottish Environment Protection AgencyPolycyclic aromatic hydrocarbons (PAH)-total content within PM10 fraction","Polycyclic aromatic hydrocarbons (PAH)-total content within PM10 fraction",null,null,null,null,null,"Air",false,0,null,null,null,null,false,"","PAHs as benzo(a)pyrene",1000,1,"","",null,"yes"]
["Scottish Environment Protection AgencyPropan-1-ol","Propan-1-ol",5000,62500,null,null,56.12,"Air",false,0,null,null,null,null,false,"","",null,null,"","","","yes"]
["Scottish Environment Protection AgencyPropan-2-ol","Propan-2-ol",9990,125000,null,null,18.82,"Air",false,0,null,null,null,null,false,"","",null,null,"","","","no"]
["Scottish Environment Protection AgencyPropane","Propane",null,null,null,null,17.600000000000001,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection AgencyPropane-1,2-diol vapour & particulates","Propane-1,2-diol vapour & particulates",null,null,null,null,45.72,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection AgencyPropionaldehyde","Propionaldehyde",null,null,null,null,79.8,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"yes"]
["Scottish Environment Protection AgencyPropionic acid","Propionic acid",310,4600,null,null,15,"Air",false,0,null,null,null,null,false,"","",null,null,"","","","no"]
["Scottish Environment Protection AgencyPropylene","Propylene",null,null,null,null,112.3,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"yes"]
["Scottish Environment Protection AgencyPropylene oxide","Propylene oxide",24,720,null,null,null,"Air",false,0,null,null,null,null,false,"","Propylene oxide",1000,100,"","","","no"]
["Scottish Environment Protection Agencyp-xylene","p-xylene",null,null,null,null,101,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection Agencys-butyl acetate","s-butyl acetate",null,null,null,null,27.52,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,"","yes"]
["Scottish Environment Protection AgencySelenium and compounds (as Se), except hydrogen selenide","Selenium and compounds (as Se), except hydrogen selenide",2,null,1.2E-2,null,null,"Air",false,0,null,null,null,null,false,"","Selenium",1000,10,"","","","yes"]
["Scottish Environment Protection AgencySodium hydroxide","Sodium hydroxide",null,200,null,null,null,"Air",false,0,null,null,null,null,false,"","",null,null,"","","","yes"]
["Scottish Environment Protection AgencyStyrene","Styrene",260,800,null,null,14.2,"Both",false,0,500,50,500,50,false,"","Styrene",1000,500,"","","",{"$f":"IF(#REF!+#REF!>0,\"yes\",\"no\")","v":{"$error":"#REF!"}}]
["Scottish Environment Protection AgencySulphur dioxide  (15 min mean)","Sulphur dioxide  (15 min mean)",0,266,null,null,4.8,"Air",false,0,null,null,null,null,false,"","Oxides of Sulphur",1000000,10,"","","1 Hr Mean",{"$f":"IF(#REF!+#REF!>0,\"yes\",\"no\")","v":{"$error":"#REF!"}}]
["Scottish Environment Protection AgencySulphur dioxide (24 hr mean)","Sulphur dioxide (24 hr mean)",null,125,null,null,4.8,"Air",false,0,null,null,null,null,false,"","Oxides of Sulphur",1000000,10,"","","","no"]
["Scottish Environment Protection AgencySulphur dioxide (ecological-lichens and bryophytes)","Sulphur dioxide (ecological-lichens and bryophytes)",10,null,null,null,4.8,"Air",false,0,null,null,null,null,false,"","Oxides of Sulphur",1000000,10,"","","",{"$f":"IF(#REF!+#REF!>0,\"yes\",\"no\")","v":{"$error":"#REF!"}}]
[{"$f":"\"Scottish Environment Protection Agency\"&B346","v":"Scottish Environment Protection AgencySulphur dioxide (ecological-other vegetation)"},"Sulphur dioxide (ecological-other vegetation)",20,null,null,null,4.8,"Air",false,0,null,null,null,null,false,"","Oxides of Sulphur",1000000,10,"","","",{"$f":"IF(#REF!+#REF!>0,\"yes\",\"no\")","v":{"$error":"#REF!"}}]
["Scottish Environment Protection AgencySulphur dioxide (ecological-crops)","Sulphur dioxide (ecological-crops)",30,null,null,null,4.8,"Air",false,0,null,null,null,null,false,"","Oxides of Sulphur",1000000,10,"","","",{"$f":"IF(#REF!+#REF!>0,\"yes\",\"no\")","v":{"$error":"#REF!"}}]
["Scottish Environment Protection AgencySulphur hexafluoride","Sulphur hexafluoride",60700,759000,null,23900,null,"Air",false,0,null,null,null,null,false,"","",null,null,"","","","yes"]
["Scottish Environment Protection AgencySulphuric acid","Sulphuric acid",10,300,null,null,null,"Air",false,0,null,null,null,null,false,"","",null,null,"","","","no"]
["Scottish Environment Protection Agencyt-butyl acetate","t-butyl acetate",null,null,null,null,5.32,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection AgencyTetrachloroethylene","Tetrachloroethylene",40,null,null,null,2.9,"Both",false,0,null,10,null,10,false,"","Tetrachloroethylene",1000,500,"","","","yes"]
["Scottish Environment Protection AgencyTetrahydrofuran","Tetrahydrofuran",1500,30000,null,null,null,"Air",false,0,null,null,null,null,false,"","Dioxins and Furans",1E-3,0.1,"","","","yes"]
["Scottish Environment Protection AgencyToluene","Toluene",260,8000,null,null,63.7,"Air",false,0,null,null,null,null,false,"","",null,null,"","","",{"$f":"IF(#REF!+#REF!>0,\"yes\",\"no\")","v":{"$error":"#REF!"}}]
["Scottish Environment Protection Agencytrans - but - 2 - ene","trans - but - 2 - ene",null,null,null,null,113.2,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection Agencytrans - hex -2- ene","trans - hex -2- ene",null,null,null,null,107.3,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection Agencytrans - pent - 2 - ene","trans - pent - 2 - ene",null,null,null,null,111.7,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
["Scottish Environment Protection Agencytrans -dichloroethylene","trans -dichloroethylene",null,null,null,null,39.200000000000003,"Air",false,null,null,null,null,null,null,null,null,null,null,null,null,"","no"]
["Scottish Environment Protection AgencyTrichloroethylene","Trichloroethylene",2,null,null,null,32.5,"Both",false,0,null,10,null,10,false,"","Trichloroethylene",1000,500,"","",null,{"$f":"IF(D359+E359>0,\"yes\",\"no\")","v":"yes"}]
["Scottish Environment Protection AgencyTrimethylbenzenes, all isomers or mixtures","Trimethylbenzenes, all isomers or mixtures",1250,37500,null,null,null,"Air",false,0,null,null,null,null,false,"","Trimethylbenzene",1000,500,"","","","yes"]
["Scottish Environment Protection AgencyVanadium and compounds (as V)","Vanadium and compounds (as V)",null,1,null,null,null,"Air",false,0,null,null,null,null,false,"","Other Metals Specify",1000,100,"","","","yes"]
["Scottish Environment Protection AgencyVinyl acetate","Vinyl acetate",176.00000000000003,3520.0000000000005,null,null,null,"Air",false,0,null,null,null,null,false,"","",null,null,"","","","yes"]
["Scottish Environment Protection AgencyVinyl chloride","Vinyl chloride",10,1300,null,null,27.21,"Air",false,0,null,null,null,null,false,"","",null,null,"","","","yes"]
["Scottish Environment Protection AgencyXylene, o-, m-, p- or mixed isomers","Xylene, o-, m-, p- or mixed isomers",2200,44100,null,null,null,"Air",false,0,null,null,null,null,false,"","Xylene",1000,500,"","","","yes"]
["Scottish Environment Protection AgencyZinc oxide","Zinc oxide",50,1000,0.48,null,null,"Air",false,0,null,null,null,null,false,"","",null,null,"","","SUBOtherPeriod",{"$error":"#VALUE!"}]
[null,"Substance","H1 LongTermAirEAL  µg/m3","H1 ShortTermAirEAL  µg/m3","SUBAirToLandDepositionRate","SUBGlobalWarmingFactor","SUBOzoneCreationFactor","SUBReleaseType","SUBUserAdded","SUBOtherPeriodValue","SUBFreshWaterMAC","SUBFreshWaterAnnual","SUBSaltWaterMAC","SubSaltWaterAnnual","SUBPriorityWaterEQS","SUBSigAnnualLoad","SUBOPRAName","SUBOPRAConvFromGram","SUBOPRAThreshold_Air","Field19","Field20","SUBOtherPeriod"]

{"sheet":"SubstancesW","index":32,"n_rows":228,"n_cols":22,"rows_kept":228,"cut":false,"hidden":false,"merged":[]}
[]
[]
[]
[{"$f":"S4+1","v":19},1,{"$f":"B4+1","v":2},{"$f":"C4+1","v":3},4,5,6,7,8,9,10,11,12,13,14,15,16,17,18,null,{"$f":"A4+1","v":20}]
["Country","SUBSubstance","SUBLongTermAirEAL","SUBShortTermAirEAL","SUBAirToLandDepositionRate","SUBGlobalWarmingFactor","SUBOzoneCreationFactor","SUBReleaseType","SUBUserAdded","SUBOtherPeriodValue","SUBFreshWaterMAC","SUBFreshWaterAnnual","SUBSaltWaterMAC","SubSaltWaterAnnual","SUBPriorityWaterEQS","SUBSigAnnualLoad","SUBOPRAName","SUBOPRAConvFromGram","SUBOPRAThreshold_Air"]
[{"$f":"\"Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection Agency\"&B6","v":"Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection Agency1,1,1-trichloroethane"},"1,1,1-trichloroethane",null,null,null,null,null,null,null,null,null,100,null,100,false,null,null,null,null,null,null,{"$f":"IF(C6+D6>0,\"yes\",\"no\")","v":"no"}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection Agency1,1,2-Trichloroethane","1,1,2-Trichloroethane",null,null,null,null,null,"Water",false,0,null,400,null,300,false,null,null,null,null,null,null,{"$f":"IF(C7+D7>0,\"yes\",\"no\")","v":"no"}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection Agency1,2 Dichloroethane","1,2 Dichloroethane",42,700,null,null,null,"Both",false,0,null,10,null,10,false,null,null,null,"1,2-Dichloroethane",1000,100,"yes"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection Agency2,4-Dichlorophenol","2,4-Dichlorophenol",null,null,null,null,null,"Water",false,0,140,4.2,6,0.42,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection Agency2,4-Dichlorophenoxyacetic acid (2,4-D) (95%ile)","2,4-Dichlorophenoxyacetic acid (2,4-D) (95%ile)",null,null,null,null,null,"Water",false,0,1.3,0.3,1.3,0.3,false,null,null,null,"2,4 D ester",1000,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection Agency2-Chlorophenol","2-Chlorophenol",null,null,null,null,null,"Water",false,0,null,50,null,50,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection Agency3,4 - dichloroaniline","3,4 - dichloroaniline",null,null,null,null,null,"Water",false,null,5.4,0.2,5.4,0.2,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection Agency3-Chlorophenol + 4-chlorophenol (total or individual monochlorophenols)","3-Chlorophenol + 4-chlorophenol (total or individual monochlorophenols)",null,null,null,null,null,"Water",false,0,250,50,250,50,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection Agency4-chloro-3-methyl-phenol","4-chloro-3-methyl-phenol",null,null,null,null,null,"Water",false,0,null,40,null,40,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyAbamectin","Abamectin",null,null,null,null,null,"Water",false,0,0.03,0.01,0.01,3.0000000000000001E-3,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyAclonifen","Aclonifen",null,null,null,null,null,"Water",false,null,0.12,0.12,1.2E-2,1.2E-2,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyAlachlor","Alachlor",null,null,null,null,null,"Water",false,0,0.7,0.3,0.7,0.3,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyAmmonia (≤ 50mg/l CaCO3 (90 %ile))","Ammonia (≤ 50mg/l CaCO3 (90 %ile))",null,null,null,null,null,"Water",false,0,null,300,null,null,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyAmmonia (un-ionised)","Ammonia (un-ionised)",null,null,null,null,null,"Water",false,0,null,null,null,21,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyAmmonia CaCO3 >50mg/l (90 %ile)","Ammonia CaCO3 >50mg/l (90 %ile)",null,null,null,null,null,"Water",false,0,null,200,null,null,false,3,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyAmmonia CaCO3 ≤50mg/l (90 %ile)","Ammonia CaCO3 ≤50mg/l (90 %ile)",null,null,null,null,null,"Water",false,0,null,300,null,null,false,3,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyAnthracene","Anthracene",null,null,null,null,null,"Water",false,0,0.1,0.1,0.1,0.1,true,1,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyArsenic","Arsenic",null,null,null,null,null,"Water",false,0,null,50,null,25,false,null,null,null,"Arsenic",1000,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyAtrazine","Atrazine",null,null,null,null,null,"Water",false,0,2,0.6,2,0.6,false,null,null,null,"Atrazin",1000,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyAzinphos methyl (dissolved)","Azinphos methyl (dissolved)",null,null,null,null,null,"Water",false,0,null,0.01,null,0.01,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyBentazone","Bentazone",null,null,null,null,null,"Water",false,0,null,500,null,500,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyBenzene","Benzene",5,195,null,null,21.8,"Both",false,0,50,10,50,8,false,null,null,null,"Benzene",1000,10,"yes"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyBenzo (b) fluoranthene","Benzo (b) fluoranthene",null,null,null,null,null,"Water",false,null,1.7000000000000001E-2,null,1.7000000000000001E-2,null,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyBenzo (a) pyrene","Benzo (a) pyrene",null,null,null,null,null,"Water",false,null,0.27,null,2.7E-2,null,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyBenzo (g,h,i) perylene","Benzo (g,h,i) perylene",null,null,null,null,null,"Water",false,null,8.2000000000000007E-3,null,8.1999999999999998E-4,null,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyBenzo (k) fluoranthene","Benzo (k) fluoranthene",null,null,null,null,null,"Water",false,null,1.7000000000000001E-2,null,1.7000000000000001E-2,null,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyBenzyl Butyl phthalate","Benzyl Butyl phthalate",null,null,null,null,null,"Water",false,null,51,7.5,10,0.75,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyBifenox (Methyl 5-(2,4-dichlorophenoxy)-2-nitrobenzoate)","Bifenox (Methyl 5-(2,4-dichlorophenoxy)-2-nitrobenzoate)",null,null,null,null,null,"Water",false,null,0.04,1.2E-2,4.0000000000000001E-3,1.1999999999999999E-3,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyBiphenyl","Biphenyl",null,null,null,null,null,"Water",false,0,null,25,null,25,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyBoron","Boron",null,null,null,null,null,"Water",false,0,null,2000,null,7000,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyBrominated diphenylether - total PDPE (Polybrominated diphenylether, or congener) numbers 28, 47, 99, 100, 153 and 154","Brominated diphenylether - total PDPE (Polybrominated diphenylether, or congener) numbers 28, 47, 99, 100, 153 and 154",null,null,null,null,null,"Water",false,0,0.14000000000000001,null,1.4E-2,null,true,1,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyBromine","Bromine",null,70,null,null,null,"Both",false,0,5,2,10,null,false,null,null,null,null,null,null,"yes"]
[{"$f":"\"Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection Agency\"&B38","v":"Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyBromoxynil"},"Bromoxynil",null,null,null,null,null,"Water",false,0,1000,100,1000,100,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyButylbenzyl phthalate","Butylbenzyl phthalate",null,null,null,null,null,"Water",false,0,100,20,100,20,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyCadmium and its compounds (dissolved, water hardness < 40 mg/l Ca CO3)","Cadmium and its compounds (dissolved, water hardness < 40 mg/l Ca CO3)",null,null,null,null,null,"Water",false,0,0.45,0.08,null,0.2,true,5,null,null,"Cadmium",1000,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyCadmium and its compounds (dissolved, water hardness ≥ 200 mg/l CaCO3)","Cadmium and its compounds (dissolved, water hardness ≥ 200 mg/l CaCO3)",null,null,null,null,null,"Water",false,0,1.5,0.25,null,0.2,true,5,null,null,"Cadmium",1000,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyCadmium and its compounds (dissolved, water hardness 100 - <200 mg/l CaCO3)","Cadmium and its compounds (dissolved, water hardness 100 - <200 mg/l CaCO3)",null,null,null,null,null,"Water",false,0,0.9,0.15,null,0.2,true,5,null,null,"Cadmium",1000,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyCadmium and its compounds (dissolved, water hardness 40 - < 50 mg/l CaCO3)","Cadmium and its compounds (dissolved, water hardness 40 - < 50 mg/l CaCO3)",null,null,null,null,null,"Water",false,0,0.46,0.09,null,0.2,true,5,null,null,"Cadmium",1000,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyCadmium and its compounds (dissolved, water hardness 50 - <100 mg/l CaCO3)","Cadmium and its compounds (dissolved, water hardness 50 - <100 mg/l CaCO3)",null,null,null,null,null,"Water",false,0,0.6,0.09,null,0.2,true,5,null,null,"Cadmium",1000,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyCarbendazim","Carbendazim",null,null,null,null,null,"Water",false,0,0.7,0.15,0,0,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyCarbon tetrachloride","Carbon tetrachloride",130,3900,null,1400,null,"Both",false,0,null,12,null,12,false,null,null,null,"Carbon Tetrachloride",1000,1.0000000000000001E-5,"yes"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyChlorfenvinphos","Chlorfenvinphos",null,null,null,null,null,"Water",false,0,0.3,0.1,0.3,0.1,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyChloride","Chloride",null,null,null,null,null,"Water",false,0,null,250000,null,null,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyChlorine (95%ile concentration of total residual oxidant)","Chlorine (95%ile concentration of total residual oxidant)",null,null,null,null,null,"Water",false,0,5,2,10,null,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyC10-13 Chloroalkanes","C10-13 Chloroalkanes",null,null,null,null,null,"Water",false,0,1.4,0.4,1.4,0.4,true,1,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyChloronitrotoluenes","Chloronitrotoluenes",null,null,null,null,null,"Water",false,0,null,10,null,10,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyChlorothalonil","Chlorothalonil",null,null,null,null,null,"Water",false,0,1.2,3.5000000000000003E-2,null,null,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyChlorotoluron","Chlorotoluron",null,null,null,null,null,"Water",false,0,20,2,null,2,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyChlorpropham","Chlorpropham",null,null,null,null,null,"Water",false,0,40,10,40,10,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyChlorpyrifos (chlorpyrifos ethyl)","Chlorpyrifos (chlorpyrifos ethyl)",null,null,null,null,null,"Water",false,0,0.1,0.03,0.1,0.03,false,null,null,null,"Chlorfenvinphos",1000,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyChromium III (95%ile) (dissolved)","Chromium III (95%ile) (dissolved)",null,null,null,null,null,"Water",false,0,32,4.7,null,null,false,null,null,null,"Chromium",1000,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyChromium VI (95%ile) (dissolved)","Chromium VI (95%ile) (dissolved)",null,null,null,null,null,"Water",false,0,null,3.4,32,0.6,false,null,null,null,"Chromium",1000,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyCobalt","Cobalt",null,null,null,null,null,"Water",false,0,100,3,100,3,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyCobalt (dissolved)","Cobalt (dissolved)",null,null,null,null,null,"Water",false,0,100,3,100,3,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyCopper (dissolved, bioavailable)","Copper (dissolved, bioavailable)",null,null,null,null,null,"Water",false,null,null,1,null,3.6,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyCopper - dissolved (Dissolved Organic Carbon (DOC) less than or equal to 1mg/l) ","Copper - dissolved (Dissolved Organic Carbon (DOC) less than or equal to 1mg/l) ",null,null,null,null,null,null,null,null,null,null,null,3.76,null,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyCopper - dissolved (Dissolved Organic Carbon (DOC) greater than 1mg/l) ","Copper - dissolved (Dissolved Organic Carbon (DOC) greater than 1mg/l) ",null,null,null,null,null,null,null,null,null,null,null," 3.76 + (2.677 x ((DOC/2) –0.5)) μg/l ",null,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyCoumaphos","Coumaphos",null,null,null,null,null,"Water",false,0,0.1,0.01,0.1,0.03,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyCyanide ","Cyanide ",null,null,null,null,null,"Water",false,0,5,1,5,1,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyCybutryne","Cybutryne",null,null,null,null,null,"Water",false,null,1.6E-2,2.5000000000000001E-3,1.6E-2,2.5000000000000001E-3,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyCyclodiene pesticides: Aldrin, Dieldrin, Endrin, Isodrin (Total)","Cyclodiene pesticides: Aldrin, Dieldrin, Endrin, Isodrin (Total)",null,null,null,null,null,"Water",false,0,null,0.01,null,5.0000000000000001E-3,false,null,null,null,"Aldrin",1000,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyCyfluthrin","Cyfluthrin",null,null,null,null,null,"Water",false,0,1E-3,null,1E-3,null,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyCypermethrin (95%ile)","Cypermethrin (95%ile)",null,null,null,null,null,"Water",false,0,5.9999999999999995E-4,8.0000000000000007E-5,6.0000000000000002E-5,7.9999999999999996E-6,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyDDT total","DDT total",null,null,null,null,null,"Water",false,0,null,2.5000000000000001E-2,null,2.5000000000000001E-2,false,null,null,null,"DDT all isomers",1000,null,"no"]
[{"$f":"\"Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection Agency\"&B70","v":"Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyDemetons"},"Demetons",null,null,null,null,null,"Water",false,0,null,0.5,null,0.5,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyDi(2-ethylhexyl)-phthalate (DEHP)","Di(2-ethylhexyl)-phthalate (DEHP)",null,null,null,null,null,"Water",false,0,null,1.3,null,1.3,false,null,null,null,null,null,null,{"$f":"IF(C71+D71>0,\"yes\",\"no\")","v":"no"}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyDiazinon (95%ile)","Diazinon (95%ile)",null,null,null,null,null,"Water",false,0,0.02,0.01,0.26,0.01,false,null,null,null,"Diazinon",1000,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyDibutyl phthalate","Dibutyl phthalate",null,null,null,null,null,"Water",false,0,40,8,40,8,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyDichlorobenzene (total dichlorobenzene isomers)","Dichlorobenzene (total dichlorobenzene isomers)",null,null,null,null,null,"Water",false,0,200,20,200,20,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyDichloromethane (DCM, Methylene Chloride)","Dichloromethane (DCM, Methylene Chloride)",700,3000,null,9,6.8,"Both",false,0,null,20,null,20,false,null,null,null,null,null,null,"yes"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyDichlorvos (insecticide)","Dichlorvos (insecticide)",null,null,null,null,null,"Water",false,0,6.9999999999999999E-4,5.9999999999999995E-4,6.9999999999999994E-5,6.0000000000000002E-5,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyDicofol (insecticide)","Dicofol (insecticide)",null,null,null,null,null,"Water",false,null,null,1.2999999999999999E-3,null,3.1999999999999999E-5,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyDiethyl phthalate","Diethyl phthalate",null,null,null,null,null,"Water",false,0,1000,200,4000,800,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyDiflubenzuron","Diflubenzuron",null,null,null,null,null,"Water",false,0,1.4999999999999999E-2,1E-3,0.1,5.0000000000000001E-3,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyDimethoate (95%ile)","Dimethoate (95%ile)",null,null,null,null,null,"Water",false,0,4,0.48,4,0.48,false,null,null,null,"Dimethoate",1000,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyDimethyl phthalate","Dimethyl phthalate",null,null,null,null,null,"Water",false,0,4000,800,4000,800,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyDioctyl phthalate","Dioctyl phthalate",null,null,null,null,null,"Water",false,0,40,20,40,20,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyDiuron (herbicide)","Diuron (herbicide)",null,null,null,null,null,"Water",false,0,1.8,0.2,1.8,0.2,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyDoramectin","Doramectin",null,null,null,null,null,"Water",false,0,0.01,1E-3,0.1,1E-3,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyEDTA","EDTA",null,null,null,null,null,"Water",false,0,4000,400,4000,400,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyEndosulfan","Endosulfan",null,null,null,null,null,"Water",false,0,0.01,5.0000000000000001E-3,4.0000000000000001E-3,5.0000000000000001E-4,true,1,null,null,"Endosulfan",1000,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyFenchlorphos","Fenchlorphos",null,null,null,null,null,"Water",false,0,0.1,0.01,0.1,0.03,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyFenitrothion","Fenitrothion",null,null,null,null,null,"Water",false,0,null,0.01,null,0.01,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyFlocfuron","Flocfuron",null,null,null,null,null,"Water",false,0,1,null,1,null,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyFluoranthene","Fluoranthene",null,null,null,null,null,"Water",false,0,0.12,6.3E-3,0.12,6.3E-3,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyFluoride (> 50mg/l CaCO3) (dissolved)","Fluoride (> 50mg/l CaCO3) (dissolved)",null,null,null,null,null,"Water",false,0,15000,5000,15000,5000,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyFluoride (≤ 50mg/l CaCO3) (dissolved)","Fluoride (≤ 50mg/l CaCO3) (dissolved)",null,null,null,null,null,"Water",false,0,3000,1000,15000,5000,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyFluoride >50mg/l CaCO3","Fluoride >50mg/l CaCO3",null,null,null,null,null,"Water",false,0,15000,5000,15000,5000,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyFluoride ≤50mg/l CaCO3","Fluoride ≤50mg/l CaCO3",null,null,null,null,null,"Water",false,0,3000,1000,15000,5000,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyFormaldehyde","Formaldehyde",5,100,null,null,51.9,"Both",false,0,50,5,null,null,false,null,null,null,null,null,null,"yes"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyGlyphosate","Glyphosate",null,null,null,null,null,"Water",false,null,398,196,398,196,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyHeptachlor & heptachlor epoxide","Heptachlor & heptachlor epoxide",null,null,null,null,null,"Water",false,null,2.9999999999999997E-4,1.9999999999999999E-7,3.0000000000000001E-5,1E-8,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyHexabromocyclododecane (HBCDD)","Hexabromocyclododecane (HBCDD)",null,null,null,null,null,"Water",false,null,0.5,1.6000000000000001E-3,0.05,8.0000000000000004E-4,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyHexachlorobenzene","Hexachlorobenzene",null,null,null,null,null,"Water",false,0,0.05,null,0.05,null,true,1,null,null,"Hexachlorobenzene",1000,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyHexachlorobutadiene","Hexachlorobutadiene",null,null,null,null,null,"Water",false,0,0.6,null,0.6,null,true,1,null,null,"Hexachlorobutadiene",1000,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyHexachlorocyclohexane","Hexachlorocyclohexane",null,null,null,null,null,"Water",false,0,0.04,0.02,0.02,2E-3,true,1,null,null,"Hexachlorocyclohexanes",1000,null,"no"]
[{"$f":"\"Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection Agency\"&B102","v":"Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyHydrogen sulphide"},"Hydrogen sulphide",140,150,null,null,null,"Both",false,0,1,0.25,10,null,false,null,null,null,null,null,null,"yes"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyIndeno (1,2,3-cd) pyrene (see PAHs for AA and biota EQS)","Indeno (1,2,3-cd) pyrene (see PAHs for AA and biota EQS)",null,null,null,null,null,"Water",false,null,null,null,null,null,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyIoxynil","Ioxynil",null,null,null,null,null,"Water",false,0,100,10,100,10,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyIron","Iron",null,null,null,null,null,"Water",false,0,null,1000,null,1000,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyIron (dissolved)","Iron (dissolved)",null,null,null,null,null,"Water",false,0,null,1000,null,1000,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyIsoproturon","Isoproturon",null,null,null,null,null,"Water",false,0,1,0.3,1,0.3,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyIvermectin","Ivermectin",null,null,null,null,null,"Water",false,0,1E-3,1E-4,0.01,1E-3,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyLead and its compounds (dissolved)","Lead and its compounds (dissolved)",null,null,null,null,null,"Water",false,0,14,1.2,14,1.3,false,null,null,null,"Lead",1000,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyLinuron (95%ile)","Linuron (95%ile)",null,null,null,null,null,"Water",false,0,0.9,0.5,0.9,0.5,false,null,null,null,"Linuron",1000,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyLithium (I) cation","Lithium (I) cation",null,null,null,null,null,null,null,null,1050,null,110,null,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyMalachite green","Malachite green",null,null,null,null,null,"Water",false,0,100,0.5,100,0.5,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyMalathion","Malathion",null,null,null,null,null,"Water",false,0,null,0.01,null,0.02,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyMancozeb","Mancozeb",null,null,null,null,null,"Water",false,0,20,2,20,2,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyManeb","Maneb",null,null,null,null,null,"Water",false,0,30,3,30,3,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyManganese","Manganese",null,null,null,null,null,null,null,null,null,123,null,null,null,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyMCPA (pH level less than 7)","MCPA (pH level less than 7)",null,null,null,null,null,"Water",false,0,80,12,800,80,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyMCPA (pH level higher than 7)","MCPA (pH level higher than 7)",null,null,null,null,null,"Water",false,0,100,80,800,80,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyMecoprop (95%ile)","Mecoprop (95%ile)",null,null,null,null,null,"Water",false,0,187,18,187,18,false,null,null,null,"Mecoprop",1000,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyMercury and its compounds (dissolved)","Mercury and its compounds (dissolved)",null,null,null,null,null,"Water",false,0,7.0000000000000007E-2,null,7.0000000000000007E-2,null,true,1,null,null,"Mercury",1000,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyMethiocarb","Methiocarb",null,null,null,null,null,"Water",false,0,0.77,0.01,null,"n/a",false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyMevinphos","Mevinphos",null,null,null,null,null,"Water",false,0,0.02,null,null,null,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyNaphthalene","Naphthalene",530,8000,null,null,null,"Both",false,0,130,2,130,2,false,null,null,null,"Napthalene",1000,1.0000000000000001E-5,"yes"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyNickel and its compounds (dissolved)","Nickel and its compounds (dissolved)",null,null,null,null,null,"Water",false,0,34,4,34,8.6,false,null,null,null,"Nickel",1000,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyNitrilotriacetic acid (NTA)","Nitrilotriacetic acid (NTA)",null,null,null,null,null,null,null,null,10000,1000,30000,3000,null,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyNonyl phenol (4-Nonylphenol)","Nonyl phenol (4-Nonylphenol)",null,null,null,null,null,"Water",false,0,2,0.3,2,0.3,true,1,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyNTA","NTA",null,null,null,null,null,"Water",false,0,10000,1000,30000,3000,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyOctyl phenol ((4-(1,1',3,3',-tetramethylbutyl)-phenol))","Octyl phenol ((4-(1,1',3,3',-tetramethylbutyl)-phenol))",null,null,null,null,null,"Water",false,0,null,0.1,null,0.01,false,null,null,null,"Octylphenols",1000,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyOmethoate","Omethoate",null,null,null,null,null,"Water",false,0,null,0.01,null,null,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection Agencypara-para DDT","para-para DDT",null,null,null,null,null,"Water",false,0,null,0.01,null,0.01,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyPCSDs","PCSDs",null,null,null,null,null,"Water",false,0,0.05,null,0.05,null,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyPendimethalin","Pendimethalin",null,null,null,null,null,"Water",false,0,0.57999999999999996,0.3,null,"n/a",false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyPentachlorobenzene","Pentachlorobenzene",null,null,null,null,null,"Water",false,0,null,7.0000000000000001E-3,null,6.9999999999999999E-4,true,1,null,null,null,null,null,"no"]
[{"$f":"\"Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection Agency\"&B134","v":"Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyPentachlorophenol"},"Pentachlorophenol",null,null,null,null,null,"Water",false,0,1,0.4,1,0.4,false,3,null,null,"Pentachlorophenol and its compound",1000,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyPerfluoroctane sulphonic acid and its salts (PFOS)","Perfluoroctane sulphonic acid and its salts (PFOS)",null,null,null,null,null,"Water",false,null,36,6.4999999999999997E-4,7.2,1.2999999999999999E-4,false,null,null,null,null,null,null,{"$f":"IF(C135+D135>0,\"yes\",\"no\")","v":"no"}]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyPermethrin (95%ile)","Permethrin (95%ile)",null,null,null,null,null,"Water",false,0,0.01,1E-3,1E-3,2.0000000000000001E-4,false,null,null,null,"Permethrin",1000,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyPhenol (95%ile)","Phenol (95%ile)",null,null,null,null,null,"Water",false,0,46,7.7,46,7.7,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyPirimiphos-methyl","Pirimiphos-methyl",null,null,null,null,null,"Water",false,0,0.05,1.4999999999999999E-2,0.05,1.4999999999999999E-2,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyPirmicarb","Pirmicarb",null,null,null,null,null,"Water",false,0,5,1,5,1,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyPolyaromatic hydrocarbons - Benzo (b) or (k)fluoranthene","Polyaromatic hydrocarbons - Benzo (b) or (k)fluoranthene",null,null,null,null,null,"Water",false,0,null,0.03,null,0.03,true,5,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyPolyaromatic hydrocarbons (PAH): Benzo (a)pyrene. Polyaromatic hydrocarbons (PAH) - Benzo(a)-pyrene (BaP), Benzo(b)-fluor-anthene, Benzo(k)-fluor-anthene, Benzo(g,h,i)-perylene and Indeno(1,2,3-cd)-pyrene. Benzo(a)pyrene can be  considered as a marker for the other PAHs, hence only benzo(a)pyrene needs to be  monitored for comparison with the biota EQS or the corresponding AA-EQS in water","Polyaromatic hydrocarbons (PAH): Benzo (a)pyrene. Polyaromatic hydrocarbons (PAH) - Benzo(a)-pyrene (BaP), Benzo(b)-fluor-anthene, Benzo(k)-fluor-anthene, Benzo(g,h,i)-perylene and Indeno(1,2,3-cd)-pyrene. Benzo(a)pyrene can be  considered as a marker for the other PAHs, hence only benzo(a)pyrene needs to be  monitored for comparison with the biota EQS or the corresponding AA-EQS in water",null,null,null,null,null,"Water",false,0,null,1.7000000000000001E-4,null,1.7000000000000001E-4,true,5,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyPolyaromatic hydrocarbons: Benzo (g,h,i)-perylene / Indeno(1,2,3-cd)-pyrene","Polyaromatic hydrocarbons: Benzo (g,h,i)-perylene / Indeno(1,2,3-cd)-pyrene",null,null,null,null,null,"Water",false,0,null,2E-3,null,2E-3,true,1,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyProchloraz","Prochloraz",null,null,null,null,null,"Water",false,0,40,4,40,4,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyPropetamphos","Propetamphos",null,null,null,null,null,"Water",false,0,0.1,0.03,0.1,0.03,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyPropyzamide","Propyzamide",null,null,null,null,null,"Water",false,0,1000,100,1000,100,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyQuinoxyfen","Quinoxyfen",null,null,null,null,null,"Water",false,null,2.7,0.15,0.54,1.4999999999999999E-2,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencySilver","Silver",null,null,null,null,null,"Water",false,0,0.1,0.05,1,0.5,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencySilver (dissolved)","Silver (dissolved)",null,null,null,null,null,"Water",false,0,0.1,0.05,1,0.5,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencySimazine","Simazine",null,null,null,null,null,"Water",false,0,4,1,4,1,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencySimazine (+ atrazine)","Simazine (+ atrazine)",null,null,null,null,null,"Water",false,0,2,0.6,2,0.6,false,null,null,null,"Simazine",1000,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyStyrene","Styrene",800,800,null,null,14.2,"Both",false,0,500,50,500,50,false,null,null,null,"Styrene",1000,500,"yes"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencySulcophuron","Sulcophuron",null,null,null,null,null,"Water",false,0,25,null,25,null,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencySulphate","Sulphate",null,null,null,null,null,"Water",false,0,null,400000,null,null,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyTecnazene (total)","Tecnazene (total)",null,null,null,null,null,"Water",false,0,10,1,10,1,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyTerbutryn","Terbutryn",null,null,null,null,null,"Water",false,null,0.34,6.2E-2,3.4000000000000002E-2,6.4999999999999997E-3,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyTetrachloroethane","Tetrachloroethane",null,null,null,null,null,"Water",false,null,1848,140,null,null,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyTetrachloroethylene","Tetrachloroethylene",3450,8000,null,null,2.9,"Both",false,0,null,10,null,10,false,null,null,null,"Tetrachloroethylene",1000,500,"yes"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyThiabendazole","Thiabendazole",null,null,null,null,null,"Water",false,0,50,5,50,5,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyTin (inorganic) - dissolved","Tin (inorganic) - dissolved",null,null,null,null,null,"Water",false,0,null,25,null,10,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyToluene (95%ile)","Toluene (95%ile)",null,null,null,null,null,"Water",false,0,380,74,370,74,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyTotal anions","Total anions",null,null,null,null,null,null,null,null,null,250000,null,null,null,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyTriallate","Triallate",null,null,null,null,null,"Water",false,0,5,0.25,5,0.25,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyTriazaphos","Triazaphos",null,null,null,null,null,"Water",false,0,null,5.0000000000000001E-3,null,5.0000000000000001E-3,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyTributyl phosphate","Tributyl phosphate",null,null,null,null,null,"Water",false,0,500,50,500,50,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyTributyltin compounds (Tributyltin cation)","Tributyltin compounds (Tributyltin cation)",null,null,null,null,null,"Water",false,0,1.5E-3,2.0000000000000001E-4,1.5E-3,2.0000000000000001E-4,true,1,null,null,"Tributyltin compounds",1000,null,"no"]
[{"$f":"\"Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection Agency\"&B166","v":"Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyTrichlorobenzenes"},"Trichlorobenzenes",null,null,null,null,null,"Water",false,0,null,0.4,null,0.4,false,null,null,null,"Trichlorobenzene all isomers",1000,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyTrichloroethylene","Trichloroethylene",1100,1000,null,null,32.5,"Both",false,0,null,10,null,10,false,null,null,null,"Trichloroethylene",1000,500,"yes"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyTrichloromethane (chloroform)","Trichloromethane (chloroform)",null,null,null,null,null,"Water",false,0,null,2.5,null,2.5,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyTriclosan","Triclosan",null,null,null,null,null,"Water",false,null,0.28000000000000003,0.1,0.28000000000000003,0.1,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyTrifluralin","Trifluralin",null,null,null,null,null,"Water",false,0,null,0.03,null,0.03,false,null,null,null,"Trifluralin",1000,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyTriphenyltin & derivatives","Triphenyltin & derivatives",null,null,null,null,null,"Water",false,0,0.02,null,8.0000000000000002E-3,null,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyUn-ionised ammonia as nitrogen","Un-ionised ammonia as nitrogen",null,null,null,null,null,"Water",false,0,null,null,null,21,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyVanadium (> 200 mg/l CaCO3)","Vanadium (> 200 mg/l CaCO3)",null,null,null,null,null,"Water",false,0,null,60,null,100,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyVanadium (0 - 200 mg/l CaCO3)","Vanadium (0 - 200 mg/l CaCO3)",null,null,null,null,null,"Water",false,0,null,20,null,100,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyXylene","Xylene",null,null,null,null,null,null,null,null,null,30,null,30,null,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyZinc","Zinc",null,null,null,null,null,"Water",false,null,null,10.9,null,6.8,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyZinc - dissolved plus ambient background concentration. For saltwater, an ambient background concentration of 1.1ug/l is recommended.","Zinc - dissolved plus ambient background concentration. For saltwater, an ambient background concentration of 1.1ug/l is recommended.",null,null,null,null,null,null,null,null,null,null,null,30,false,null,null,null,null,null,null,"no"]
["Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency/Scottish Environment Protection AgencyDiflubenzuron","Diflubenzuron",null,null,null,null,null,"Water",false,0,1.4999999999999999E-2,1E-3,0.1,5.0000000000000001E-3,false,null,null,null,null,null,null,"no"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"no"]
[]
[]
[]
[]
[]
[]
[null,null,null,null,null,null,null,"Water",true]
[null,null,null,null,null,null,null,"Water",true]
[null,null,null,null,null,null,null,"Water",true]
[null,null,null,null,null,null,null,"Water",true]
[null,null,null,null,null,null,null,"Water",true]
[null,null,null,null,null,null,null,"Water",true]
[null,null,null,null,null,null,null,"Water",true]
[null,null,null,null,null,null,null,"Water",true]
[null,null,null,null,null,null,null,"Water",true]
[null,null,null,null,null,null,null,"Water",true]
[null,null,null,null,null,null,null,"Water",true]
[null,null,null,null,null,null,null,"Water",true]
[null,null,null,null,null,null,null,"Water",true]
[null,null,null,null,null,null,null,"Water",true]
[null,null,null,null,null,null,null,"Water",true]
[null,null,null,null,null,null,null,"Water",true]
[null,null,null,null,null,null,null,"Water",true]
[null,null,null,null,null,null,null,"Water",true]
[null,null,null,null,null,null,null,"Water",true]
[null,null,null,null,null,null,null,"Water",true]
[null,null,null,null,null,null,null,"Water",true]
[null,null,null,null,null,null,null,"Water",true]
[null,null,null,null,null,null,null,"Water",true]
[null,null,null,null,null,null,null,"Water",true]
[null,null,null,null,null,null,null,"Water",true]
[null,null,null,null,null,null,null,"Water",true]
[null,null,null,null,null,null,null,"Water",true]
[null,null,null,null,null,null,null,"Water",true]
[null,null,null,null,null,null,null,"Water",true]
[null,null,null,null,null,null,null,"Water",true]
[null,null,null,null,null,null,null,"Water",true]
[null,null,null,null,null,null,null,"Water",true]
[null,null,null,null,null,null,null,"Water",true]
[null,null,null,null,null,null,null,"Water",true]

{"sheet":"Devel1","index":33,"n_rows":95,"n_cols":8,"rows_kept":95,"cut":false,"hidden":false,"merged":[]}
[]
[null,"Notes"]
[null,null,"The functions and data on this page are for support of development and should not be used without first understanding their operation."]
[]
[]
[]
[]
[null,null,"Rerun initialisation"]
[]
[]
[]
[]
[]
[]
[null,null,null,0,0,true,"TR",0]
[null,null,null,0,1,true,"River Nene",0]
[null,null,null,0,2,false,null,1.5]
[null,null,null,0,3,true,"W1",0]
[null,null,null,0,4,false,null,2.5]
[null,null,null,0,5,false,null,5]
[null,null,null,0,6,false,null,0]
[null,null,null,0,7,true,"2,4-Dichlorophenol",0]
[null,null,null,0,8,false,null,0.5]
[null,null,null,0,9,false,null,0]
[null,null,null,0,10,false,null,0]
[null,null,null,0,11,false,null,1]
[null,null,null,1,0,false,null,0]
[null,null,null,1,1,false,null,0]
[null,null,null,1,2,false,null,0]
[null,null,null,1,3,false,null,0]
[null,null,null,1,4,false,null,0]
[null,null,null,1,5,false,null,0]
[null,null,null,1,6,false,null,0]
[null,null,null,1,7,false,null,0]
[null,null,null,1,8,false,null,0]
[null,null,null,1,9,false,null,0]
[null,null,null,1,10,false,null,0]
[null,null,null,1,11,false,null,0]
[null,null,null,2,0,false,null,0]
[null,null,null,2,1,false,null,0]
[null,null,null,2,2,false,null,0]
[null,null,null,2,3,false,null,0]
[null,null,null,2,4,false,null,0]
[null,null,null,2,5,false,null,0]
[null,null,null,2,6,false,null,0]
[null,null,null,2,7,false,null,0]
[null,null,null,2,8,false,null,0]
[null,null,null,2,9,false,null,0]
[null,null,null,2,10,false,null,0]
[null,null,null,2,11,false,null,0]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[null,null,null,0,0,true,"TR",0]
[null,null,null,0,1,true,"River Nene",0]
[null,null,null,0,2,false,null,1.5]
[null,null,null,0,3,true,"2,4-Dichlorophenol",0]
[null,null,null,0,4,false,null,0.3125]
[null,null,null,0,5,false,null,0.76923076923076927]
[null,null,null,0,6,false,null,0]
[null,null,null,0,7,true,"2,4-Dichlorophenol",0]
[null,null,null,0,8,false,null,0.5]
[null,null,null,0,9,false,null,0]
[null,null,null,0,10,false,null,0]
[null,null,null,0,11,false,null,1]
[null,null,null,1,0,false,null,0]
[null,null,null,1,1,false,null,0]
[null,null,null,1,2,false,null,0]
[null,null,null,1,3,false,null,0]
[null,null,null,1,4,false,null,0]
[null,null,null,1,5,false,null,0]
[null,null,null,1,6,false,null,0]
[null,null,null,1,7,false,null,0]
[null,null,null,1,8,false,null,0]
[null,null,null,1,9,false,null,0]
[null,null,null,1,10,false,null,0]
[null,null,null,1,11,false,null,0]
[null,null,null,2,0,false,null,0]
[null,null,null,2,1,false,null,0]
[null,null,null,2,2,false,null,0]
[null,null,null,2,3,false,null,0]
[null,null,null,2,4,false,null,0]
[null,null,null,2,5,false,null,0]
[null,null,null,2,6,false,null,0]
[null,null,null,2,7,false,null,0]
[null,null,null,2,8,false,null,0]
[null,null,null,2,9,false,null,0]
[null,null,null,2,10,false,null,0]
[null,null,null,2,11,false,null,0]

{"sheet":"0Ei","index":34,"n_rows":30,"n_cols":11,"rows_kept":30,"cut":false,"hidden":false,"merged":[]}
[]
["Energy",{"$f":"B1+1","v":1},null,{"$f":"IFERROR(VLOOKUP(#REF!,Variables!$AH$3:$AI$19,2,FALSE),\"\")","v":""},null,{"$f":"IF(ISNUMBER(VLOOKUP(#REF!,Variables!$AH$3:$AK$19,4,FALSE)),VLOOKUP(#REF!,Variables!$AH$3:$AK$19,4,FALSE),\"Please specify a conversion factor on the right or enter 1\")","v":"Please specify a conversion factor on the right or enter 1"},null,{"$f":"IF(ISNUMBER(#REF!),#REF!*#REF!,IF(ISNUMBER(#REF!),#REF!*#REF!,\"Please enter a conversion factor or a value of 1 in column G\"))","v":"Please enter a conversion factor or a value of 1 in column G"},{"$f":"IF(ISNUMBER(VLOOKUP(#REF!,Variables!$AH$3:$AK$19,3,FALSE)),VLOOKUP(#REF!,Variables!$AH$3:$AK$19,3,FALSE),\"Please specify a CO2 factor on the right\")","v":"Please specify a CO2 factor on the right"},null,{"$f":"IF(ISNUMBER(#REF!),#REF!*#REF!,IF(ISNUMBER(#REF!),#REF!*#REF!,\"Please enter a CO2 factor in column J\"))","v":"Please enter a CO2 factor in column J"}]
["Option 0: Default Blank Option"]
[null,null,null,null,null,"Please specify a conversion factor on the right or enter 1",null,null,"Please specify a CO2 factor on the right"]
[]
[null,null,null,null,null,null,null,"Please enter a conversion factor or a value of 1 in column G",null,null,"Please enter a CO2 factor in column J"]
[null,"Number","Energy source","Direct/Indirect emissions","Delivered MWh/yr","Conversion factor","User conv factor","Primary MWh/yr","CO2 factor","User CO2 factor","CO2 tonne/yr"]
[null,1,null,{"$f":"IFERROR(VLOOKUP('0Ei'!C8,Variables!$AH$3:$AI$19,2,FALSE),\"\")","v":""},null,{"$f":"IF(ISNUMBER(VLOOKUP('0Ei'!$C8,Variables!$AH$3:$AK$19,4,FALSE)),VLOOKUP('0Ei'!$C8,Variables!$AH$3:$AK$19,4,FALSE),\"\")","v":""},null,{"$f":"IF(ISNUMBER('0Ei'!$F8),'0Ei'!$E8*'0Ei'!$F8,IF(ISNUMBER('0Ei'!$G8),'0Ei'!$E8*'0Ei'!$G8,\"\"))","v":""},{"$f":"IF(ISNUMBER(VLOOKUP('0Ei'!$C8,Variables!$AH$3:$AK$19,3,FALSE)),VLOOKUP('0Ei'!$C8,Variables!$AH$3:$AK$19,3,FALSE),\"\")","v":""},null,{"$f":"IF(ISNUMBER('0Ei'!$I8),'0Ei'!$H8*'0Ei'!$I8,IF(ISNUMBER('0Ei'!$J8),'0Ei'!$H8*'0Ei'!$I8,\"\"))","v":""}]
[null,{"$f":"B8+1","v":2},null,{"$f":"IFERROR(VLOOKUP('0Ei'!C9,Variables!$AH$3:$AI$19,2,FALSE),\"\")","v":""},null,{"$f":"IF(ISNUMBER(VLOOKUP('0Ei'!$C9,Variables!$AH$3:$AK$19,4,FALSE)),VLOOKUP('0Ei'!$C9,Variables!$AH$3:$AK$19,4,FALSE),\"\")","v":""},null,{"$f":"IF(ISNUMBER('0Ei'!$F9),'0Ei'!$E9*'0Ei'!$F9,IF(ISNUMBER('0Ei'!$G9),'0Ei'!$E9*'0Ei'!$G9,\"\"))","v":""},{"$f":"IF(ISNUMBER(VLOOKUP('0Ei'!$C9,Variables!$AH$3:$AK$19,3,FALSE)),VLOOKUP('0Ei'!$C9,Variables!$AH$3:$AK$19,3,FALSE),\"\")","v":""},null,{"$f":"IF(ISNUMBER('0Ei'!$I9),'0Ei'!$H9*'0Ei'!$I9,IF(ISNUMBER('0Ei'!$J9),'0Ei'!$H9*'0Ei'!$I9,\"\"))","v":""}]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[null,null,null,"Comments:"]

{"sheet":"0Ri","index":35,"n_rows":9,"n_cols":5,"rows_kept":9,"cut":false,"hidden":false,"merged":[]}
[]
["Raw",{"$f":"B1+1","v":1}]
["Option 0: Default Blank Option"]
[]
[]
[]
[null,"Number","Material","Annual consumption","Units"]
[null,1,"Non-potable water"]
[null,{"$f":"B8+1","v":2},"Potable water"]

{"sheet":"0Wastei","index":36,"n_rows":9,"n_cols":6,"rows_kept":9,"cut":false,"hidden":false,"merged":[]}
[]
["Waste",{"$f":"B1+1","v":1}]
["Option 0: Default Blank Option"]
[]
[]
[]
[null,"Number","Waste stream","Category of waste","Mass (t/yr)","Disposal/Recovery option"]
[null,1]
[null,{"$f":"B8+1","v":2}]

{"sheet":"0WatoR1","index":37,"n_rows":296,"n_cols":17,"rows_kept":296,"cut":false,"hidden":false,"merged":[[0,7,0,8]]}
[]
["Option 0: Default Blank Option"]
[]
[null,null,"Type of water body","Description","Freshwater Q95 flowrate (m3/s)","Release point","Mean effluent flow rate (m3/s)","Max effluent flow rate (m3/s)","Sewer factor (%)","Substance","Release conc  (ug/l)","Annual EQS (ug/l)","Test 1: Release conc <10% EQS avg","Max release conc (ug/l)","MAC (ug/l)","Test: Release conc <10% EQS max","Comments"]
[{"$f":"C5&F5&J5","v":""},null,null,null,null,null,null,null,null,null,null,{"$f":"IF(RivTest129[[#This Row],[Substance]]<>\"\",(IFERROR(VLOOKUP(\"*\"&'Reference information'!$E$14&\"*\"&RivTest129[[#This Row],[Substance]],SubstancesW!$A$6:$U$168,SubstancesW!$M$4,FALSE),\"\")),\"\")","v":""},{"$f":"IFERROR(IF(RivTest129[[#This Row],[Release conc  (ug/l)]]/RivTest129[[#This Row],[Annual EQS (ug/l)]]<0.1,\"Pass\",IF(RivTest129[[#This Row],[Release conc  (ug/l)]]/RivTest129[[#This Row],[Annual EQS (ug/l)]]>=0.1,\"Fail\",\"some error\")),\"\")","v":""},null,{"$f":"IFERROR(VLOOKUP(RivTest129[[#This Row],[Substance]],SubstancesW!$B$6:$U$168,SubstancesW!$K$4,FALSE),\"N/A\")","v":"N/A"},{"$f":"IF(RivTest129[[#This Row],[MAC (ug/l)]]>0,IFERROR(IF(RivTest129[[#This Row],[Max release conc (ug/l)]]/RivTest129[[#This Row],[MAC (ug/l)]]<0.1,\"Pass\",IF(RivTest129[[#This Row],[Max release conc (ug/l)]]/RivTest129[[#This Row],[MAC (ug/l)]]>=0.1,\"Fail\",\"some error\")),\"\"),\"N/A\")","v":""}]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL62),INDIRECT(\"F\"&Variables!BL62),INDIRECT(\"J\"&Variables!BL62))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL63),INDIRECT(\"F\"&Variables!BL63),INDIRECT(\"J\"&Variables!BL63))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL64),INDIRECT(\"F\"&Variables!BL64),INDIRECT(\"J\"&Variables!BL64))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL65),INDIRECT(\"F\"&Variables!BL65),INDIRECT(\"J\"&Variables!BL65))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL66),INDIRECT(\"F\"&Variables!BL66),INDIRECT(\"J\"&Variables!BL66))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL67),INDIRECT(\"F\"&Variables!BL67),INDIRECT(\"J\"&Variables!BL67))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL68),INDIRECT(\"F\"&Variables!BL68),INDIRECT(\"J\"&Variables!BL68))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL69),INDIRECT(\"F\"&Variables!BL69),INDIRECT(\"J\"&Variables!BL69))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL70),INDIRECT(\"F\"&Variables!BL70),INDIRECT(\"J\"&Variables!BL70))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL71),INDIRECT(\"F\"&Variables!BL71),INDIRECT(\"J\"&Variables!BL71))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL72),INDIRECT(\"F\"&Variables!BL72),INDIRECT(\"J\"&Variables!BL72))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL73),INDIRECT(\"F\"&Variables!BL73),INDIRECT(\"J\"&Variables!BL73))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL74),INDIRECT(\"F\"&Variables!BL74),INDIRECT(\"J\"&Variables!BL74))","v":""}]
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[]
["Option 0: Default Blank Option"]
[null,null,null,null,null,null,null,null,null,null,null,"Annual avg EQS",null,null,null,null,"MAC EQS"]
[null,null,"Type of water body","Description","Freshwater Q95 flowrate (m3/s)","Release point","Mean effluent flow rate (m3/s)","Max effluent flow rate (m3/s)","Substance","Release conc (ug/l)","Max release conc (ug/l)","Annual EQS (ug/l)","PC (ug/l)","Modelled PC (ug/l)","%PC of EQS%","Test 2: PC<4% of EQS?","MAC EQS (ug/l)","PC (max) (ug/l)","Modelled PC (max) (ug/l)","%PC of MAC","Test 2: PC<4% of MAC?"]
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[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL200),INDIRECT(\"F\"&Variables!BL200),INDIRECT(\"I\"&Variables!BL200))","v":""}]
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[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL205),INDIRECT(\"F\"&Variables!BL205),INDIRECT(\"I\"&Variables!BL205))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL206),INDIRECT(\"F\"&Variables!BL206),INDIRECT(\"I\"&Variables!BL206))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL207),INDIRECT(\"F\"&Variables!BL207),INDIRECT(\"I\"&Variables!BL207))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL208),INDIRECT(\"F\"&Variables!BL208),INDIRECT(\"I\"&Variables!BL208))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL209),INDIRECT(\"F\"&Variables!BL209),INDIRECT(\"I\"&Variables!BL209))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL210),INDIRECT(\"F\"&Variables!BL210),INDIRECT(\"I\"&Variables!BL210))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL211),INDIRECT(\"F\"&Variables!BL211),INDIRECT(\"I\"&Variables!BL211))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL212),INDIRECT(\"F\"&Variables!BL212),INDIRECT(\"I\"&Variables!BL212))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL213),INDIRECT(\"F\"&Variables!BL213),INDIRECT(\"I\"&Variables!BL213))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL214),INDIRECT(\"F\"&Variables!BL214),INDIRECT(\"I\"&Variables!BL214))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL215),INDIRECT(\"F\"&Variables!BL215),INDIRECT(\"I\"&Variables!BL215))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL216),INDIRECT(\"F\"&Variables!BL216),INDIRECT(\"I\"&Variables!BL216))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL217),INDIRECT(\"F\"&Variables!BL217),INDIRECT(\"I\"&Variables!BL217))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL218),INDIRECT(\"F\"&Variables!BL218),INDIRECT(\"I\"&Variables!BL218))","v":""}]
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[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL221),INDIRECT(\"F\"&Variables!BL221),INDIRECT(\"I\"&Variables!BL221))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL222),INDIRECT(\"F\"&Variables!BL222),INDIRECT(\"I\"&Variables!BL222))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL223),INDIRECT(\"F\"&Variables!BL223),INDIRECT(\"I\"&Variables!BL223))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL224),INDIRECT(\"F\"&Variables!BL224),INDIRECT(\"I\"&Variables!BL224))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL225),INDIRECT(\"F\"&Variables!BL225),INDIRECT(\"I\"&Variables!BL225))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL226),INDIRECT(\"F\"&Variables!BL226),INDIRECT(\"I\"&Variables!BL226))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL227),INDIRECT(\"F\"&Variables!BL227),INDIRECT(\"I\"&Variables!BL227))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL228),INDIRECT(\"F\"&Variables!BL228),INDIRECT(\"I\"&Variables!BL228))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL229),INDIRECT(\"F\"&Variables!BL229),INDIRECT(\"I\"&Variables!BL229))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL230),INDIRECT(\"F\"&Variables!BL230),INDIRECT(\"I\"&Variables!BL230))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL231),INDIRECT(\"F\"&Variables!BL231),INDIRECT(\"I\"&Variables!BL231))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL232),INDIRECT(\"F\"&Variables!BL232),INDIRECT(\"I\"&Variables!BL232))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL233),INDIRECT(\"F\"&Variables!BL233),INDIRECT(\"I\"&Variables!BL233))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL235),INDIRECT(\"F\"&Variables!BL235),INDIRECT(\"I\"&Variables!BL235))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL236),INDIRECT(\"F\"&Variables!BL236),INDIRECT(\"I\"&Variables!BL236))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL237),INDIRECT(\"F\"&Variables!BL237),INDIRECT(\"I\"&Variables!BL237))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL238),INDIRECT(\"F\"&Variables!BL238),INDIRECT(\"I\"&Variables!BL238))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL239),INDIRECT(\"F\"&Variables!BL239),INDIRECT(\"I\"&Variables!BL239))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL240),INDIRECT(\"F\"&Variables!BL240),INDIRECT(\"I\"&Variables!BL240))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL241),INDIRECT(\"F\"&Variables!BL241),INDIRECT(\"I\"&Variables!BL241))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL242),INDIRECT(\"F\"&Variables!BL242),INDIRECT(\"I\"&Variables!BL242))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL243),INDIRECT(\"F\"&Variables!BL243),INDIRECT(\"I\"&Variables!BL243))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL244),INDIRECT(\"F\"&Variables!BL244),INDIRECT(\"I\"&Variables!BL244))","v":""}]
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[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL247),INDIRECT(\"F\"&Variables!BL247),INDIRECT(\"I\"&Variables!BL247))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL248),INDIRECT(\"F\"&Variables!BL248),INDIRECT(\"I\"&Variables!BL248))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL249),INDIRECT(\"F\"&Variables!BL249),INDIRECT(\"I\"&Variables!BL249))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL250),INDIRECT(\"F\"&Variables!BL250),INDIRECT(\"I\"&Variables!BL250))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL251),INDIRECT(\"F\"&Variables!BL251),INDIRECT(\"I\"&Variables!BL251))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL252),INDIRECT(\"F\"&Variables!BL252),INDIRECT(\"I\"&Variables!BL252))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL253),INDIRECT(\"F\"&Variables!BL253),INDIRECT(\"I\"&Variables!BL253))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL254),INDIRECT(\"F\"&Variables!BL254),INDIRECT(\"I\"&Variables!BL254))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL255),INDIRECT(\"F\"&Variables!BL255),INDIRECT(\"I\"&Variables!BL255))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL256),INDIRECT(\"F\"&Variables!BL256),INDIRECT(\"I\"&Variables!BL256))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL257),INDIRECT(\"F\"&Variables!BL257),INDIRECT(\"I\"&Variables!BL257))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL258),INDIRECT(\"F\"&Variables!BL258),INDIRECT(\"I\"&Variables!BL258))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL259),INDIRECT(\"F\"&Variables!BL259),INDIRECT(\"I\"&Variables!BL259))","v":""}]
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[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL261),INDIRECT(\"F\"&Variables!BL261),INDIRECT(\"I\"&Variables!BL261))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL262),INDIRECT(\"F\"&Variables!BL262),INDIRECT(\"I\"&Variables!BL262))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL263),INDIRECT(\"F\"&Variables!BL263),INDIRECT(\"I\"&Variables!BL263))","v":""}]
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{"sheet":"0WatoR3","index":39,"n_rows":300,"n_cols":24,"rows_kept":300,"cut":false,"hidden":false,"merged":[[0,3,0,5]]}
[]
["Option 0: Default Blank Option"]
[]
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[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL294),INDIRECT(\"F\"&Variables!BL294),INDIRECT(\"I\"&Variables!BL294))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL295),INDIRECT(\"F\"&Variables!BL295),INDIRECT(\"I\"&Variables!BL295))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL296),INDIRECT(\"F\"&Variables!BL296),INDIRECT(\"I\"&Variables!BL296))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL297),INDIRECT(\"F\"&Variables!BL297),INDIRECT(\"I\"&Variables!BL297))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL298),INDIRECT(\"F\"&Variables!BL298),INDIRECT(\"I\"&Variables!BL298))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL299),INDIRECT(\"F\"&Variables!BL299),INDIRECT(\"I\"&Variables!BL299))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL300),INDIRECT(\"F\"&Variables!BL300),INDIRECT(\"I\"&Variables!BL300))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL301),INDIRECT(\"F\"&Variables!BL301),INDIRECT(\"I\"&Variables!BL301))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL302),INDIRECT(\"F\"&Variables!BL302),INDIRECT(\"I\"&Variables!BL302))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL303),INDIRECT(\"F\"&Variables!BL303),INDIRECT(\"I\"&Variables!BL303))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL304),INDIRECT(\"F\"&Variables!BL304),INDIRECT(\"I\"&Variables!BL304))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL305),INDIRECT(\"F\"&Variables!BL305),INDIRECT(\"I\"&Variables!BL305))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL306),INDIRECT(\"F\"&Variables!BL306),INDIRECT(\"I\"&Variables!BL306))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL307),INDIRECT(\"F\"&Variables!BL307),INDIRECT(\"I\"&Variables!BL307))","v":""}]

{"sheet":"0WatoT1","index":40,"n_rows":300,"n_cols":17,"rows_kept":300,"cut":false,"hidden":false,"merged":[[0,2,0,3]]}
[]
["Option 0: Default Blank Option"]
[]
[null,null,"Type of water body","Description","Freshwater Q95 flowrate (m3/s)","Release point","Mean effluent flow rate (m3/s)","Max effluent flow rate (m3/s)","Sewer factor (%)","Substance","Release conc (ug/l)","Annual EQS (ug/l)","Test 1: Release conc <100% EQS avg","Max release conc (ug/l)","MAC (ug/l)","Test 1: Release conc <100% EQS max","Comments"]
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{"sheet":"0WatoT2","index":41,"n_rows":301,"n_cols":16,"rows_kept":301,"cut":false,"hidden":false,"merged":[[0,3,0,4],[2,6,2,10],[2,11,2,15]]}
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["Option 0: Default Blank Option"]
[null,null,null,null,null,null,"Annual avg EQS",null,null,null,null,"MAC EQS"]
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{"sheet":"0WatoT3","index":42,"n_rows":302,"n_cols":20,"rows_kept":302,"cut":false,"hidden":false,"merged":[[0,3,0,4]]}
[]
["Option 0: Default Blank Option"]
[]
[null,null,"Type of water body","Description","Freshwater Q95 flowrate (m3/s)","Substance","Annual Average Background conc (ug/l)","PC (ug/l)","PEC (ug/l)","Annual EQS (ug/l)","(PEC-BC)/EQS","Test 3 - (PEC-BC)/EQS>10% annual EQS","%PEC EQS %","Test 4a - PEC >100% EQS","MAC EQS (ug/l)","PC (max) (ug/l)","PEC Max (ug/l)","%PEC of MAC %","Test 4b: PEC>100% MAC","DOC"]
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[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL239),INDIRECT(\"F\"&Variables!BL239),INDIRECT(\"J\"&Variables!BL239))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL240),INDIRECT(\"F\"&Variables!BL240),INDIRECT(\"J\"&Variables!BL240))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL241),INDIRECT(\"F\"&Variables!BL241),INDIRECT(\"J\"&Variables!BL241))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL242),INDIRECT(\"F\"&Variables!BL242),INDIRECT(\"J\"&Variables!BL242))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL243),INDIRECT(\"F\"&Variables!BL243),INDIRECT(\"J\"&Variables!BL243))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL244),INDIRECT(\"F\"&Variables!BL244),INDIRECT(\"J\"&Variables!BL244))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL245),INDIRECT(\"F\"&Variables!BL245),INDIRECT(\"J\"&Variables!BL245))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL247),INDIRECT(\"F\"&Variables!BL247),INDIRECT(\"J\"&Variables!BL247))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL248),INDIRECT(\"F\"&Variables!BL248),INDIRECT(\"J\"&Variables!BL248))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL249),INDIRECT(\"F\"&Variables!BL249),INDIRECT(\"J\"&Variables!BL249))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL250),INDIRECT(\"F\"&Variables!BL250),INDIRECT(\"J\"&Variables!BL250))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL251),INDIRECT(\"F\"&Variables!BL251),INDIRECT(\"J\"&Variables!BL251))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL252),INDIRECT(\"F\"&Variables!BL252),INDIRECT(\"J\"&Variables!BL252))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL253),INDIRECT(\"F\"&Variables!BL253),INDIRECT(\"J\"&Variables!BL253))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL254),INDIRECT(\"F\"&Variables!BL254),INDIRECT(\"J\"&Variables!BL254))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL255),INDIRECT(\"F\"&Variables!BL255),INDIRECT(\"J\"&Variables!BL255))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL256),INDIRECT(\"F\"&Variables!BL256),INDIRECT(\"J\"&Variables!BL256))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL257),INDIRECT(\"F\"&Variables!BL257),INDIRECT(\"J\"&Variables!BL257))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL258),INDIRECT(\"F\"&Variables!BL258),INDIRECT(\"J\"&Variables!BL258))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL259),INDIRECT(\"F\"&Variables!BL259),INDIRECT(\"J\"&Variables!BL259))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL260),INDIRECT(\"F\"&Variables!BL260),INDIRECT(\"J\"&Variables!BL260))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL261),INDIRECT(\"F\"&Variables!BL261),INDIRECT(\"J\"&Variables!BL261))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL262),INDIRECT(\"F\"&Variables!BL262),INDIRECT(\"J\"&Variables!BL262))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL263),INDIRECT(\"F\"&Variables!BL263),INDIRECT(\"J\"&Variables!BL263))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL264),INDIRECT(\"F\"&Variables!BL264),INDIRECT(\"J\"&Variables!BL264))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL265),INDIRECT(\"F\"&Variables!BL265),INDIRECT(\"J\"&Variables!BL265))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL266),INDIRECT(\"F\"&Variables!BL266),INDIRECT(\"J\"&Variables!BL266))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL267),INDIRECT(\"F\"&Variables!BL267),INDIRECT(\"J\"&Variables!BL267))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL268),INDIRECT(\"F\"&Variables!BL268),INDIRECT(\"J\"&Variables!BL268))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL269),INDIRECT(\"F\"&Variables!BL269),INDIRECT(\"J\"&Variables!BL269))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL270),INDIRECT(\"F\"&Variables!BL270),INDIRECT(\"J\"&Variables!BL270))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL271),INDIRECT(\"F\"&Variables!BL271),INDIRECT(\"J\"&Variables!BL271))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL272),INDIRECT(\"F\"&Variables!BL272),INDIRECT(\"J\"&Variables!BL272))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL273),INDIRECT(\"F\"&Variables!BL273),INDIRECT(\"J\"&Variables!BL273))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL274),INDIRECT(\"F\"&Variables!BL274),INDIRECT(\"J\"&Variables!BL274))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL275),INDIRECT(\"F\"&Variables!BL275),INDIRECT(\"J\"&Variables!BL275))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL276),INDIRECT(\"F\"&Variables!BL276),INDIRECT(\"J\"&Variables!BL276))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL277),INDIRECT(\"F\"&Variables!BL277),INDIRECT(\"J\"&Variables!BL277))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL278),INDIRECT(\"F\"&Variables!BL278),INDIRECT(\"J\"&Variables!BL278))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL279),INDIRECT(\"F\"&Variables!BL279),INDIRECT(\"J\"&Variables!BL279))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL280),INDIRECT(\"F\"&Variables!BL280),INDIRECT(\"J\"&Variables!BL280))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL281),INDIRECT(\"F\"&Variables!BL281),INDIRECT(\"J\"&Variables!BL281))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL282),INDIRECT(\"F\"&Variables!BL282),INDIRECT(\"J\"&Variables!BL282))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL283),INDIRECT(\"F\"&Variables!BL283),INDIRECT(\"J\"&Variables!BL283))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL284),INDIRECT(\"F\"&Variables!BL284),INDIRECT(\"J\"&Variables!BL284))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL285),INDIRECT(\"F\"&Variables!BL285),INDIRECT(\"J\"&Variables!BL285))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL286),INDIRECT(\"F\"&Variables!BL286),INDIRECT(\"J\"&Variables!BL286))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL287),INDIRECT(\"F\"&Variables!BL287),INDIRECT(\"J\"&Variables!BL287))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL288),INDIRECT(\"F\"&Variables!BL288),INDIRECT(\"J\"&Variables!BL288))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL289),INDIRECT(\"F\"&Variables!BL289),INDIRECT(\"J\"&Variables!BL289))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL290),INDIRECT(\"F\"&Variables!BL290),INDIRECT(\"J\"&Variables!BL290))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL291),INDIRECT(\"F\"&Variables!BL291),INDIRECT(\"J\"&Variables!BL291))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL292),INDIRECT(\"F\"&Variables!BL292),INDIRECT(\"J\"&Variables!BL292))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL293),INDIRECT(\"F\"&Variables!BL293),INDIRECT(\"J\"&Variables!BL293))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL294),INDIRECT(\"F\"&Variables!BL294),INDIRECT(\"J\"&Variables!BL294))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL295),INDIRECT(\"F\"&Variables!BL295),INDIRECT(\"J\"&Variables!BL295))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL296),INDIRECT(\"F\"&Variables!BL296),INDIRECT(\"J\"&Variables!BL296))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL297),INDIRECT(\"F\"&Variables!BL297),INDIRECT(\"J\"&Variables!BL297))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL298),INDIRECT(\"F\"&Variables!BL298),INDIRECT(\"J\"&Variables!BL298))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL299),INDIRECT(\"F\"&Variables!BL299),INDIRECT(\"J\"&Variables!BL299))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL300),INDIRECT(\"F\"&Variables!BL300),INDIRECT(\"J\"&Variables!BL300))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL301),INDIRECT(\"F\"&Variables!BL301),INDIRECT(\"J\"&Variables!BL301))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL302),INDIRECT(\"F\"&Variables!BL302),INDIRECT(\"J\"&Variables!BL302))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL303),INDIRECT(\"F\"&Variables!BL303),INDIRECT(\"J\"&Variables!BL303))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL304),INDIRECT(\"F\"&Variables!BL304),INDIRECT(\"J\"&Variables!BL304))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL305),INDIRECT(\"F\"&Variables!BL305),INDIRECT(\"J\"&Variables!BL305))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL306),INDIRECT(\"F\"&Variables!BL306),INDIRECT(\"J\"&Variables!BL306))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL307),INDIRECT(\"F\"&Variables!BL307),INDIRECT(\"J\"&Variables!BL307))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL308),INDIRECT(\"F\"&Variables!BL308),INDIRECT(\"J\"&Variables!BL308))","v":{"$error":"#REF!"}}]

{"sheet":"0WatoT4","index":43,"n_rows":5,"n_cols":10,"rows_kept":5,"cut":false,"hidden":false,"merged":[]}
[]
["Option 0: Default Blank Option"]
[]
[null,null,"Type of water body","Description","Release point","1. Is the discharge to a riverine estuary or direct to a low water channel within an estuary?","2. Is the discharge to a location with restricted dilution/dispersion characteristics?","3. Is the discharge either to a location less than 50m offshore from where the sea-bed is at Chart Datum or to a location where the sea-bed is less than 1m below Chart Datum?","4. Is the discharge buoyant?","Notes"]
[null,null,"T","Horton Brook","W1","Yes","Unrequired","Unrequired",null,{"$f":"IF(TRACTest438[[#This Row],[1. Is the discharge to a riverine estuary or direct to a low water channel within an estuary?]]=\"Yes\",\"Ensure the receiving water is set to TR and complete ‘TRAC tests 2-4’ and that ‘TRAC test 5b’ doesn’t need to be completed \",IF(TRACTest438[[#This Row],[2. Is the discharge to a location with restricted dilution/dispersion characteristics?]]=\"Yes\",\"Proceed to Phase 2: Modelling\",IF(TRACTest438[[#This Row],[3. Is the discharge either to a location less than 50m offshore from where the sea-bed is at Chart Datum or to a location where the sea-bed is less than 1m below Chart Datum?]]=\"Yes\",\"Proceed to Phase 2, Modelling\",IF(TRACTest438[[#This Row],[4. Is the discharge buoyant?]]=\"Yes\", \"Proceed to TRAC test 5b\",IF(TRACTest438[[#This Row],[4. Is the discharge buoyant?]]=\"No\", \"Proceed to Phase 2: Modelling\")))))","v":"Ensure the receiving water is set to TR and complete ‘TRAC tests 2-4’ and that ‘TRAC test 5b’ doesn’t need to be completed "}]

{"sheet":"0WatoT5","index":44,"n_rows":204,"n_cols":20,"rows_kept":204,"cut":false,"hidden":false,"merged":[[0,3,0,4]]}
[]
["Option 0: Default Blank Option"]
[]
[null,null,"Type of water body","Description","TRaC water release depth (m)","Release point","Mean effluent flow rate (m3/s)","Max effluent flow rate (m3/s)","Sewer factor (%)","Substance","Release conc (ug/l)","Max release conc (ug/l)","Maximum Background conc (ug/l)","Annual Average Background conc (ug/l)","Annual EQS (ug/l)","EVF (annual)","MAC EQS (ug/l)","EVF (max)","Allowable EVF","Test 5"]
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[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL11),INDIRECT(\"F\"&Variables!BL11),INDIRECT(\"J\"&Variables!BL11))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL12),INDIRECT(\"F\"&Variables!BL12),INDIRECT(\"J\"&Variables!BL12))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL13),INDIRECT(\"F\"&Variables!BL13),INDIRECT(\"J\"&Variables!BL13))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL14),INDIRECT(\"F\"&Variables!BL14),INDIRECT(\"J\"&Variables!BL14))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL15),INDIRECT(\"F\"&Variables!BL15),INDIRECT(\"J\"&Variables!BL15))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL16),INDIRECT(\"F\"&Variables!BL16),INDIRECT(\"J\"&Variables!BL16))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL17),INDIRECT(\"F\"&Variables!BL17),INDIRECT(\"J\"&Variables!BL17))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL18),INDIRECT(\"F\"&Variables!BL18),INDIRECT(\"J\"&Variables!BL18))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL19),INDIRECT(\"F\"&Variables!BL19),INDIRECT(\"J\"&Variables!BL19))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL20),INDIRECT(\"F\"&Variables!BL20),INDIRECT(\"J\"&Variables!BL20))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL21),INDIRECT(\"F\"&Variables!BL21),INDIRECT(\"J\"&Variables!BL21))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL22),INDIRECT(\"F\"&Variables!BL22),INDIRECT(\"J\"&Variables!BL22))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL23),INDIRECT(\"F\"&Variables!BL23),INDIRECT(\"J\"&Variables!BL23))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL24),INDIRECT(\"F\"&Variables!BL24),INDIRECT(\"J\"&Variables!BL24))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL25),INDIRECT(\"F\"&Variables!BL25),INDIRECT(\"J\"&Variables!BL25))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL26),INDIRECT(\"F\"&Variables!BL26),INDIRECT(\"J\"&Variables!BL26))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL27),INDIRECT(\"F\"&Variables!BL27),INDIRECT(\"J\"&Variables!BL27))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL28),INDIRECT(\"F\"&Variables!BL28),INDIRECT(\"J\"&Variables!BL28))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL29),INDIRECT(\"F\"&Variables!BL29),INDIRECT(\"J\"&Variables!BL29))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL30),INDIRECT(\"F\"&Variables!BL30),INDIRECT(\"J\"&Variables!BL30))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL31),INDIRECT(\"F\"&Variables!BL31),INDIRECT(\"J\"&Variables!BL31))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL32),INDIRECT(\"F\"&Variables!BL32),INDIRECT(\"J\"&Variables!BL32))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL33),INDIRECT(\"F\"&Variables!BL33),INDIRECT(\"J\"&Variables!BL33))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL34),INDIRECT(\"F\"&Variables!BL34),INDIRECT(\"J\"&Variables!BL34))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL35),INDIRECT(\"F\"&Variables!BL35),INDIRECT(\"J\"&Variables!BL35))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL36),INDIRECT(\"F\"&Variables!BL36),INDIRECT(\"J\"&Variables!BL36))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL37),INDIRECT(\"F\"&Variables!BL37),INDIRECT(\"J\"&Variables!BL37))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL38),INDIRECT(\"F\"&Variables!BL38),INDIRECT(\"J\"&Variables!BL38))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL39),INDIRECT(\"F\"&Variables!BL39),INDIRECT(\"J\"&Variables!BL39))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL40),INDIRECT(\"F\"&Variables!BL40),INDIRECT(\"J\"&Variables!BL40))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL41),INDIRECT(\"F\"&Variables!BL41),INDIRECT(\"J\"&Variables!BL41))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL42),INDIRECT(\"F\"&Variables!BL42),INDIRECT(\"J\"&Variables!BL42))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL43),INDIRECT(\"F\"&Variables!BL43),INDIRECT(\"J\"&Variables!BL43))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL44),INDIRECT(\"F\"&Variables!BL44),INDIRECT(\"J\"&Variables!BL44))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL45),INDIRECT(\"F\"&Variables!BL45),INDIRECT(\"J\"&Variables!BL45))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL46),INDIRECT(\"F\"&Variables!BL46),INDIRECT(\"J\"&Variables!BL46))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL47),INDIRECT(\"F\"&Variables!BL47),INDIRECT(\"J\"&Variables!BL47))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL48),INDIRECT(\"F\"&Variables!BL48),INDIRECT(\"J\"&Variables!BL48))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL49),INDIRECT(\"F\"&Variables!BL49),INDIRECT(\"J\"&Variables!BL49))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL50),INDIRECT(\"F\"&Variables!BL50),INDIRECT(\"J\"&Variables!BL50))","v":""}]
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[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL199),INDIRECT(\"F\"&Variables!BL199),INDIRECT(\"J\"&Variables!BL199))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL200),INDIRECT(\"F\"&Variables!BL200),INDIRECT(\"J\"&Variables!BL200))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL201),INDIRECT(\"F\"&Variables!BL201),INDIRECT(\"J\"&Variables!BL201))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL202),INDIRECT(\"F\"&Variables!BL202),INDIRECT(\"J\"&Variables!BL202))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL203),INDIRECT(\"F\"&Variables!BL203),INDIRECT(\"J\"&Variables!BL203))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL204),INDIRECT(\"F\"&Variables!BL204),INDIRECT(\"J\"&Variables!BL204))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL205),INDIRECT(\"F\"&Variables!BL205),INDIRECT(\"J\"&Variables!BL205))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL206),INDIRECT(\"F\"&Variables!BL206),INDIRECT(\"J\"&Variables!BL206))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL207),INDIRECT(\"F\"&Variables!BL207),INDIRECT(\"J\"&Variables!BL207))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL208),INDIRECT(\"F\"&Variables!BL208),INDIRECT(\"J\"&Variables!BL208))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL209),INDIRECT(\"F\"&Variables!BL209),INDIRECT(\"J\"&Variables!BL209))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL210),INDIRECT(\"F\"&Variables!BL210),INDIRECT(\"J\"&Variables!BL210))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL211),INDIRECT(\"F\"&Variables!BL211),INDIRECT(\"J\"&Variables!BL211))","v":""}]
[{"$f":"CONCATENATE(INDIRECT(\"C\"&Variables!BL212),INDIRECT(\"F\"&Variables!BL212),INDIRECT(\"J\"&Variables!BL212))","v":""}]

{"sheet":"0WatoSigL","index":45,"n_rows":5,"n_cols":8,"rows_kept":5,"cut":false,"hidden":false,"merged":[[0,2,0,3]]}
[]
["Option 0: Default Blank Option"]
[]
[null,null,"Type of water body","Description","Substance","Annual rate (kg/yr)","Significant load (PHS only) kg","Significant load test"]
[null,null,null,null,null,null,{"$f":"IFERROR(VLOOKUP(Country&SigLoadTest140[[#This Row],[Substance]],SubstancesW,16,FALSE),\"\")","v":""},{"$f":"IF(ISNUMBER(SigLoadTest140[[#This Row],[Significant load (PHS only) kg]]),IF(SigLoadTest140[[#This Row],[Significant load (PHS only) kg]]>0.00000000000001,IF(SigLoadTest140[[#This Row],[Annual rate (kg/yr)]]>SigLoadTest140[[#This Row],[Significant load (PHS only) kg]],\"Fail\",\"Pass\"),\"\"),\"\")","v":""}]

{"sheet":"0Ao1","index":46,"n_rows":5,"n_cols":10,"rows_kept":5,"cut":false,"hidden":false,"merged":[[0,7,0,8]]}
[]
["Option 0: Default Blank Option"]
[]
[null,null,"Number","Substance","Long term EAL (ug/m3)","Long term PC (ug/m3)","Long term modelled PC","Short term EAL (ug/m3)","Short term PC (ug/m3)","Short term modelled PC"]
[null,null,null,null,{"$f":"IFERROR(VLOOKUP($H$1&_Air74227[[#This Row],[Substance]],SubstancesA!$A$6:$V$505,3,FALSE),\"\")","v":""},null,null,{"$f":"IFERROR(VLOOKUP($H$1&_Air74227[[#This Row],[Substance]],SubstancesA!$A$6:$V$505,4,FALSE),\"\")","v":""}]

{"sheet":"0Ao2","index":47,"n_rows":5,"n_cols":12,"rows_kept":5,"cut":false,"hidden":false,"merged":[[0,7,0,8]]}
[]
["Option 0: Default Blank Option"]
[]
[null,null,"Number","Substance","Long term EAL (ug/m3)","Long term PC (ug/m3)","%PC of EAL (long term)",">1% of EAL? (long term)","Short term EAL (ug/m3)","Short term PC (ug/m3)","%PC of EAL (short term)",">10% of EAL? (short term)"]
[null,null,null,null,{"$f":"IF(_Air7354328[[#This Row],[Substance]]<>\"\",(IFERROR(VLOOKUP(\"*\"&'Reference information'!$E$14&\"*\"&_Air7354328[[#This Row],[Substance]],SubstancesA,3,FALSE),\"\")),\"\")","v":40},null,{"$f":"IFERROR(_Air7354328[[#This Row],[Long term PC (ug/m3)]]/_Air7354328[[#This Row],[Long term EAL (ug/m3)]],\"\")","v":2.197537053333333E-2},{"$f":"IF(ISNUMBER(_Air7354328[[#This Row],[%PC of EAL (long term)]]),IF(_Air7354328[[#This Row],[%PC of EAL (long term)]]>0.01,\"fail\",\"pass\"),\"\")","v":"fail"},{"$f":"IFERROR(VLOOKUP(_Air7354328[[#This Row],[Substance]],_Air74227[[Substance]:[Short term PC (ug/m3)]],5,FALSE),\"\")","v":50},null,{"$f":"IFERROR(_Air7354328[[#This Row],[Short term PC (ug/m3)]]/_Air7354328[[#This Row],[Short term EAL (ug/m3)]],\"\")","v":1.1388587296666663},{"$f":"IF(ISNUMBER(_Air7354328[[#This Row],[%PC of EAL (short term)]]),IF(_Air7354328[[#This Row],[%PC of EAL (short term)]]>0.1,\"fail\",\"pass\"),\"\")","v":"fail"}]

{"sheet":"0Ao3","index":48,"n_rows":5,"n_cols":16,"rows_kept":5,"cut":false,"hidden":false,"merged":[[0,7,0,8]]}
[]
["Option 0: Default Blank Option"]
[]
[null,null,"Number","Substance","Long term EAL (ug/m3)","Long term PC (ug/m3)","Air Background conc (ug/m3)","%PC of headroom (long term)","PEC Long term (mg/m3)","%PEC of EAL% (Long term)","%PEC of EAL>70%? (long term)","Short term EAL (ug/m3)","Short term PC (ug/m3)","%PC of headroom (short term)"," %PC of the EAL-2*background","%PC of headroom >=20%? (short term)"]
[null,null,null,null,{"$f":"IF(_Air735364435[[#This Row],[Substance]]<>\"\",(IFERROR(VLOOKUP(\"*\"&'Reference information'!$E$14&\"*\"&_Air735364435[[#This Row],[Substance]],SubstancesA,3,FALSE),\"\")),\"\")","v":40},null,null,{"$f":"IFERROR(_Air735364435[[#This Row],[Long term PC (ug/m3)]]/(_Air735364435[[#This Row],[Long term EAL (ug/m3)]]-_Air735364435[[#This Row],[Air Background conc (ug/m3)]]),\"\")","v":3.0000505847554034E-2},{"$f":"IF(_Air735364435[[#This Row],[Substance]]<>\"\",SUM(_Air735364435[[#This Row],[Long term PC (ug/m3)]],_Air735364435[[#This Row],[Air Background conc (ug/m3)]]),\"\")","v":11.579014821333333},{"$f":"IFERROR(_Air735364435[[#This Row],[PEC Long term (µg/m3)]]/_Air735364435[[#This Row],[Long term EAL (ug/m3)]],\"\")","v":0.28947537053333333},{"$f":"IF(ISNUMBER(_Air735364435[[#This Row],[%PEC of EAL% (Long term)]]),IF(_Air735364435[[#This Row],[%PEC of EAL% (Long term)]]>=0.7,\"fail\",\"pass\"),\"\")","v":"pass"},{"$f":"IF(_Air735364435[[#This Row],[Substance]]<>\"\",(IFERROR(VLOOKUP(\"*\"&'Reference information'!$E$14&\"*\"&_Air735364435[[#This Row],[Substance]],SubstancesA,4,FALSE),\"\")),\"\")","v":50},null,{"$f":"IFERROR(_Air735364435[[#This Row],[Short term PC (ug/m3)]]/(_Air735364435[[#This Row],[Short term EAL (ug/m3)]]-(_Air735364435[[#This Row],[Air Background conc (ug/m3)]]*2)),\"\")","v":1.9910117651515147},{"$f":"IF(ISNUMBER(_Air735364435[[#This Row],[ %PC of the EAL-2*background]]),IF(_Air735364435[[#This Row],[ %PC of the EAL-2*background]]>=0.2,\"fail\",\"pass\"),\"\")","v":"fail"},{"$f":"IF(ISNUMBER(_Air7353644[[#This Row],[%PC of headroom (short term)]]),IF(_Air7353644[[#This Row],[%PC of headroom (short term)]]>=0.2,\"fail\",\"pass\"),\"\")","v":"fail"}]

{"sheet":"0Ao4","index":49,"n_rows":5,"n_cols":7,"rows_kept":5,"cut":false,"hidden":false,"merged":[[0,7,0,8]]}
[]
["Option 0: Default Blank Option"]
[]
[null,null,"Number","Substance","%PC of EAL (long term)","Insignificant?","Commentary"]
[null,null,0,null,0,{"$f":"IF(ISNUMBER(_Air735363745[[#This Row],[%PC of EAL (long term)]]),IF(_Air735363745[[#This Row],[%PC of EAL (long term)]]>0.01,\"No\",\"Yes\"),\"\")","v":"Yes"}]

{"sheet":"0Ao5","index":50,"n_rows":5,"n_cols":7,"rows_kept":5,"cut":false,"hidden":false,"merged":[[0,7,0,8]]}
[]
["Option 0: Default Blank Option"]
[]
[null,null,"Number","Substance","Annual rate (tonne/yr))","POCP value per tonne","POCP"]
[null,null,null,null,null,{"$f":"IF(ISBLANK(_Air7353637246[[#This Row],[Substance]]),\"\",IF(ISNUMBER(VLOOKUP(\"*\"&'Reference information'!$E$14&\"*\"&_Air7353637246[[#This Row],[Substance]],SubstancesA,7,FALSE)),VLOOKUP(\"*\"&'Reference information'!$E$14&\"*\"&_Air7353637246[[#This Row],[Substance]],SubstancesA,7,FALSE),\"No POCP value\"))","v":""},{"$f":"IF(ISNUMBER(_Air7353637246[[#This Row],[POCP value per tonne]]),_Air7353637246[[#This Row],[Annual rate (tonne/yr))]]*_Air7353637246[[#This Row],[POCP value per tonne]],\"\")","v":""}]

{"sheet":"0AWato1","index":51,"n_rows":261,"n_cols":19,"rows_kept":261,"cut":false,"hidden":false,"merged":[[0,7,0,8]]}
[]
["Option 0: Default Blank Option"]
[]
[null,null,"Sector","Air/Water?","Release point code","Substance","Long term conc (ug/l)","Short term conc (ug/l)","Product / sub-sector","Sub-Product / sub sub-sector","Plant type","Plant age","Fuel type","Plant capacity","Emission Source","BAT","BAT-AEL units","BAT-AEL lower value","BAT-AEL upper value"]
[1]
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{"sheet":"0PIo","index":52,"n_rows":31,"n_cols":13,"rows_kept":31,"cut":false,"hidden":false,"merged":[[6,5,6,12]]}
[]
["Option 0: Default Blank Option"]
[]
[]
[]
[]
[]
[]
[]
[]
[null,"Basic consumption data:",null,null,null,null,null,null,{"$f":"\"Specific combustion per \"&F14&\" of \"&F16&\":\"","v":"Specific combustion per  of :"}]
[]
[null,null,null,"Name","Annual quantity","Units"]
[null,"Amount of product:",null,null,null,null,null,null,"Production efficiency:",{"$f":"IFERROR(E14/E16,\"\")","v":""},{"$f":"F14&\"/\"&F16","v":"/"}]
[]
[null,"Main raw material:",null,null,{"$f":"IFERROR(VLOOKUP($D16,#REF!,2,FALSE),\"\")","v":""},{"$f":"IFERROR(VLOOKUP($D16,#REF!,3,FALSE),\"\")","v":""}]
[]
[null,{"$f":"IF($F$5=\"Intermediate\",\"Intermediate:\",\"\")","v":""}]
[]
[null,"Potable water",null,null,{"$f":"IFERROR(VLOOKUP($B20,'0Ri'!$C$8:$E$100,2,FALSE),\"\")","v":0},"m3",null,null,"Potable water:",null,null,{"$f":"IFERROR(IF($F$5=\"Product\",E20/$E$14,IF($F$5=\"Raw material\",E20/$E$16,IF($F$5=\"Intermediate\",E20/$E$18,\"\"))),\"\")","v":""},"m3"]
[]
[null,"Non-potable water",null,null,{"$f":"IFERROR(VLOOKUP($B22,'0Ri'!$C$8:$E$100,2,FALSE),\"\")","v":0},"m3",null,null,"Non-potable water:",null,null,{"$f":"IFERROR(IF($F$5=\"Product\",E22/$E$14,IF($F$5=\"Raw material\",E22/$E$16,IF($F$5=\"Intermediate\",E22/$E$18,\"\"))),\"\")","v":""},"m3"]
[]
[null,"Energy:",null,null,{"$f":"IFERROR(SUM('0Ei'!$E$8:$E$100),\"\")","v":0},"MWh",null,null,"Energy:",null,null,{"$f":"IFERROR(IF($F$5=\"Product\",E24/$E$14,IF($F$5=\"Raw material\",E24/$E$16,IF($F$5=\"Intermediate\",E24/$E$18,\"\"))),\"\")","v":""},"MWh"]
[]
[null,"Waste:",null,null,null,null,null,null,"Waste:"]
[null,null,"Hazardous",null,{"$f":"SUMIF('0Wastei'!$D$8:$D$100,$C27,'0Wastei'!$E$8:$E$100)","v":0},"tonne",null,null,null,"Hazardous",null,{"$f":"IFERROR(IF($F$5=\"Product\",E27/$E$14,IF($F$5=\"Raw material\",E27/$E$16,IF($F$5=\"Intermediate\",E27/$E$18,\"\"))),\"\")","v":""},"tonne"]
[null,null,"Stable non-reactive hazardous waste",null,{"$f":"SUMIF('0Wastei'!$D$8:$D$100,$C28,'0Wastei'!$E$8:$E$100)","v":0},"tonne",null,null,null,"Stable non-reactive hazardous waste",null,{"$f":"IFERROR(IF($F$5=\"Product\",E28/$E$14,IF($F$5=\"Raw material\",E28/$E$16,IF($F$5=\"Intermediate\",E28/$E$18,\"\"))),\"\")","v":""},"tonne"]
[null,null,"Biodegradable non-hazardous waste",null,{"$f":"SUMIF('0Wastei'!$D$8:$D$100,$C29,'0Wastei'!$E$8:$E$100)","v":0},"tonne",null,null,null,"Biodegradable non-hazardous waste",null,{"$f":"IFERROR(IF($F$5=\"Product\",E29/$E$14,IF($F$5=\"Raw material\",E29/$E$16,IF($F$5=\"Intermediate\",E29/$E$18,\"\"))),\"\")","v":""},"tonne"]
[null,null,"Other non-hazardous",null,{"$f":"SUMIF('0Wastei'!$D$8:$D$100,$C30,'0Wastei'!$E$8:$E$100)","v":0},"tonne",null,null,null,"Other non-hazardous",null,{"$f":"IFERROR(IF($F$5=\"Product\",E30/$E$14,IF($F$5=\"Raw material\",E30/$E$16,IF($F$5=\"Intermediate\",E30/$E$18,\"\"))),\"\")","v":""},"tonne"]
[null,null,"Inert",null,{"$f":"SUMIF('0Wastei'!$D$8:$D$100,$C31,'0Wastei'!$E$8:$E$100)","v":0},"tonne",null,null,null,"Inert",null,{"$f":"IFERROR(IF($F$5=\"Product\",E31/$E$14,IF($F$5=\"Raw material\",E31/$E$16,IF($F$5=\"Intermediate\",E31/$E$18,\"\"))),\"\")","v":""},"tonne"]

{"sheet":"0Eo","index":53,"n_rows":14,"n_cols":9,"rows_kept":14,"cut":false,"hidden":false,"merged":[[0,3,0,4]]}
[]
["Option 0: Default Blank Option"]
[]
[]
[]
[]
[null,null,null,null,"Energy","Source","Annual rate (MWh/yr)","GWP value","Annual GWP"]
[null,null,null,null,"Direct (CO2)","Direct emissions",{"$f":"IFERROR(SUMIF('0Ei'!$D$8:$D$100,$F8,'0Ei'!$E$8:$E$100),\"\")","v":0},1,{"$f":"IFERROR(SUMIF('0Ei'!$D$8:$D$100,$F8,'0Ei'!$K$8:$K$100),\"\")","v":0}]
[]
[null,null,null,null,"Indirect (CO2)","Indirect emissions",{"$f":"IFERROR(SUMIF('0Ei'!$D$8:$D$100,$F10,'0Ei'!$E$8:$E$100),\"\")","v":0},1,{"$f":"IFERROR(SUMIF('0Ei'!$D$8:$D$100,$F10,'0Ei'!$K$8:$K$100),\"\")","v":0}]
[]
[]
[]
[null,null,null,null,null,null,null,"Total",{"$f":"SUM(I8,I10)","v":0}]

{"sheet":"0Wasteo","index":54,"n_rows":47,"n_cols":13,"rows_kept":47,"cut":false,"hidden":false,"merged":[[0,3,0,4]]}
[]
["Option 0: Default Blank Option"]
[]
[]
[]
[]
[null,null,null,null,"Number","Mass","Waste stream","Final treatment/disposal method","Score","Waste type","Score",null,"Impact score"]
[null,null,null,null,{"$f":"IF(ISBLANK('0Wastei'!B8),\"\",'0Wastei'!B8)","v":1},{"$f":"IF(ISNUMBER($E8),IFERROR(VLOOKUP($E8,'1Wastei'!$B$9:$F$23,4,FALSE),\"\"))","v":""},{"$f":"IF(ISNUMBER($E8),IFERROR(VLOOKUP($E8,'1Wastei'!$B$9:$F$23,2,FALSE),\"\"))","v":""},{"$f":"IF(ISNUMBER($E8),IFERROR(VLOOKUP($E8,'1Wastei'!$B$9:$F$23,5,FALSE),\"\"))","v":""},{"$f":"IFERROR(VLOOKUP(H8,Variables!$AU$3:$AV$14,2,FALSE),\"\")","v":""},{"$f":"IF(ISNUMBER($E8),IFERROR(VLOOKUP($E8,'1Wastei'!$B$9:$F$23,3,FALSE),\"\"))","v":""},{"$f":"IFERROR(VLOOKUP(J8,Variables!$AQ$3:$AR$7,2,FALSE),\"\")","v":""},null,{"$f":"IFERROR(F8*I8*K8,\"\")","v":""}]
[]
[null,null,null,null,{"$f":"IF(ISBLANK('0Wastei'!B9),\"\",'0Wastei'!B9)","v":2},{"$f":"IF(ISNUMBER($E10),IFERROR(VLOOKUP($E10,'1Wastei'!$B$9:$F$23,4,FALSE),\"\"))","v":""},{"$f":"IF(ISNUMBER($E10),IFERROR(VLOOKUP($E10,'1Wastei'!$B$9:$F$23,2,FALSE),\"\"))","v":""},{"$f":"IF(ISNUMBER($E10),IFERROR(VLOOKUP($E10,'1Wastei'!$B$9:$F$23,5,FALSE),\"\"))","v":""},{"$f":"IFERROR(VLOOKUP(H10,Variables!$AU$3:$AV$14,2,FALSE),\"\")","v":""},{"$f":"IF(ISNUMBER($E10),IFERROR(VLOOKUP($E10,'1Wastei'!$B$9:$F$23,3,FALSE),\"\"))","v":""},{"$f":"IFERROR(VLOOKUP(J10,Variables!$AQ$3:$AR$7,2,FALSE),\"\")","v":""},null,{"$f":"IFERROR(F10*I10*K10,\"\")","v":""}]
[]
[null,null,null,null,3,{"$f":"IF(ISNUMBER($E12),IFERROR(VLOOKUP($E12,'0Wastei'!$B$8:$F$26,4,FALSE),\"\"))","v":""},{"$f":"IF(ISNUMBER($E12),IFERROR(VLOOKUP($E12,'0Wastei'!$B$8:$F$26,2,FALSE),\"\"))","v":""},{"$f":"IF(ISNUMBER($E12),IFERROR(VLOOKUP($E12,'0Wastei'!$B$8:$F$26,5,FALSE),\"\"))","v":""},{"$f":"IFERROR(VLOOKUP(H12,Variables!$AU$3:$AV$14,2,FALSE),\"\")","v":""},{"$f":"IF(ISNUMBER($E12),IFERROR(VLOOKUP($E12,'0Wastei'!$B$8:$F$26,3,FALSE),\"\"))","v":""},{"$f":"IFERROR(VLOOKUP(J12,Variables!$AQ$3:$AR$7,2,FALSE),\"\")","v":""},null,{"$f":"IFERROR(F12*I12*K12,\"\")","v":""}]
[]
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[]
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{"sheet":"0Visual","index":55,"n_rows":17,"n_cols":6,"rows_kept":17,"cut":false,"hidden":false,"merged":[[18,2,22,5]]}
[]
["Option 0: Default Blank Option"]
[]
[]
[]
[null,null,"Can ANY of the options generate a visible plume?",null,null,{"$f":"IF(E6=\"No\",\"Move on to the next page\",\"\")","v":""}]
[]
[null,null,"Can any of the release points generate a Visible Plume"]
[]
[null,null,"For what percentage of daylight hours per year does the"]
[null,null,"plume extend beyond the facility boundary?",null,null,{"$f":"IF(E8=\"No\",\"You selected that none of the release points generates a visible plume\",\"\")","v":""}]
[]
[null,null,"Refer to the guidance in Annex A and assign a level of",null,{"$f":"IFERROR(VLOOKUP($E$11,Variables!$BP$3:$BQ$6,2,FALSE),\"\")","v":""}]
[null,null,"significance"]
[]
[]
[null,null,"Provide any supporting evidence below"]

{"sheet":"SEARCH","index":56,"n_rows":33,"n_cols":8,"rows_kept":33,"cut":false,"hidden":false,"merged":[]}
[]
[null,null,null,"Row"]
[null,null,null,1]
[]
[null,null,"Sector"]
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[]
[null,null,"Product / Sub-sector"]
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[]
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[null,null,null,null,null,null,"1:Basecase","Option"]
[null,null,"Plant type"]
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[]
[null,null,"Plant age"]
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[]
[null,null,"Plant capacity"]
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[]
[null,null,"Fuel type"]
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[]
[null,null,"Emission source"]
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[]
[null,null,"Release type"]
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[]
[null,null,"Pollutant"]
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{"sheet":"Stackdispersions","index":57,"n_rows":2006,"n_cols":14,"rows_kept":2006,"cut":false,"hidden":false,"merged":[]}
[]
[]
[]
[null,1,{"$f":"B4+1","v":2},{"$f":"C4+1","v":3},{"$f":"D4+1","v":4},null,null,null,null,null,"Original table"]
[null,"Min Stack Height","Long Term","Short Term","Monthly",null,null,null,null,null,"Min Stack Height","Long Term","Short Term","Monthly"]
[null,0,148,3900,529,null,null,null,null,null,0,148,3900,529]
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[null,0.2,{"$f":"C7+(($C$106-$C$6)/COUNT($B$7:$B$106))","v":145.68},{"$f":"D7+(($D$106-$D$6)/COUNT($B$7:$B$106))","v":3833.6000000000004},{"$f":"E7+(($E$106-$E$6)/COUNT($B$7:$B$106))","v":519.09400000000005},null,null,null,null,null,20,4.5999999999999996,161,6.2]
[null,0.3,144.52000000000001,3800.4000000000005,514.14100000000008,null,null,null,null,null,30,1.7,77,2.2999999999999998]
[null,0.4,143.36000000000001,3767.2000000000007,509.1880000000001,null,null,null,null,null,50,0.52,31,0.68]
[null,0.5,142.20000000000002,3734.0000000000009,504.23500000000013,null,null,null,null,null,70,0.24,16,0.31]
[null,0.6,141.04000000000002,3700.8000000000011,499.28200000000015,null,null,null,null,null,100,0.11,8.6,0.13]
[null,0.7,139.88000000000002,3667.6000000000013,494.32900000000018,null,null,null,null,null,150,4.8000000000000001E-2,4,5.1999999999999998E-2]
[null,0.8,138.72000000000003,3634.4000000000015,489.3760000000002,null,null,null,null,null,200,2.3E-2,2.2999999999999998,2.5999999999999999E-2]
[null,0.9,137.56000000000003,3601.2000000000016,484.42300000000023]
[null,1,136.40000000000003,3568.0000000000018,479.47000000000025]
[null,1.1000000000000001,135.24000000000004,3534.800000000002,474.51700000000028]
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[null,1.3,132.92000000000004,3468.4000000000024,464.61100000000033]
[null,1.4,131.76000000000005,3435.2000000000025,459.65800000000036]
[null,1.5,130.60000000000005,3402.0000000000027,454.70500000000038]
[null,1.6,129.44000000000005,3368.8000000000029,449.75200000000041]
[null,1.7,128.28000000000006,3335.6000000000031,444.79900000000043]
[null,1.8,127.12000000000006,3302.4000000000033,439.84600000000046]
[null,1.9,125.96000000000006,3269.2000000000035,434.89300000000048]
[null,2,124.80000000000007,3236.0000000000036,429.94000000000051]
[null,2.1,123.64000000000007,3202.8000000000038,424.98700000000053]
[null,2.2000000000000002,122.48000000000008,3169.600000000004,420.03400000000056]
[null,2.2999999999999998,121.32000000000008,3136.4000000000042,415.08100000000059]
[null,2.4,120.16000000000008,3103.2000000000044,410.12800000000061]
[null,2.5,119.00000000000009,3070.0000000000045,405.17500000000064]
[null,2.6,117.84000000000009,3036.8000000000047,400.22200000000066]
[null,2.7,116.68000000000009,3003.6000000000049,395.26900000000069]
[null,2.8,115.5200000000001,2970.4000000000051,390.31600000000071]
[null,2.9,114.3600000000001,2937.2000000000053,385.36300000000074]
[null,3,113.2000000000001,2904.0000000000055,380.41000000000076]
[null,3.1,112.04000000000011,2870.8000000000056,375.45700000000079]
[null,3.2,110.88000000000011,2837.6000000000058,370.50400000000081]
[null,3.3,109.72000000000011,2804.400000000006,365.55100000000084]
[null,3.4,108.56000000000012,2771.2000000000062,360.59800000000087]
[null,3.5,107.40000000000012,2738.0000000000064,355.64500000000089]
[null,3.6,106.24000000000012,2704.8000000000065,350.69200000000092]
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[]
[]
[]
[]
[]
["ID","Sector","IED Annex I Activity Category","IED Annex I Activity","Product / sub-sector","Sub-Product / sub-sub-sector","Plant type","Plant age","Fuel type","Plant capacity","Emission Source","Release type","Release type converted","Pollutant","Pollutant converted","BAT","BAT-AEL units","BAT-AEL lower value","BAT-AEL upper value","Colour","Monitoring","Reference temperature (K)","Reference Pressure (kPa)","Reference O2 content (% waste gas volume)","Averaging period","Notes","Source (BATC)","Source (Section)","Source (BATC page number)","Source (pdf page number)"]
[320,"Cement, lime and MgO","3. Mineral Industry ","3.1. Installations for the production of cement clinker in rotary kilns with a production capacity exceeding 500t/day or lime in rotary kilns with a production capacity exceeding 50t/day or in other furnaces with a production capacity exceeding 50t/day.","Lime","Unspecified","PFRK, OSK, LRK, PRK","Unspecified","Unspecified","Unspecified","Kiln firing process","Emissions to air","Air","Carbon monoxide, expressed as CO ","Carbon monoxide, expressed as CO ","In order to reduce the emissions of CO from the flue-gases of kiln firing processes, BAT is to use one or a combination of the following techniques: (i) Selecting, raw materials with a low content of organic matter; (ii) Using process optimisation techniques to achieve a stable and complete combustion","mg/Nm3","N/A","500","Green","Continuous",0,0,0.11,"daily average value or average over the sampling period (spot measurements for at least half an hour)","Emissions can be higher depending on raw materials used and/or type of lime produced, e.g. hydraulic lime.\n\nBAT-AEL does not apply to MFSK and ASK","CLM (2013)\n2013/163/EU","1.3.7.4.1",31,31]
[332,"Cement, lime and MgO","3. Mineral Industry ","3.1. Installations for the production of cement clinker in rotary kilns with a production capacity exceeding 500t/day or lime in rotary kilns with a production capacity exceeding 50t/day or in other furnaces with a production capacity exceeding 50t/day.","Magnesium oxide","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Kiln firing process","Emissions to air","Air","Carbon monoxide, expressed as CO ","Carbon monoxide, expressed as CO ","In order to reduce the emissions of CO from the flue-gases of kiln firing processes, BAT is to use a combination of the following techniques: (i) Selecting raw materials with a low content of organic matter; (ii) Process control optimisation; (iii) Feeding fuels controlled, constantly and continuously","mg/Nm3",50,"1000","Green","Continuous",0,0,0.1,"Daily",0,"CLM (2013)\n2013/163/EU","1.4.4.3",38,38]
[300,"Cement, lime and MgO","3. Mineral Industry ","3.1. Installations for the production of cement clinker in rotary kilns with a production capacity exceeding 500t/day or lime in rotary kilns with a production capacity exceeding 50t/day or in other furnaces with a production capacity exceeding 50t/day.","Cement","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Chanelled dust emissions from dusty oeprations","Emissions to air","Air","Dust ","Particulates (PM10) (24 hr Mean)","In order to reduce channelled dust emissions, BAT is to apply a maintenance management system which especially addresses the performance of filters applied to dusty operations, other than those from kiln firing, cooling and main milling processes. Taking this management system into account, BAT is to use dry flue-gas cleaning with a filter.","mg/Nm3","N/A",10,"Green","Continuous",0,0,"N/A","Daily","It should be noted that for small sources (< 10 000 Nm 3 /h) a priority approach, based on the maintenance management system, regarding the frequency for checking the performance of the filter has to be taken into account","CLM (2013)\n2013/163/EU","1.2.5.2",16,16]
[302,"Cement, lime and MgO","3. Mineral Industry ","3.1. Installations for the production of cement clinker in rotary kilns with a production capacity exceeding 500t/day or lime in rotary kilns with a production capacity exceeding 50t/day or in other furnaces with a production capacity exceeding 50t/day.","Cement","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Cooling and milling processes","Emissions to air","Air","Dust ","Particulates (PM10) (24 hr Mean)","In order to reduce dust emissions from the flue-gases of cooling and milling processes, BAT is to use dry flue-gas cleaning with a filter","mg/Nm3",10,"20","Green","Continuous",0,0,"N/A","Daily ","When applying fabric filters or new or upgraded ESPs, the lower level is achieved.","CLM (2013)\n2013/163/EU","1.2.5.4",17,17]
[301,"Cement, lime and MgO","3. Mineral Industry ","3.1. Installations for the production of cement clinker in rotary kilns with a production capacity exceeding 500t/day or lime in rotary kilns with a production capacity exceeding 50t/day or in other furnaces with a production capacity exceeding 50t/day.","Cement","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Kiln firing process","Emissions to air","Air","Dust ","Particulates (PM10) (24 hr Mean)","In order to reduce dust emissions from flue-gases of kiln firing processes, BAT is to use dry flue-gas cleaning with a filter.","mg/Nm3",10,"20","Green","Continuous",0,0,0.1,"Daily ",0,"CLM (2013)\n2013/163/EU","1.2.5.3",16,16]
[315,"Cement, lime and MgO","3. Mineral Industry ","3.1. Installations for the production of cement clinker in rotary kilns with a production capacity exceeding 500t/day or lime in rotary kilns with a production capacity exceeding 50t/day or in other furnaces with a production capacity exceeding 50t/day.","Lime","Unspecified","ESP or other filters","Unspecified","Unspecified","Unspecified","Kiln firing process","Emissions to air","Air","Dust ","Particulates (PM10) (24 hr Mean)","In order to reduce dust emissions from the flue-gases of kiln firing processes, BAT is to use flue-gas cleaning with a filter. One or a combination of the following techniques can be used: (i) ESP; (ii) Fabric filter; (iii) Wet dust separator; (iv) Centrifugal separator/cyclone","mg/Nm3","N/A","20","Green","Continuous",0,0,0.11,"daily average value or average over the sampling period (spot measurements for at least half an hour)","In exceptional cases where the resistivity of dust is high, the BAT-AEL could be higher, up to 30 mg/Nm 3 , as the daily average value.","CLM (2013)\n2013/163/EU","1.3.6.3",28,28]
[312,"Cement, lime and MgO","3. Mineral Industry ","3.1. Installations for the production of cement clinker in rotary kilns with a production capacity exceeding 500t/day or lime in rotary kilns with a production capacity exceeding 50t/day or in other furnaces with a production capacity exceeding 50t/day.","Lime","Unspecified","Fabric filter","Unspecified","Unspecified","Unspecified","Chanelled dust emissions from dusty oeprations","Emissions to air","Air","Dust ","Particulates (PM10) (24 hr Mean)","In order to reduce channelled dust emissions from dusty operations other than those from kiln firing processes, BAT is to use one of the following techniques and to use a maintenance management system which specifically addresses the performance of filters: (i) Fabric filter; (ii) Wet scrubbers","mg/Nm3","N/A","10","Green","Continuous",0,0,"N/A","daily average or average over the sampling period (spot measurements for at least half an hour)","daily average or average over the sampling period (spot measurements for at least half an hour)","CLM (2013)\n2013/163/EU","1.3.6.2",28,28]
[314,"Cement, lime and MgO","3. Mineral Industry ","3.1. Installations for the production of cement clinker in rotary kilns with a production capacity exceeding 500t/day or lime in rotary kilns with a production capacity exceeding 50t/day or in other furnaces with a production capacity exceeding 50t/day.","Lime","Unspecified","Fabric filter","Unspecified","Unspecified","Unspecified","Kiln firing process","Emissions to air","Air","Dust ","Particulates (PM10) (24 hr Mean)","In order to reduce dust emissions from the flue-gases of kiln firing processes, BAT is to use flue-gas cleaning with a filter. One or a combination of the following techniques can be used: (i) ESP; (ii) Fabric filter; (iii) Wet dust separator; (iv) Centrifugal separator/cyclone","mg/Nm3","N/A","10","Green","Continuous",0,0,0.11,"daily average value or average over the sampling period (spot measurements for at least half an hour)",0,"CLM (2013)\n2013/163/EU","1.3.6.3",28,28]
[313,"Cement, lime and MgO","3. Mineral Industry ","3.1. Installations for the production of cement clinker in rotary kilns with a production capacity exceeding 500t/day or lime in rotary kilns with a production capacity exceeding 50t/day or in other furnaces with a production capacity exceeding 50t/day.","Lime","Unspecified","Wet scrubber","Unspecified","Unspecified","Unspecified","Chanelled dust emissions from dusty oeprations","Emissions to air","Air","Dust ","Particulates (PM10) (24 hr Mean)","In order to reduce channelled dust emissions from dusty operations other than those from kiln firing processes, BAT is to use one of the following techniques and to use a maintenance management system which specifically addresses the performance of filters: (i) Fabric filter; (ii) Wet scrubbers","mg/Nm3","N/A","10","Green","Continuous",0,0,"N/A","daily average or average over the sampling period (spot measurements for at least half an hour)","daily average or average over the sampling period (spot measurements for at least half an hour)","CLM (2013)\n2013/163/EU","1.3.6.2",28,28]
[329,"Cement, lime and MgO","3. Mineral Industry ","3.1. Installations for the production of cement clinker in rotary kilns with a production capacity exceeding 500t/day or lime in rotary kilns with a production capacity exceeding 50t/day or in other furnaces with a production capacity exceeding 50t/day.","Magnesium oxide","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Chanelled dust emissions from dusty oeprations","Emissions to air","Air","Dust ","Particulates (PM10) (24 hr Mean)","In order to reduce channelled dust emissions from dusty operations other than those from kiln firing processes, BAT is to use flue-gas cleaning with a filter by applying one or a combination of the following techniques, and to use a maintenance management system which specifically addresses the performance of techniques: (i) Fabric filters; (ii) Centrifugal separators/ cyclones; (iii) Wet dust separators","mg/Nm3","N/A","10","Green","Continuous",0,0,"N/A","Daily","It should be noted that for small sources (< 10 000 Nm 3 /h) a priority approach, based on a maintenance management system regarding the frequency for checking the performance of the filter has to be taken into account","CLM (2013)\n2013/163/EU","1.4.3.2",36,36]
[330,"Cement, lime and MgO","3. Mineral Industry ","3.1. Installations for the production of cement clinker in rotary kilns with a production capacity exceeding 500t/day or lime in rotary kilns with a production capacity exceeding 50t/day or in other furnaces with a production capacity exceeding 50t/day.","Magnesium oxide","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Kiln firing process","Emissions to air","Air","Dust ","Particulates (PM10) (24 hr Mean)","In order to reduce dust emissions from the flue-gases of kiln firing processes, BAT is to use flue-gas cleaning with a filter by applying one or a combination of the following techniques: (i) Electrostatic precipitators (ESPs); (ii) Fabric filters; (iii) Centrifugal separators/ cyclones; (iv) Wet dust separators","mg/Nm3",20,"35","Green","Continuous",0,0,0.1,"Daily",0,"CLM (2013)\n2013/163/EU","1.4.3.3",37,37]
[309,"Cement, lime and MgO","3. Mineral Industry ","3.1. Installations for the production of cement clinker in rotary kilns with a production capacity exceeding 500t/day or lime in rotary kilns with a production capacity exceeding 50t/day or in other furnaces with a production capacity exceeding 50t/day.","Cement","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Kiln firing process","Emissions to air","Air","Hg","Mercury and compounds, except mercury alkyls, (as","In order to minimise the emissions of metals from the flue-gases of the kiln firing processes, BAT is to use one or a combination of the following techniques: (i) Selecting materials with a low content of relevant metals and limiting the content of relevant metals in materials, especially mercury; (ii) Using a quality assurance system to guarantee the characteristics of the waste materials used; (iii) Using effective dust removal techniques as set out in BAT 17","mg/Nm3","N/A","0.05","Green","Periodic",0,0,0.1,"average over the sampling period (spot measurements, for at least half an hour)","Low levels have been reported based on the quality of the raw materials and the fuels. Values higher than 0,03 mg/Nm 3 have to be further investigated. Values close to 0,05 mg/Nm 3 require consideration of additional techniques (e.g. lowering of the flue-gas temperature, activated carbon).","CLM (2013)\n2013/163/EU","1.2.8",28,28]
[326,"Cement, lime and MgO","3. Mineral Industry ","3.1. Installations for the production of cement clinker in rotary kilns with a production capacity exceeding 500t/day or lime in rotary kilns with a production capacity exceeding 50t/day or in other furnaces with a production capacity exceeding 50t/day.","Lime","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Kiln firing process","Emissions to air","Air","Hg","Mercury and compounds, except mercury alkyls, (as","In order to minimise the emissions of metals from the flue-gases of kiln firing processes, BAT is to use one or a combination of the following techniques: (i) Selecting fuels with a low content of metals; (ii) Using a quality assurance system to guarantee the characteristics of the waste fuels used; (iii) Limiting the content of relevant metals in materials, especially mercury; (iv) Using one or a combination of dust removal techniques as set out in BAT 43","mg/Nm3","N/A","0.05","Green","Periodic",0,0,0.11,"average over the sampling period (spot measurements for at least half an hour)",0,"CLM (2013)\n2013/163/EU","1.3.9",34,34]
[307,"Cement, lime and MgO","3. Mineral Industry ","3.1. Installations for the production of cement clinker in rotary kilns with a production capacity exceeding 500t/day or lime in rotary kilns with a production capacity exceeding 50t/day or in other furnaces with a production capacity exceeding 50t/day.","Cement","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Kiln firing process","Emissions to air","Air","Hydrogen chloride, expressed as HCl","Hydrogen chloride, expressed as HCl","In order prevent/reduce the emissions of HCl from flue-gases of the kiln firing processes, BAT is to use one or a combination of the following primary techniques: (i) Using raw materials and fuels with a low chlorine content; (ii) Limiting the amount of chlorine content for any waste that is to be used as raw material and/or fuel in a cement kiln","mg/Nm3","N/A","10","Green","Continuous",0,0,0.1,"Daily",0,"CLM (2013)\n2013/163/EU","1.2.6.4",20,20]
[323,"Cement, lime and MgO","3. Mineral Industry ","3.1. Installations for the production of cement clinker in rotary kilns with a production capacity exceeding 500t/day or lime in rotary kilns with a production capacity exceeding 50t/day or in other furnaces with a production capacity exceeding 50t/day.","Lime","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Kiln firing process","Emissions to air","Air","Hydrogen chloride, expressed as HCl","Hydrogen chloride, expressed as HCl","In order to reduce the emissions of HCl and the emissions of HF from the flue-gas of kiln firing processes, when using waste, BAT is to use the following primary techniques: (i) Using conventional fuels with a low chlorine and fluorine content; (ii) Limiting the amount of chlorine and fluorine content for any waste that is to be used as fuel in a lime kiln","mg/Nm3","N/A","10","Green","Continuous",0,0,0.11,0,0,"CLM (2013)\n2013/163/EU","1.3.7.6",33,33]
[324,"Cement, lime and MgO","3. Mineral Industry ","3.1. Installations for the production of cement clinker in rotary kilns with a production capacity exceeding 500t/day or lime in rotary kilns with a production capacity exceeding 50t/day or in other furnaces with a production capacity exceeding 50t/day.","Lime","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Kiln firing process","Emissions to air","Air","Hydrogen flouride, expressed as HF","Hydrogen flouride, expressed as HF","In order to reduce the emissions of HCl and the emissions of HF from the flue-gas of kiln firing processes, when using waste, BAT is to use the following primary techniques: (i) Using conventional fuels with a low chlorine and fluorine content; (ii) Limiting the amount of chlorine and fluorine content for any waste that is to be used as fuel in a lime kiln","mg/Nm3","N/A","1","Green","Continuous",0,0,0.11,"daily average value or the average value over the sampling period (spot measurements, for at least half an hour",0,"CLM (2013)\n2013/163/EU","1.3.7.6",33,33]
[310,"Cement, lime and MgO","3. Mineral Industry ","3.1. Installations for the production of cement clinker in rotary kilns with a production capacity exceeding 500t/day or lime in rotary kilns with a production capacity exceeding 50t/day or in other furnaces with a production capacity exceeding 50t/day.","Cement","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Kiln firing process","Emissions to air","Air","Metals (Cd, Tl) ","Metals (Cd, Tl) ","In order to minimise the emissions of metals from the flue-gases of the kiln firing processes, BAT is to use one or a combination of the following techniques: (i) Selecting materials with a low content of relevant metals and limiting the content of relevant metals in materials, especially mercury; (ii) Using a quality assurance system to guarantee the characteristics of the waste materials used; (iii) Using effective dust removal techniques as set out in BAT 17","mg/Nm3","N/A","0.05","Green","Periodic",0,0,0.1,"average over the sampling period (spot measurements, for at least half an hour)","Low levels have been reported based on the quality of the raw materials and the fuels.","CLM (2013)\n2013/163/EU","1.2.8",28,28]
[327,"Cement, lime and MgO","3. Mineral Industry ","3.1. Installations for the production of cement clinker in rotary kilns with a production capacity exceeding 500t/day or lime in rotary kilns with a production capacity exceeding 50t/day or in other furnaces with a production capacity exceeding 50t/day.","Lime","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Kiln firing process","Emissions to air","Air","Metals (Cd, Tl) ","Metals (Cd, Tl) ","In order to minimise the emissions of metals from the flue-gases of kiln firing processes, BAT is to use one or a combination of the following techniques: (i) Selecting fuels with a low content of metals; (ii) Using a quality assurance system to guarantee the characteristics of the waste fuels used; (iii) Limiting the content of relevant metals in materials, especially mercury; (iv) Using one or a combination of dust removal techniques as set out in BAT 43","mg/Nm3","N/A","0.05","Green","Periodic",0,0,0.11,"average over the sampling period (spot measurements for at least half an hour)",0,"CLM (2013)\n2013/163/EU","1.3.9",34,34]
[311,"Cement, lime and MgO","3. Mineral Industry ","3.1. Installations for the production of cement clinker in rotary kilns with a production capacity exceeding 500t/day or lime in rotary kilns with a production capacity exceeding 50t/day or in other furnaces with a production capacity exceeding 50t/day.","Cement","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Kiln firing process","Emissions to air","Air","Metals( As, Sb, Pb, Cr, Co, Cu, Mn, Ni, V)","Metals( As, Sb, Pb, Cr, Co, Cu, Mn, Ni, V)","In order to minimise the emissions of metals from the flue-gases of the kiln firing processes, BAT is to use one or a combination of the following techniques: (i) Selecting materials with a low content of relevant metals and limiting the content of relevant metals in materials, especially mercury; (ii) Using a quality assurance system to guarantee the characteristics of the waste materials used; (iii) Using effective dust removal techniques as set out in BAT 17","mg/Nm3","N/A","0.5","Green","Periodic",0,0,0.1,"average over the sampling period (spot measurements, for at least half an hour)","Low levels have been reported based on the quality of the raw materials and the fuels.","CLM (2013)\n2013/163/EU","1.2.8",28,28]
[328,"Cement, lime and MgO","3. Mineral Industry ","3.1. Installations for the production of cement clinker in rotary kilns with a production capacity exceeding 500t/day or lime in rotary kilns with a production capacity exceeding 50t/day or in other furnaces with a production capacity exceeding 50t/day.","Lime","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Kiln firing process","Emissions to air","Air","Metals( As, Sb, Pb, Cr, Co, Cu, Mn, Ni, V)","Metals( As, Sb, Pb, Cr, Co, Cu, Mn, Ni, V)","In order to minimise the emissions of metals from the flue-gases of kiln firing processes, BAT is to use one or a combination of the following techniques: (i) Selecting fuels with a low content of metals; (ii) Using a quality assurance system to guarantee the characteristics of the waste fuels used; (iii) Limiting the content of relevant metals in materials, especially mercury; (iv) Using one or a combination of dust removal techniques as set out in BAT 43","mg/Nm3","N/A","0.5","Green","Periodic",0,0,0.11,"average over the sampling period (spot measurements for at least half an hour)",0,"CLM (2013)\n2013/163/EU","1.3.9",34,34]
[305,"Cement, lime and MgO","3. Mineral Industry ","3.1. Installations for the production of cement clinker in rotary kilns with a production capacity exceeding 500t/day or lime in rotary kilns with a production capacity exceeding 50t/day or in other furnaces with a production capacity exceeding 50t/day.","Cement","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Emissions to air","Air","NH3 slip ","NH3 slip ","When SNCR is used, BAT is to achieve efficient NO x reduction, while keeping the ammonia slip as low as possible, by using the following technique: (i) To apply an appropriate and sufficient NO x reduction efficiency along with a stable operating process; (ii) To apply a good stoichiometric distribution of ammonia in order to achieve the highest efficiency of NO x reduction and to reduce the NH 3 slip; (iii) To keep the emissions of NH 3 slip (due to unreacted ammonia) from the flue-gases as low as possible taking into account the correlation between the NO x abatement efficiency and the NH 3 slip","mg/Nm3",30,"50","Green","Continuous",0,0,"Unspecified","Daily ","The ammonia slip depends on the initial NO x level and on the NO x abatement efficiency. For Lepol and long rotary kilns, the level may be even higher.","CLM (2013)\n2013/163/EU","1.2.5.6",18,18]
[304,"Cement, lime and MgO","3. Mineral Industry ","3.1. Installations for the production of cement clinker in rotary kilns with a production capacity exceeding 500t/day or lime in rotary kilns with a production capacity exceeding 50t/day or in other furnaces with a production capacity exceeding 50t/day.","Cement","Unspecified","Lepol and long rotary kilns","Unspecified","Unspecified","Unspecified","Kiln firing proceeses","Emissions to air","Air","NOx","Nitrogen dioxide","In order to reduce the emissions of NO x from the flue-gases of kiln firing and/or preheating/precalcining processes, BAT is to use one or a combination of the following techniques: (i) Primary techniques; (ii) Staged combustion (conventional or waste fuels), also in combination with a precalciner and the use of optimised fuel mix; (iii) Selective non-catalytic reduction (SNCR); (iv) Selective catalytic reduction (SCR)","mg/Nm3",400,"800","Green","Continuous",0,0,0.1,"Daily ","Depending on initial levels and NH 3 slip.","CLM (2013)\n2013/163/EU","1.2.5.6",18,18]
[303,"Cement, lime and MgO","3. Mineral Industry ","3.1. Installations for the production of cement clinker in rotary kilns with a production capacity exceeding 500t/day or lime in rotary kilns with a production capacity exceeding 50t/day or in other furnaces with a production capacity exceeding 50t/day.","Cement","Unspecified","Preheater kilns","Unspecified","Unspecified","Unspecified","Kiln firing processes","Emissions to air","Air","NOx","Nitrogen dioxide","In order to reduce the emissions of NO x from the flue-gases of kiln firing and/or preheating/precalcining processes, BAT is to use one or a combination of the following techniques: (i) Primary techniques; (ii) Staged combustion (conventional or waste fuels), also in combination with a precalciner and the use of optimised fuel mix; (iii) Selective non-catalytic reduction (SNCR); (iv) Selective catalytic reduction (SCR)","mg/Nm3",200,"450","Green","Continuous",0,0,0.1,"Daily ","The upper level of the BAT-AEL range is 500 mg/Nm 3 , if the initial NO x level after primary techniques is > 1 000 mg/Nm 3.\n\nExisting kiln system design, fuel mix properties including waste and raw material burnability (e.g. special cement or white cement clinker) can influence the ability to be within the range. Levels below 350 mg/Nm 3 are achieved at kilns with favourable conditions when using SNCR. In 2008, the lower value of 200 mg/Nm 3 has been reported as a monthly average for three plants (easy burning mix used) using SNCR.","CLM (2013)\n2013/163/EU","1.2.5.6",18,18]
[317,"Cement, lime and MgO","3. Mineral Industry ","3.1. Installations for the production of cement clinker in rotary kilns with a production capacity exceeding 500t/day or lime in rotary kilns with a production capacity exceeding 50t/day or in other furnaces with a production capacity exceeding 50t/day.","Lime","Unspecified","LRK, PRK","Unspecified","Unspecified","Unspecified","Kiln firing process","Emissions to air","Air","NOx","Nitrogen dioxide","In order to reduce the emissions of NO X from the flue-gases of kiln firing processes, BAT is to use one or a combination of the following techniques:(i) Primary techniques; (ii) SNCR","mg/Nm3",200,"500","Green","Continuous",0,0,0.11,"daily average value or average over the sampling period (spot measurements for at least half an hour), stated as NO 2","The higher ends of the ranges are related to the production of dolime and hard burned lime. Higher levels than the upper end of the range may be associated with the production of sintered dolime.\n\nWhere primary techniques as indicated in BAT 45 (a)I are not sufficient to reach this level and where secondary techniques are not applicable to reduce the NO x emissions to 350 mg/Nm 3 , the upper level is 500 mg/Nm 3 , especially for hard burned lime and for the use of biomass as fuel.","CLM (2013)\n2013/163/EU","1.3.7.2",30,30]
[316,"Cement, lime and MgO","3. Mineral Industry ","3.1. Installations for the production of cement clinker in rotary kilns with a production capacity exceeding 500t/day or lime in rotary kilns with a production capacity exceeding 50t/day or in other furnaces with a production capacity exceeding 50t/day.","Lime","Unspecified","PFRK, ASK, MFSK, OSK","Unspecified","Unspecified","Unspecified","Kiln firing process","Emissions to air","Air","NOx","Nitrogen dioxide","In order to reduce the emissions of NO X from the flue-gases of kiln firing processes, BAT is to use one or a combination of the following techniques:(i) Primary techniques; (ii) SNCR","mg/Nm3",100,"350","Green","Continuous",0,0,0.11,"daily average value or average over the sampling period (spot measurements for at least half an hour), stated as NO 2","The higher ends of the ranges are related to the production of dolime and hard burned lime. Higher levels than the upper end of the range may be associated with the production of sintered dolime.\n\nWhere primary techniques as indicated in BAT 45 (a)I are not sufficient to reach this level and where secondary techniques are not applicable to reduce the NO x emissions to 350 mg/Nm 3 , the upper level is 500 mg/Nm 3 , especially for hard burned lime and for the use of biomass as fuel.","CLM (2013)\n2013/163/EU","1.3.7.2",30,30]
[331,"Cement, lime and MgO","3. Mineral Industry ","3.1. Installations for the production of cement clinker in rotary kilns with a production capacity exceeding 500t/day or lime in rotary kilns with a production capacity exceeding 50t/day or in other furnaces with a production capacity exceeding 50t/day.","Magnesium oxide","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Kiln firing process","Emissions to air","Air","NOx","Nitrogen dioxide","In order to reduce the emissions of NO x from the flue-gases of kiln firing processes, BAT is to use a combination of the following techniques: (i) Appropriate fuel selection along with a limited nitrogen content in the fuel; (ii) Process optimisation and improved firing technique","mg/Nm3",500,"1500","Green","Continuous",0,0,0.1,"Daily","The higher values are related to the high temperature DBM process.","CLM (2013)\n2013/163/EU","1.4.4.2",37,37]
[308,"Cement, lime and MgO","3. Mineral Industry ","3.1. Installations for the production of cement clinker in rotary kilns with a production capacity exceeding 500t/day or lime in rotary kilns with a production capacity exceeding 50t/day or in other furnaces with a production capacity exceeding 50t/day.","Cement","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Kiln firing process","Emissions to air","Air","PCDD/F","PCDD/F","In order to prevent emissions of PCDD/F or to keep the emissions of PCDD/F from the flue-gases of the kiln firing processes low, BAT is to use one or a combination of the following techniques: (i) Carefully selecting and controlling of kiln inputs (raw materials), i.e. chlorine, copper and volatile organic compounds; (ii) Carefully selecting and controlling kiln inputs (fuels), i.e. chlorine and copper; (iii) Limiting/avoiding the use of wastes which contain chlorinated organic materials; (iv) Avoid feeding fuels with a high content of halogens (e.g. chlorine) in secondary firing; (v) Quick cooling of kiln flue-gases to lower than 200 °C and minimising residence time of flue-gases and oxygen content in zones where the temperatures range between 300 and 450 °C; (vi) Stop co-incinerating waste for operations such as start-ups and/or shutdowns","ng PCDD/F I-TEQ/Nm 3",0.05,"0.1","Green","Periodic",0,0,0.1,"average over the sampling period (6 – 8 hours)",0,"CLM (2013)\n2013/163/EU","1.2.7",21,21]
[325,"Cement, lime and MgO","3. Mineral Industry ","3.1. Installations for the production of cement clinker in rotary kilns with a production capacity exceeding 500t/day or lime in rotary kilns with a production capacity exceeding 50t/day or in other furnaces with a production capacity exceeding 50t/day.","Lime","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Kiln firing process","Emissions to air","Air","PCDD/F","PCDD/F","In order to prevent or reduce the emissions of PCDD/F from the flue-gas of kiln firing processes, BAT is to use one or a combination of the following primary techniques: (i) Selecting fuels with a low chlorine content; (ii) limiting the copper input through the fuel; (iii) Minimsing the residence time of the flue gases and the oxygen content in zones where the termperatures range between 300-450oC","ng PCDD/F I-TEQ/Nm 3",0.05,"0.1","Green","Periodic",0,0,0.11,"average over the sampling period (6 – 8 hours)",0,"CLM (2013)\n2013/163/EU","1.3.8",33,33]
[306,"Cement, lime and MgO","3. Mineral Industry ","3.1. Installations for the production of cement clinker in rotary kilns with a production capacity exceeding 500t/day or lime in rotary kilns with a production capacity exceeding 50t/day or in other furnaces with a production capacity exceeding 50t/day.","Cement","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Emissions to air","Air","SOx expressed as SO2","Sulphur Dioxide (24 Hour Mean)","In order to reduce/minimise the emissions of SO x from the flue-gases of kiln firing and/or preheating/precalcining processes, BAT is to use one of the following techniques: (i) Absorbent addition; (ii) Wet scrubber","mg/Nm3",50,"400","Green","Continuous",0,0,"Unspecified","Daily ","The range takes into account the sulphur content in the raw materials.\n\nFor white cement and special cement clinker production, the ability of clinker to retain fuel sulphur might be significantly lower leading to higher SO X emissions.","CLM (2013)\n2013/163/EU","1.2.6.2",19,19]
[319,"Cement, lime and MgO","3. Mineral Industry ","3.1. Installations for the production of cement clinker in rotary kilns with a production capacity exceeding 500t/day or lime in rotary kilns with a production capacity exceeding 50t/day or in other furnaces with a production capacity exceeding 50t/day.","Lime","Unspecified","LRK, PRK","Unspecified","Unspecified","Unspecified","Kiln firing process","Emissions to air","Air","SOx expressed as SO2","Sulphur Dioxide (24 Hour Mean)","In order to reduce the emissions of SO x from the flue-gases of kiln firing processes, BAT is to use one or a combination of the following techniques: (i) Process optimisation to ensure an efficient absorption of sulphur dioxide (e.g. efficient contact between the kiln gases and the quicklime); (ii) Selecting fuels with a low sulphur content; (iii) Using absorbent addition techniques (e.g. absorbent addition, dry flue-gas cleaning with a filter, wet scrubber, or activated carbon injection)","mg/Nm3",50,"400","Green","Continuous",0,0,0.11,"daily average value or average over the sampling period (spot measurements for at least half an hour), SO x expressed as SO 2","The level depends on the initial SO x level in the flue-gas and on the reduction technique used.\n\nFor the production of sintered dolime using the ‘double- pass process’, SO x emissions might be higher than the upper end of the range.","CLM (2013)\n2013/163/EU","1.3.7.3",31,31]
[318,"Cement, lime and MgO","3. Mineral Industry ","3.1. Installations for the production of cement clinker in rotary kilns with a production capacity exceeding 500t/day or lime in rotary kilns with a production capacity exceeding 50t/day or in other furnaces with a production capacity exceeding 50t/day.","Lime","Unspecified","PFRK, ASK, MFSK, OSK","Unspecified","Unspecified","Unspecified","Kiln firing process","Emissions to air","Air","SOx expressed as SO2","Sulphur Dioxide (24 Hour Mean)","In order to reduce the emissions of SO x from the flue-gases of kiln firing processes, BAT is to use one or a combination of the following techniques: (i) Process optimisation to ensure an efficient absorption of sulphur dioxide (e.g. efficient contact between the kiln gases and the quicklime); (ii) Selecting fuels with a low sulphur content; (iii) Using absorbent addition techniques (e.g. absorbent addition, dry flue-gas cleaning with a filter, wet scrubber, or activated carbon injection)","mg/Nm3",50,"200","Green","Continuous",0,0,0.11,"daily average value or average over the sampling period (spot measurements for at least half an hour), SO x expressed as SO 2","The level depends on the initial SO x level in the flue-gas and on the reduction technique used.\n\nFor the production of sintered dolime using the ‘double- pass process’, SO x emissions might be higher than the upper end of the range.","CLM (2013)\n2013/163/EU","1.3.7.3",31,31]
[333,"Cement, lime and MgO","3. Mineral Industry ","3.1. Installations for the production of cement clinker in rotary kilns with a production capacity exceeding 500t/day or lime in rotary kilns with a production capacity exceeding 50t/day or in other furnaces with a production capacity exceeding 50t/day.","Magnesium oxide","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Kiln firing process","Emissions to air","Air","SOx expressed as SO2","Sulphur Dioxide (24 Hour Mean)","In order to reduce the emissions of SO x from the flue-gases of kiln firing processes, BAT is to use a combination of the following primary and secondary techniques: (i) Process optimisation techniques; (ii) Selecting fuels with a low sulphur content; (iii) A dry absorbent addition technique (sorbent addition into the flue gas stream such as reactive MgO grades, hydrated lime, activated carbon, etc.), in combination with a filter; (iv) Wet scrubber","mg/Nm3",50,"400","Green","Continuous",0,0,0.1,"daily average value or average over the sampling period (spot measurements for at least half an hour","The BAT-AELs depend on the content of sulphur in the raw materials and fuels. The lower end of the range is associated with the use of raw materials with low sulphur content and the use of natural gas; the upper end of the range is associated with the use of raw materials with higher sulphur content and/or the use of sulphur-containing fuels.\n\nCross-media effects should be taken into account to assess the best combination of BAT to reduce SO x emissions.\n\nWhen a wet scrubber is not applicable, BAT-AELs depend on the sulphur content of raw materials and fuels. In this case, the BAT-AEL is < 1 500 mg/Nm 3 while ensuring a SO X emissions removal efficiency of at least 60 %.","CLM (2013)\n2013/163/EU","1.4.4.4",39,39]
[322,"Cement, lime and MgO","3. Mineral Industry ","3.1. Installations for the production of cement clinker in rotary kilns with a production capacity exceeding 500t/day or lime in rotary kilns with a production capacity exceeding 50t/day or in other furnaces with a production capacity exceeding 50t/day.","Lime","Unspecified","ASK, MFSK, PFRK","Unspecified","Unspecified","Unspecified","Kiln firing process","Emissions to air","Air","Total organic compounds","Total organic compounds","In order to reduce the emissions of TOC from the flue-gases of kiln firing processes, BAT is to use one or a combination of the following techniques: (i) Applying general primary techniques and monitoring (see also BAT 30 and 31 in Section 1.3.1, and BAT 32 in Section 1.3.2); (ii) Avoid feeding raw materials with a high content of volatile organic compounds into the kiln system (except for hydraulic lime production)","mg/Nm3","N/A","30","Green","Continuous",0,0,0.11,"daily average value or average over the sampling period (spot measurements for at least half an hour)","Level can be higher depending on the content of organic matter of raw materials used and/or the type of lime produced, in particular for the production of natural hydraulic lime.\n\nIn exceptional cases, the level can be higher.","CLM (2013)\n2013/163/EU","1.3.7.5",32,32]
[321,"Cement, lime and MgO","3. Mineral Industry ","3.1. Installations for the production of cement clinker in rotary kilns with a production capacity exceeding 500t/day or lime in rotary kilns with a production capacity exceeding 50t/day or in other furnaces with a production capacity exceeding 50t/day.","Lime","Unspecified","LRK, PRK","Unspecified","Unspecified","Unspecified","Kiln firing process","Emissions to air","Air","Total organic compounds","Total organic compounds","In order to reduce the emissions of TOC from the flue-gases of kiln firing processes, BAT is to use one or a combination of the following techniques: (i) Applying general primary techniques and monitoring (see also BAT 30 and 31 in Section 1.3.1, and BAT 32 in Section 1.3.2); (ii) Avoid feeding raw materials with a high content of volatile organic compounds into the kiln system (except for hydraulic lime production)","mg/Nm3","N/A","10","Green","Continuous",0,0,0.11,"daily average value or average over the sampling period (spot measurements for at least half an hour)","Level can be higher depending on the content of organic matter of raw materials used and/or the type of lime produced, in particular for the production of natural hydraulic lime","CLM (2013)\n2013/163/EU","1.3.7.5",32,32]
[400,"Chlor-Alkali","4. Chemical industry","4.2. Chemical installations for the production of basic inorganic chemicals.","Chlor-alkali industry",0,"Unspecified","Unspecified","Unspecified","Unspecified","Processing of chlorine","Emissions to air","Air","Chlorine and chlorine dioxide, measured together and expressed as Cl2","Chlorine","In order to reduce channelled emissions of chlorine and chlorine dioxide to air from the processing of chlorine, BAT is to design, maintain and operate a chlorine absorption unit that incorporates an appropriate combination of the following features:\n(i) absorption unit based on packed columns and/or ejectors with an alkaline solution (e.g. sodium hydroxide solution) as scrubbing liquid;\n(ii) hydrogen peroxide dosing equipment or a separate wet scrubber with hydrogen peroxide if necessary to reduce chlorine dioxide concentrations;\n(iii) size suitable for the worst case scenario (derived from a risk assessment), in terms of produced chlorine quantity and flowrate (absorption of the full cell room production for a sufficient duration until the plant is shut down);\n(iv) size of the scrubbing liquid supply and storage capacity suitable to ensure an excess at all times;\n(v) in the case of packed columns, their size should be suitable to prevent flooding at all times;\n(vi) prevention of ingress of liquid chlorine into the absorption unit;\n(vii) prevention of backflow of scrubbing liquid into the chlorine system;\n(viii) prevention of solids precipitation in the absorption unit;\n(ix) use of heat exchangers to limit the temperature in the absorption unit below 55 °C at all times;\n(x) supply of dilution air after chlorine absorption to prevent the formation of explosive gas mixtures;\n(xi) use of construction materials which withstand the extremely corrosive conditions at all times;\n(xii) use of backup equipment, such as an additional scrubber in series with the one in operation, an emergency tank with scrubbing liquid feeding the scrubber by gravity, stand-by and spare fans, stand-by and spare pumps;\n(xiii) provision of an independent backup system for critical electrical equipment;\n(xiv) provision of an automatic switch to the backup system in case of emergencies, including periodic tests on this system and the switch;\n(xv) provision of a monitoring and alarm system for the following parameters:\n(a) chlorine in the outlet of the absorption unit and the surrounding area;\n(b) temperature of the scrubbing liquids;\n(c) reduction potential and alkalinity of the scrubbing liquids;\n(d) suction pressure;\n(e) flowrate of scrubbing liquids.","mg/m3",0.2,1,"Green","Continous with electrochemical cells\n\nYearly with absorption in a solution with subsequent analysis",0,0,"Unspecified","average value of at least three consecutive hourly measurements performed at least once every year at the outlet of the chlorine absorption unit.",0,"CAK (2013)\n2013/732/EU",6,45,45]
[401,"Chlor-Alkali","4. Chemical industry","4.2. Chemical installations for the production of basic inorganic chemicals.","Chlor-alkali industry",0,"Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Emissions to water","Water","Free chlorine, expressed as Cl2 ","Chlorine (95%ile)","In order to reduce emissions of free chlorine to water from the chlor-alkali plant, BAT is to treat waste water streams containing free chlorine as close as possible to the source, to prevent stripping of chlorine and/or the formation of halogenated organic compounds, by using one or a combination of the techniques given below: (i) Chemical reduction; (ii) Catalytic decomposition; (iii) Thermal decomposition; (iv) Acidic decomposition; (v) Waste water recycling","mg/l",0.05,0.2,"Green","Continouos ",0,0,"Unspecified",0,0,"CAK (2013)\n2013/732/EU",7,46,46]
[1106,"Common Waste Water and Waste Gas Treatment","4. Chemical industry","4: Chemical industry;\n6.11: Independently operated treatment of waste water not covered by Council Directive 91/271/EEC and discharged by an installation undertaking activities covered under Section 4 of Annex I to Directive 2010/75/EU.\n \n",0,0,"Unspecified","Unspecified","Unspecified","Unspecified","Whole plant","Emissions to water","Water","Adsorbable organically bound halogens (AOX)","Adsorbable organically bound halogens (AOX)","Appropriate final waste water treatment techniques, depending on the pollutant, include:\n\nPreliminary and primary treatment:(i) Equalisation; (ii) Neutralisation; (iii) Physical separation, e.g.\nscreens, sieves, grit separators,\ngrease separators or\nprimary settlement tanks \n\nBiological treatment: (i) Activated sludge process; (ii) Membrane bioreactor\n\nNitrogen removal: (i) Nitrification/denitrification\n\nPhosphorus removal: (i) Chemical precipitation\n\nFinal solids removal: (i) Coagulation and flocculation; (ii) Sedimentation; (iii) Filtration (e.g. sand filtration,\nmicrofiltration, ultrafiltration); (iv) Flotation\n","mg/l",0.2,1,"Green","Monthly",0,0,"N/A","Yearly","The lower end of the range is typically achieved when few halogenated organic compounds are used or produced by the installation\n\nThis BAT-AEL may not apply when the main pollutant load originates from the production of iodinated X-ray contrast agents due\nto the high refractory loads. This BAT-AEL may also not apply when the main pollutant load originates from the production of propylene\noxide or epichlorohydrin via the chlorohydrin process due to the high loads. ","CWW (2016) 2016/902 \n",3.4,35,13]
[1101,"Common Waste Water and Waste Gas Treatment","4. Chemical industry","4: Chemical industry;\n6.11: Independently operated treatment of waste water not covered by Council Directive 91/271/EEC and discharged by an installation undertaking activities covered under Section 4 of Annex I to Directive 2010/75/EU.\n \n",0,0,"Unspecified","Unspecified","Unspecified","Unspecified","Whole plant","Emissions to water","Water","Chemical Oxygen Demand (COD)","COD","Appropriate final waste water treatment techniques, depending on the pollutant, include:\n\nPreliminary and primary treatment:(i) Equalisation; (ii) Neutralisation; (iii) Physical separation, e.g.\nscreens, sieves, grit separators,\ngrease separators or\nprimary settlement tanks \n\nBiological treatment: (i) Activated sludge process; (ii) Membrane bioreactor\n\nNitrogen removal: (i) Nitrification/denitrification\n\nPhosphorus removal: (i) Chemical precipitation\n\nFinal solids removal: (i) Coagulation and flocculation; (ii) Sedimentation; (iii) Filtration (e.g. sand filtration,\nmicrofiltration, ultrafiltration); (iv) Flotation\n","mg/l",30,100,"Green","Daily",0,0,"N/A","Yearly","No BAT-AEL applies for Biochemical oxygen demand (BOD). As an indication, the yearly average BOD5 level in the effluent from a biological waste water treatment plant will generally be ≤ 20 mg/l.\n\nEither the BAT-AEL for TOC or the BAT-AEL for COD applies. TOC is the preferred option because its monitoring does not rely on\nthe use of very toxic compounds. \n\nThe lower end of the range is typically achieved when few tributary waste water streams contain organic compounds and/or the\nwaste water mostly contains easily biodegradable organic compounds. \n\nThe upper end of the range may be up to 100 mg/l for TOC or up to 300 mg/l for COD, both as yearly averages, if both of the following\nconditions are fulfilled:\n— Condition A: Abatement efficiency ≥ 90 % as a yearly average (including both pretreatment and final treatment).\n— Condition B: If a biological treatment is used, at least one of the following criteria is met:\n— A low-loaded biological treatment step is used (i.e. ≤ 0,25 kg COD/kg of organic dry matter of sludge). This implies that the\nBOD5 level in the effluent is ≤ 20 mg/l.\n— Nitrification is used. \n\nThe upper end of the range may not apply if all of the following conditions are fulfilled:\n— Condition A: Abatement efficiency ≥ 95 % as a yearly average (including both pretreatment and final treatment).\n— Condition B: same as Condition B in footnote (4).\n— Condition C: The influent to the final waste water treatment shows the following characteristics: TOC > 2 g/l (or COD > 6 g/l)\nas a yearly average and a high proportion of refractory organic compounds. \n\nThe upper end of the range may not apply when the main pollutant load originates from the production of methylcellulose. \n\nThe BAT-AEL applies if the emission exceeds\n10 t/yr. ","CWW (2016) 2016/902 \n",3.4,34,12]
[1107,"Common Waste Water and Waste Gas Treatment","4. Chemical industry","4: Chemical industry;\n6.11: Independently operated treatment of waste water not covered by Council Directive 91/271/EEC and discharged by an installation undertaking activities covered under Section 4 of Annex I to Directive 2010/75/EU.\n \n",0,0,"Unspecified","Unspecified","Unspecified","Unspecified","Whole plant","Emissions to water","Water","Chromium (expressed as Cr) ","Chromium VI (95%ile) (dissolved)","Appropriate final waste water treatment techniques, depending on the pollutant, include:\n\nPreliminary and primary treatment:(i) Equalisation; (ii) Neutralisation; (iii) Physical separation, e.g.\nscreens, sieves, grit separators,\ngrease separators or\nprimary settlement tanks \n\nBiological treatment: (i) Activated sludge process; (ii) Membrane bioreactor\n\nNitrogen removal: (i) Nitrification/denitrification\n\nPhosphorus removal: (i) Chemical precipitation\n\nFinal solids removal: (i) Coagulation and flocculation; (ii) Sedimentation; (iii) Filtration (e.g. sand filtration,\nmicrofiltration, ultrafiltration); (iv) Flotation\n","mg/l",5,25,"Green","Monthly",0,0,"N/A","Yearly","The lower end of the range is typically achieved when few of the corresponding metal (compounds) are used or produced by the installation\n\nThis BAT-AEL may not apply to inorganic effluents when the main pollutant load originates from the production of inorganic\nheavy metal compounds.\n\nThis BAT-AEL may not apply when the main pollutant load originates from the processing of large volumes of solid inorganic raw\nmaterials that are contaminated with metals (e.g. soda ash from the Solvay process, titanium dioxide).       \n\nThis BAT-AEL may not apply when the main pollutant load originates from the production of chromium-organic compounds.","CWW (2016) 2016/902 \n",3.4,35,13]
[1108,"Common Waste Water and Waste Gas Treatment","4. Chemical industry","4: Chemical industry;\n6.11: Independently operated treatment of waste water not covered by Council Directive 91/271/EEC and discharged by an installation undertaking activities covered under Section 4 of Annex I to Directive 2010/75/EU.\n \n",0,0,"Unspecified","Unspecified","Unspecified","Unspecified","Whole plant","Emissions to water","Water","Copper (expressed as Cu)","Copper (expressed as Cu)","Appropriate final waste water treatment techniques, depending on the pollutant, include:\n\nPreliminary and primary treatment:(i) Equalisation; (ii) Neutralisation; (iii) Physical separation, e.g.\nscreens, sieves, grit separators,\ngrease separators or\nprimary settlement tanks \n\nBiological treatment: (i) Activated sludge process; (ii) Membrane bioreactor\n\nNitrogen removal: (i) Nitrification/denitrification\n\nPhosphorus removal: (i) Chemical precipitation\n\nFinal solids removal: (i) Coagulation and flocculation; (ii) Sedimentation; (iii) Filtration (e.g. sand filtration,\nmicrofiltration, ultrafiltration); (iv) Flotation\n","mg/l",5,50,"Green","Monthly",0,0,"N/A","Yearly","The lower end of the range is typically achieved when few of the corresponding metal (compounds) are used or produced by the installation\n\nThis BAT-AEL may not apply to inorganic effluents when the main pollutant load originates from the production of inorganic\nheavy metal compounds.\n\nThis BAT-AEL may not apply when the main pollutant load originates from the processing of large volumes of solid inorganic raw\nmaterials that are contaminated with metals (e.g. soda ash from the Solvay process, titanium dioxide).       \n\nThis BAT-AEL may not apply when the main pollutant load originates from the production of chromium-organic compounds.\n\nThis BAT-AEL may not apply when the main pollutant load originates from the production of copper-organic compounds or the\nproduction of vinyl chloride monomer/ethylene dichloride via the oxychlorination process. ","CWW (2016) 2016/902 \n",3.4,35,13]
[1109,"Common Waste Water and Waste Gas Treatment","4. Chemical industry","4: Chemical industry;\n6.11: Independently operated treatment of waste water not covered by Council Directive 91/271/EEC and discharged by an installation undertaking activities covered under Section 4 of Annex I to Directive 2010/75/EU.\n \n",0,0,"Unspecified","Unspecified","Unspecified","Unspecified","Whole plant","Emissions to water","Water","Nickel (expressed as Ni)","Nickel and its compounds","Appropriate final waste water treatment techniques, depending on the pollutant, include:\n\nPreliminary and primary treatment:(i) Equalisation; (ii) Neutralisation; (iii) Physical separation, e.g.\nscreens, sieves, grit separators,\ngrease separators or\nprimary settlement tanks \n\nBiological treatment: (i) Activated sludge process; (ii) Membrane bioreactor\n\nNitrogen removal: (i) Nitrification/denitrification\n\nPhosphorus removal: (i) Chemical precipitation\n\nFinal solids removal: (i) Coagulation and flocculation; (ii) Sedimentation; (iii) Filtration (e.g. sand filtration,\nmicrofiltration, ultrafiltration); (iv) Flotation\n","mg/l",5,50,"Green","Monthly",0,0,"N/A","Yearly","The lower end of the range is typically achieved when few of the corresponding metal (compounds) are used or produced by the installation\n\nThis BAT-AEL may not apply to inorganic effluents when the main pollutant load originates from the production of inorganic\nheavy metal compounds.\n\nThis BAT-AEL may not apply when the main pollutant load originates from the processing of large volumes of solid inorganic raw\nmaterials that are contaminated with metals (e.g. soda ash from the Solvay process, titanium dioxide).   ","CWW (2016) 2016/902 \n",3.4,35,13]
[1104,"Common Waste Water and Waste Gas Treatment","4. Chemical industry","4: Chemical industry;\n6.11: Independently operated treatment of waste water not covered by Council Directive 91/271/EEC and discharged by an installation undertaking activities covered under Section 4 of Annex I to Directive 2010/75/EU.\n \n",0,0,"Unspecified","Unspecified","Unspecified","Unspecified","Whole plant","Emissions to water","Water","Total inorganic nitrogen (Ninorg)","Total inorganic nitrogen (Ninorg)","Appropriate final waste water treatment techniques, depending on the pollutant, include:\n\nPreliminary and primary treatment:(i) Equalisation; (ii) Neutralisation; (iii) Physical separation, e.g.\nscreens, sieves, grit separators,\ngrease separators or\nprimary settlement tanks \n\nBiological treatment: (i) Activated sludge process; (ii) Membrane bioreactor\n\nNitrogen removal: (i) Nitrification/denitrification\n\nPhosphorus removal: (i) Chemical precipitation\n\nFinal solids removal: (i) Coagulation and flocculation; (ii) Sedimentation; (iii) Filtration (e.g. sand filtration,\nmicrofiltration, ultrafiltration); (iv) Flotation\n","mg/l",5,20,"Green","Daily",0,0,"N/A","Yearly","Either the BAT-AEL for total nitrogen or the BAT-AEL for total inorganic nitrogen applies. \n\nThe BAT-AELs for TN and Ninorg do not apply to installations without biological waste water treatment. The lower end of the range\nis typically achieved when the influent to the biological waste water treatment plant contains low levels of nitrogen and/or when nitrification/denitrification\ncan be operated under optimum conditions. \n\nThe upper end of the range may be higher and up to 40 mg/l for TN or 35 mg/l for Ninorg, both as yearly averages, if the abatement\nefficiency is ≥ 70 % as a yearly average (including both pretreatment and final treatment). ","CWW (2016) 2016/902 \n",3.4,35,13]
[1103,"Common Waste Water and Waste Gas Treatment","4. Chemical industry","4: Chemical industry;\n6.11: Independently operated treatment of waste water not covered by Council Directive 91/271/EEC and discharged by an installation undertaking activities covered under Section 4 of Annex I to Directive 2010/75/EU.\n \n",0,0,"Unspecified","Unspecified","Unspecified","Unspecified","Whole plant","Emissions to water","Water","Total Nitrogen (TN)","Total Nitrogen (TN)","Appropriate final waste water treatment techniques, depending on the pollutant, include:\n\nPreliminary and primary treatment:(i) Equalisation; (ii) Neutralisation; (iii) Physical separation, e.g.\nscreens, sieves, grit separators,\ngrease separators or\nprimary settlement tanks \n\nBiological treatment: (i) Activated sludge process; (ii) Membrane bioreactor\n\nNitrogen removal: (i) Nitrification/denitrification\n\nPhosphorus removal: (i) Chemical precipitation\n\nFinal solids removal: (i) Coagulation and flocculation; (ii) Sedimentation; (iii) Filtration (e.g. sand filtration,\nmicrofiltration, ultrafiltration); (iv) Flotation\n","mg/l",5,25,"Green","Daily",0,0,"N/A","Yearly","Either the BAT-AEL for total nitrogen or the BAT-AEL for total inorganic nitrogen applies. \n\nThe BAT-AELs for TN and Ninorg do not apply to installations without biological waste water treatment. The lower end of the range\nis typically achieved when the influent to the biological waste water treatment plant contains low levels of nitrogen and/or when nitrification/denitrification\ncan be operated under optimum conditions. \n\nThe upper end of the range may be higher and up to 40 mg/l for TN or 35 mg/l for Ninorg, both as yearly averages, if the abatement\nefficiency is ≥ 70 % as a yearly average (including both pretreatment and final treatment). ","CWW (2016) 2016/902 \n",3.4,35,13]
[1100,"Common Waste Water and Waste Gas Treatment","4. Chemical industry","4: Chemical industry;\n6.11: Independently operated treatment of waste water not covered by Council Directive 91/271/EEC and discharged by an installation undertaking activities covered under Section 4 of Annex I to Directive 2010/75/EU.\n \n",0,0,"Unspecified","Unspecified","Unspecified","Unspecified","Whole plant","Emissions to water","Water","Total Organic Carbon (TOC)","Total Organic Carbon (TOC)","Appropriate final waste water treatment techniques, depending on the pollutant, include:\n\nPreliminary and primary treatment:(i) Equalisation; (ii) Neutralisation; (iii) Physical separation, e.g.\nscreens, sieves, grit separators,\ngrease separators or\nprimary settlement tanks \n\nBiological treatment: (i) Activated sludge process; (ii) Membrane bioreactor\n\nNitrogen removal: (i) Nitrification/denitrification\n\nPhosphorus removal: (i) Chemical precipitation\n\nFinal solids removal: (i) Coagulation and flocculation; (ii) Sedimentation; (iii) Filtration (e.g. sand filtration,\nmicrofiltration, ultrafiltration); (iv) Flotation\n","mg/l",10,33,"Green","Daily",0,0,"N/A","Yearly","No BAT-AEL applies for Biochemical oxygen demand (BOD). As an indication, the yearly average BOD5 level in the effluent from a biological waste water treatment plant will generally be ≤ 20 mg/l.\n\nEither the BAT-AEL for TOC or the BAT-AEL for COD applies. TOC is the preferred option because its monitoring does not rely on\nthe use of very toxic compounds. \n\nThe lower end of the range is typically achieved when few tributary waste water streams contain organic compounds and/or the\nwaste water mostly contains easily biodegradable organic compounds. \n\nThe upper end of the range may be up to 100 mg/l for TOC or up to 300 mg/l for COD, both as yearly averages, if both of the following\nconditions are fulfilled:\n— Condition A: Abatement efficiency ≥ 90 % as a yearly average (including both pretreatment and final treatment).\n— Condition B: If a biological treatment is used, at least one of the following criteria is met:\n— A low-loaded biological treatment step is used (i.e. ≤ 0,25 kg COD/kg of organic dry matter of sludge). This implies that the\nBOD5 level in the effluent is ≤ 20 mg/l.\n— Nitrification is used. \n\nThe upper end of the range may not apply if all of the following conditions are fulfilled:\n— Condition A: Abatement efficiency ≥ 95 % as a yearly average (including both pretreatment and final treatment).\n— Condition B: same as Condition B in footnote (4).\n— Condition C: The influent to the final waste water treatment shows the following characteristics: TOC > 2 g/l (or COD > 6 g/l)\nas a yearly average and a high proportion of refractory organic compounds. \n\nThe upper end of the range may not apply when the main pollutant load originates from the production of methylcellulose. \n\nThe BAT-AEL applies if the emission exceeds\n3,3 t/yr. ","CWW (2016) 2016/902 \n",3.4,34,12]
[1105,"Common Waste Water and Waste Gas Treatment","4. Chemical industry","4: Chemical industry;\n6.11: Independently operated treatment of waste water not covered by Council Directive 91/271/EEC and discharged by an installation undertaking activities covered under Section 4 of Annex I to Directive 2010/75/EU.\n \n",0,0,"Unspecified","Unspecified","Unspecified","Unspecified","Whole plant","Emissions to water","Water","Total phosphorous","Total phosphorous","Appropriate final waste water treatment techniques, depending on the pollutant, include:\n\nPreliminary and primary treatment:(i) Equalisation; (ii) Neutralisation; (iii) Physical separation, e.g.\nscreens, sieves, grit separators,\ngrease separators or\nprimary settlement tanks \n\nBiological treatment: (i) Activated sludge process; (ii) Membrane bioreactor\n\nNitrogen removal: (i) Nitrification/denitrification\n\nPhosphorus removal: (i) Chemical precipitation\n\nFinal solids removal: (i) Coagulation and flocculation; (ii) Sedimentation; (iii) Filtration (e.g. sand filtration,\nmicrofiltration, ultrafiltration); (iv) Flotation\n","mg/l",0.5,3,"Green","Daily",0,0,"N/A","Yearly","The lower end of the range is typically achieved when phosphorus is added for the proper operation of the biological waste water treatment plant or when phosphorus mainly originates from heating or cooling systems. The upper end of the range is typically achieved when phosphorus-containing compounds are produced by the installation.","CWW (2016) 2016/902 \n",3.4,35,13]
[1102,"Common Waste Water and Waste Gas Treatment","4. Chemical industry","4: Chemical industry;\n6.11: Independently operated treatment of waste water not covered by Council Directive 91/271/EEC and discharged by an installation undertaking activities covered under Section 4 of Annex I to Directive 2010/75/EU.\n \n",0,0,"Unspecified","Unspecified","Unspecified","Unspecified","Whole plant","Emissions to water","Water","Total Suspended Solids (TSS) ","Total Suspended Solids (TSS) ","Appropriate final waste water treatment techniques, depending on the pollutant, include:\n\nPreliminary and primary treatment:(i) Equalisation; (ii) Neutralisation; (iii) Physical separation, e.g.\nscreens, sieves, grit separators,\ngrease separators or\nprimary settlement tanks \n\nBiological treatment: (i) Activated sludge process; (ii) Membrane bioreactor\n\nNitrogen removal: (i) Nitrification/denitrification\n\nPhosphorus removal: (i) Chemical precipitation\n\nFinal solids removal: (i) Coagulation and flocculation; (ii) Sedimentation; (iii) Filtration (e.g. sand filtration,\nmicrofiltration, ultrafiltration); (iv) Flotation\n","mg/l",5,35,"Green","Daily",0,0,"N/A","Yearly","The lower end of the range is typically achieved when using filtration (e.g. sand filtration, microfiltration, ultrafiltration, membrane bioreactor), while the upper end of the range is typically achieved when using sedimentation only.\n\nThis BAT-AEL may not apply when the main pollutant load originates from the production of soda ash via the Solvay process or\nfrom the production of titanium dioxide. \n\nThe BAT-AEL applies if the emission exceeds\n3,5 t/yr. ","CWW (2016) 2016/902 \n",3.4,34,12]
[1110,"Common Waste Water and Waste Gas Treatment","4. Chemical industry","4: Chemical industry;\n6.11: Independently operated treatment of waste water not covered by Council Directive 91/271/EEC and discharged by an installation undertaking activities covered under Section 4 of Annex I to Directive 2010/75/EU.\n \n",0,0,"Unspecified","Unspecified","Unspecified","Unspecified","Whole plant","Emissions to water","Water","Zinc (expressed as Zn)","Zinc (expressed as Zn)","Appropriate final waste water treatment techniques, depending on the pollutant, include:\n\nPreliminary and primary treatment:(i) Equalisation; (ii) Neutralisation; (iii) Physical separation, e.g.\nscreens, sieves, grit separators,\ngrease separators or\nprimary settlement tanks \n\nBiological treatment: (i) Activated sludge process; (ii) Membrane bioreactor\n\nNitrogen removal: (i) Nitrification/denitrification\n\nPhosphorus removal: (i) Chemical precipitation\n\nFinal solids removal: (i) Coagulation and flocculation; (ii) Sedimentation; (iii) Filtration (e.g. sand filtration,\nmicrofiltration, ultrafiltration); (iv) Flotation\n","mg/l",20,300,"Green","Monthly",0,0,"N/A","Yearly","The lower end of the range is typically achieved when few of the corresponding metal (compounds) are used or produced by the installation\n\nThis BAT-AEL may not apply to inorganic effluents when the main pollutant load originates from the production of inorganic\nheavy metal compounds.\n\nThis BAT-AEL may not apply when the main pollutant load originates from the processing of large volumes of solid inorganic raw\nmaterials that are contaminated with metals (e.g. soda ash from the Solvay process, titanium dioxide).   \n\nThis BAT-AEL may not apply when the main pollutant load originates from the production of viscose fibres. ","CWW (2016) 2016/902 \n",3.4,35,13]
[1189,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes- Curing oven emissions ","Emissions to air","Air","Amines","Amines","BAT is to reduce emissions from downstream processes by using one or a combination of the following techniques: (i) Impact jets and cyclones; (ii) Wet scrubbers; (iii) Wet electrostatic precipitators; (iv) Stone wool filters; (v) Waste gas incineration","mg/Nm3","N/A","2","Amber",0,"273.15","101.3","N/A","Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.7.7",50,50]
[1185,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes- Curing oven emissions ","Emissions to air","Air","Amines","Amines","BAT is to reduce emissions from downstream processes by using one or a combination of the following techniques: (i) Impact jets and cyclones; (ii) Wet scrubbers; (iii) Wet electrostatic precipitators; (iv) Stone wool filters; (v) Waste gas incineration","kg/tonne melted glass","N/A","0.01","Amber",0,"273.15","101.3","N/A","Daily average (continuous)","The specific mass emissions refer to 1 tonne of produced glass","GLS (2012) - 2012/134/EU","1.7.7",50,50]
[1179,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes- Forming area ","Emissions to air","Air","Amines","Amines","BAT is to reduce emissions from downstream processes by using one or a combination of the following techniques: (i) Impact jets and cyclones; (ii) Wet scrubbers; (iii) Wet electrostatic precipitators; (iv) Stone wool filters; (v) Waste gas incineration","mg/Nm3","N/A","3","Amber",0,"273.15","101.3","N/A","Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.7.7",50,50]
[1077,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Filament glass fibre","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes (forming and coating)","Emissions to air","Air","Ammonia","Ammonia (ecological receptor - Sensitive Lichens)","BAT is to reduce emissions from downstream processes by using one or a combination of the following techniques: (i) Wet scrubbing systems; (ii) Wet electrostatic precipitator; (iii) Filtration system (bag filter)","mg/Nm3","N/A","20","Amber",0,"273.15","101.3","N/A","Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.4.6",32,32]
[1187,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes- Curing oven emissions ","Emissions to air","Air","Ammonia","Ammonia (ecological receptor - Sensitive Lichens)","BAT is to reduce emissions from downstream processes by using one or a combination of the following techniques: (i) Impact jets and cyclones; (ii) Wet scrubbers; (iii) Wet electrostatic precipitators; (iv) Stone wool filters; (v) Waste gas incineration","mg/Nm3","20","60","Green","Continuous or regular periodic measurements of NH 3 emissions, when selective catalytic reduction (SCR) or selective non-catalytic reduction (SNCR) techniques are applied","273.15","101.3","N/A","Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.7.7",50,50]
[1184,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes- Curing oven emissions ","Emissions to air","Air","Ammonia","Ammonia (ecological receptor - Sensitive Lichens)","BAT is to reduce emissions from downstream processes by using one or a combination of the following techniques: (i) Impact jets and cyclones; (ii) Wet scrubbers; (iii) Wet electrostatic precipitators; (iv) Stone wool filters; (v) Waste gas incineration","kg/tonne melted glass","N/A","0.4","Amber",0,"273.15","101.3","N/A","Daily average (continuous)","The specific mass emissions refer to 1 tonne of produced glass","GLS (2012) - 2012/134/EU","1.7.7",50,50]
[1178,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes- Forming area ","Emissions to air","Air","Ammonia","Ammonia (ecological receptor - Sensitive Lichens)","BAT is to reduce emissions from downstream processes by using one or a combination of the following techniques: (i) Impact jets and cyclones; (ii) Wet scrubbers; (iii) Wet electrostatic precipitators; (iv) Stone wool filters; (v) Waste gas incineration","mg/Nm3","30","60","Green","Continuous or regular periodic measurements of NH 3 emissions, when selective catalytic reduction (SCR) or selective non-catalytic reduction (SNCR) techniques are applied","273.15","101.3","N/A","Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.7.7",49,49]
[1025,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Container glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes","Emissions to air","Air","Dust","Particulates (PM10) (24 hr Mean)","When tin, organotin or titanium compounds are used for hot-end coating operations, BAT is to reduce emissions by using one or a combination of the following techniques: (i) Minimising the losses of the coating product by ensuring a good sealing of the application system and applying an effective extracting hood; (ii) Combining the flue-gas from the coating operations with the waste gas from the melting furnace or with the combustion air of the furnace, when a secondary treatment system is applied (filter and dry or semi-dry scrubber); (iii) Applying a secondary technique, e.g. wet scrubbing, dry scrubbing plus filtration","mg/Nm3","N/A",10,"Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3","N/A","Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.2.6",22,22]
[1001,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Container glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Dust","Particulates (PM10) (24 hr Mean)","Flue-gas cleaning system such as an electrostatic precipitator or a bag filter","mg/Nm3","10","20","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.2.1",17,17]
[100,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Container glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Dust","Particulates (PM10) (24 hr Mean)","Flue-gas cleaning system such as an electrostatic precipitator or a bag filter","kg/tonne melted glass","0.015","0.06","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The conversion factors of 1,5 × 10 –3 and 3 × 10 –3 have been used for the determination of the lower and higher value of the range respectively.","GLS (2012) - 2012/134/EU","1.2.1",17,17]
[1110,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Domestic glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Dusty downstreatm processes ","Emissions to air","Air","Dust","Particulates (PM10) (24 hr Mean)","For downstream dusty processes, BAT is to reduce emissions of dust and metals by using one or a combination of the following techniques: (i) Performing dusty operations (e.g. cutting, grinding, polishing) under liquid; (ii) Applying a bag filter system","mg/Nm3","1","10","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3","N/A","Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.5.6",38,38]
[1079,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Domestic glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Dust","Particulates (PM10) (24 hr Mean)","BAT is to reduce dust emissions from the waste gases of the melting furnace by using one or a combination of the following techniques: (i) Reduction of the volatile components by raw material; (ii) electric melting; (iii) Oxy-fuel melting; (iv) Filtration system: electrostatic precipator or bag filter; (v) Wet scrubbing system ","mg/Nm3","10","20","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","Considerations concerning the economic viability for achieving the BAT-AELs in the case of furnaces with a capacity of < 80 t/d, producing soda-lime glass, are reported.","GLS (2012) - 2012/134/EU","1.5.1",33,33]
[1079,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Domestic glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Dust","Particulates (PM10) (24 hr Mean)","BAT is to reduce dust emissions from the waste gases of the melting furnace by using one or a combination of the following techniques: (i) Reduction of the volatile components by raw material; (ii) electric melting; (iii) Oxy-fuel melting; (iv) Filtration system: electrostatic precipator or bag filter; (v) Wet scrubbing system ","kg/tonne melted glass","0.03","0.06","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","A conversion factor of 3 × 10 –3 has been applied (see Table 2). However, a case by case conversion factor may have to be applied for specific productions","GLS (2012) - 2012/134/EU","1.5.1",33,33]
[1081,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Domestic glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Dust","Particulates (PM10) (24 hr Mean)","BAT is to reduce dust emissions from the waste gases of the melting furnace by using one or a combination of the following techniques: (i) Reduction of the volatile components by raw material; (ii) electric melting; (iii) Oxy-fuel melting; (iv) Filtration system: electrostatic precipator or bag filter; (v) Wet scrubbing system ","mg/Nm3","1","10","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","This BAT-AEL applies to batch formulations containing significant amounts of constituents meeting the criteria as dangerous substances, in accordance with Regulation (EC) No 1272/2008 of the European Parliament and of the Council.","GLS (2012) - 2012/134/EU","1.5.1",33,33]
[1080,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Domestic glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Dust","Particulates (PM10) (24 hr Mean)","BAT is to reduce dust emissions from the waste gases of the melting furnace by using one or a combination of the following techniques: (i) Reduction of the volatile components by raw material; (ii) electric melting; (iii) Oxy-fuel melting; (iv) Filtration system: electrostatic precipator or bag filter; (v) Wet scrubbing system ","kg/tonne melted glass","0.003","0.03","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","This BAT-AEL applies to batch formulations containing significant amounts of constituents meeting the criteria as dangerous substances, in accordance with Regulation (EC) No 1272/2008 of the European Parliament and of the Council.\n\nA conversion factor of 3 × 10 –3 has been applied (see Table 2). However, a case by case conversion factor may have to be applied for specific productions.","GLS (2012) - 2012/134/EU","1.5.1",33,33]
[1078,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Filament glass fibre","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes (cutting and milling)","Emissions to air","Air","Dust","Particulates (PM10) (24 hr Mean)","BAT is to reduce emissions from downstream processes by using one or a combination of the following techniques: (i) Wet scrubbing systems; (ii) Wet electrostatic precipitator; (iii) Filtration system (bag filter)","mg/Nm3","5","20","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3","N/A","Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.4.6",32,32]
[1075,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Filament glass fibre","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes (forming and coating)","Emissions to air","Air","Dust","Particulates (PM10) (24 hr Mean)","BAT is to reduce emissions from downstream processes by using one or a combination of the following techniques: (i) Wet scrubbing systems; (ii) Wet electrostatic precipitator; (iii) Filtration system (bag filter)","mg/Nm3","5","20","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3","N/A","Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.4.6",32,32]
[1058,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Filament glass fibre","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Dust","Particulates (PM10) (24 hr Mean)","BAT is to reduce dust emissions from the waste gases of the melting furnace by using one or a combination of the following techniques: (i) Reduction of the volatile components by raw material; (ii) Filtration system: electrostatic precipitator or bag filter; (iii) Wet scrubbing system ","mg/Nm3","10","20","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","Values at levels of < 30 mg/Nm 3 (< 0,14 kg/tonne melted glass) have been reported for boron-free formulations, with the application of primary techniques.","GLS (2012) - 2012/134/EU","1.4.1",28,28]
[1052,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Flat glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes","Emissions to air","Air","Dust","Particulates (PM10) (24 hr Mean)","BAT is to reduce emissions to air from the downstream processes by using one or a combination of the following techniques: (i) Minimising the losses of coating products applied to the flat glass by ensuring a good sealing of the application system; (ii) Minimising the losses of SO2 from the annealing ler, by operating the control system in an optimum manner; (iii) Combining the SO2 emissions from the lehr with the waste fas from the melting furnace, when technically feasible and where a secondary treatment system is applied (filter and dry or semi-dry scrubber); (iv) Applying a secondary technique, e.g. wet scrubbing, or dry scrubbing and filtration","mg/Nm3","15","20","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3","N/A","Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.3.6",27,27]
[1030,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Flat glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Dust","Particulates (PM10) (24 hr Mean)","BAT is to reduce dust emissions from the waste gases of the melting furnace by applying an electrostatic precipitator or a bag filter system","mg/Nm3","10","20","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.3.1",23,23]
[1030,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Flat glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Dust","Particulates (PM10) (24 hr Mean)","BAT is to reduce dust emissions from the waste gases of the melting furnace by applying an electrostatic precipitator or a bag filter system","kg/tonne melted glass","0.025","0.05","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.3.1",23,23]
[1225,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Frits ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes ","Emissions to air","Air","Dust","Particulates (PM10) (24 hr Mean)","For downstream dusty processes, BAT is to reduce emissions by using one or a combination of the following techniques: (i) Applying wet milling techniques; (ii) Operating dry milling and dry product packaging under an efficient extraction system in conjunction with a fabric filter; (iii) Applying a filtration system","mg/Nm3","5","10","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3","N/A","Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.8.1",57,57]
[1207,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Frits ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Dust","Particulates (PM10) (24 hr Mean)","BAT is to reduce dust emissions from the waste gases of the melting furnace by means of an electrostatic precipitator or a bag filter system.","mg/Nm3","10","20","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.8.1",54,54]
[1207,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Frits ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Dust","Particulates (PM10) (24 hr Mean)","BAT is to reduce dust emissions from the waste gases of the melting furnace by means of an electrostatic precipitator or a bag filter system.","kg/tonne melted glass","0.05","0.15","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The conversion factors of 5 × 10 –3 and 7,5 × 10 –3 have been used for the determination of the lower and upper value of the BAT-AELs range (see Table 2). However, a case-by-case conversion factor may have to be applied based on the type of combustion.","GLS (2012) - 2012/134/EU","1.8.1",54,54]
[1195,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","HTIW wools","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes","Emissions to air","Air","Dust","Particulates (PM10) (24 hr Mean)","BAT is to reduce dust emissions from the waste gases of the melting furnace by applying a filtration system.","mg/Nm3","5","20","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3","N/A","Daily average (continuous)","The values are associated with the use of a bag filter system.","GLS (2012) - 2012/134/EU","1.8.1",50,50]
[1196,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","HTIW wools","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes","Emissions to air","Air","Dust","Particulates (PM10) (24 hr Mean)","For downstream dusty processes, BAT is to reduce emissions using one or a combination of the following techniques: (i) Minimising the losses of product by ensuring a good sealing of the production line, where technically applicable; (ii) Cutting, trimming and packaging under vacuum, by applying an efficient extraction system in conjunction with a fabric filter; (iii) Applying a fabric filter system","mg/Nm3","1","5","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3","N/A","Daily average (continuous)","BAT-AELs from dusty downstream processes in the HTIW sector, when treated separately\n\nThe lower level of the range is associated with emissions of aluminium silicate glass wool/refractory ceramic fibres","GLS (2012) - 2012/134/EU","1.8.1",51,51]
[1145,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Dust","Particulates (PM10) (24 hr Mean)","BAT is to reduce dust emissions from the waste gases of the melting furnace by applying an electrostatic precipitator or a bag filter system","mg/Nm3","10","20","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.7.1",44,44]
[1145,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Dust","Particulates (PM10) (24 hr Mean)","BAT is to reduce dust emissions from the waste gases of the melting furnace by applying an electrostatic precipitator or a bag filter system","kg/tonne melted glass","0.02","0.050","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The conversion factors of 2 × 10 –3 and 2,5 × 10 –3 have been used for the determination of the lower and upper value of the BAT-AELs range (see Table 2), in order to cover both the production of glass wool and stone wool.","GLS (2012) - 2012/134/EU","1.7.1",44,44]
[1141,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Special glass ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes","Emissions to air","Air","Dust","Particulates (PM10) (24 hr Mean)","For downstream dusty processes, BAT is to reduce emissions of dust and metals by using one or a combination of the following techniques: (i) Performing dusty operations (e.g. cutting, grinding, polishing) under liquid; (ii) Applying a bag filter system","mg/Nm3","1","10","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3","N/A","Daily average (continuous)","BAT-AELs for dust and metal emissions from downstream processes in the special glass sector, when treated separately","GLS (2012) - 2012/134/EU","1.6.6",44,44]
[1115,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Special glass ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Dust","Particulates (PM10) (24 hr Mean)","BAT is to reduce dust emissions from the waste gases of the melting furnace by using one or a combination of the following techniques: (i) Reduction of the volatile components by raw material modifications; (ii) Electric melting","mg/Nm3","10","20","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.6.1",39,39]
[1115,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Special glass ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Dust","Particulates (PM10) (24 hr Mean)","BAT is to reduce dust emissions from the waste gases of the melting furnace by using one or a combination of the following techniques: (i) Reduction of the volatile components by raw material modifications; (ii) Electric melting","kg/tonne melted glass","0.03","0.13","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The conversions factors of 2,5 × 10 –3 and 6,5 × 10 –3 have been used for the determination of the lower and upper value of the BAT-AELs range (see Table 2), with some values being approximated. However, a-case-by-case conversion factor needs to be applied, depending on the type of glass produced.","GLS (2012) - 2012/134/EU","1.6.1",39,39]
[1117,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Special glass ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Dust","Particulates (PM10) (24 hr Mean)","BAT is to reduce dust emissions from the waste gases of the melting furnace by using one or a combination of the following techniques: (i) Reduction of the volatile components by raw material modifications; (ii) Electric melting","mg/Nm3","1","10","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The BAT-AELs apply to batch formulations containing significant amounts of constituents meeting the criteria as dangerous substances, in accordance with Regulation (EC) No 1272/2008.","GLS (2012) - 2012/134/EU","1.6.1",39,39]
[1116,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Special glass ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Dust","Particulates (PM10) (24 hr Mean)","BAT is to reduce dust emissions from the waste gases of the melting furnace by using one or a combination of the following techniques: (i) Reduction of the volatile components by raw material modifications; (ii) Electric melting","kg/tonne melted glass","0.003","0.065","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The BAT-AELs apply to batch formulations containing significant amounts of constituents meeting the criteria as dangerous substances, in accordance with Regulation (EC) No 1272/2008.\n\nThe conversions factors of 2,5 × 10 –3 and 6,5 × 10 –3 have been used for the determination of the lower and upper value of the BAT-AELs range (see Table 2), with some values being approximated. However, a-case-by-case conversion factor needs to be applied, depending on the type of glass produced.","GLS (2012) - 2012/134/EU","1.6.1",39,39]
[1076,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Filament glass fibre","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes (forming and coating)","Emissions to air","Air","Formaldehyde","Formaldehyde","BAT is to reduce emissions from downstream processes by using one or a combination of the following techniques: (i) Wet scrubbing systems; (ii) Wet electrostatic precipitator; (iii) Filtration system (bag filter)","mg/Nm3","N/A","10","Amber",0,"273.15","101.3","N/A","Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.4.6",32,32]
[1185,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes- Curing oven emissions ","Emissions to air","Air","Formaldehyde","Formaldehyde","BAT is to reduce emissions from downstream processes by using one or a combination of the following techniques: (i) Impact jets and cyclones; (ii) Wet scrubbers; (iii) Wet electrostatic precipitators; (iv) Stone wool filters; (v) Waste gas incineration","mg/Nm3","2","5","Amber",0,"273.15","101.3","N/A","Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.7.7",50,50]
[1183,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes- Curing oven emissions ","Emissions to air","Air","Formaldehyde","Formaldehyde","BAT is to reduce emissions from downstream processes by using one or a combination of the following techniques: (i) Impact jets and cyclones; (ii) Wet scrubbers; (iii) Wet electrostatic precipitators; (iv) Stone wool filters; (v) Waste gas incineration","kg/tonne melted glass","N/A","0.03","Amber",0,"273.15","101.3","N/A","Daily average (continuous)","The specific mass emissions refer to 1 tonne of produced glass","GLS (2012) - 2012/134/EU","1.7.7",50,50]
[1177,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes- Forming area ","Emissions to air","Air","Formaldehyde","Formaldehyde","BAT is to reduce emissions from downstream processes by using one or a combination of the following techniques: (i) Impact jets and cyclones; (ii) Wet scrubbers; (iii) Wet electrostatic precipitators; (iv) Stone wool filters; (v) Waste gas incineration","mg/Nm3","2","5","Amber",0,"273.15","101.3","N/A","Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.7.7",49,49]
[1028,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Container glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes","Emissions to air","Air","Hydrogen chloride, expressed as HCl","Hydrogen chloride","When tin, organotin or titanium compounds are used for hot-end coating operations, BAT is to reduce emissions by using one or a combination of the following techniques: (i) Minimising the losses of the coating product by ensuring a good sealing of the application system and applying an effective extracting hood; (ii) Combining the flue-gas from the coating operations with the waste gas from the melting furnace or with the combustion air of the furnace, when a secondary treatment system is applied (filter and dry or semi-dry scrubber); (iii) Applying a secondary technique, e.g. wet scrubbing, dry scrubbing plus filtration","mg/Nm3","N/A",30,"Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3","N/A","Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.2.6",22,22]
[1017,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Container glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Hydrogen chloride, expressed as HCl","Hydrogen chloride","BAT is to reduce HCl and HF emissions from the melting furnace (possibly combined with flue-gases from hot-end coating activities) by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of chlorine and fluorine; (ii) Dry or semi-dry scrubbing, in a combination with filtration system","mg/Nm3","10","20","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The higher levels are associated with the simultaneous treatment of flue-gases from hot-end coating operations.","GLS (2012) - 2012/134/EU","1.2.4",21,21]
[108,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Container glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Hydrogen chloride, expressed as HCl","Hydrogen chloride","BAT is to reduce HCl and HF emissions from the melting furnace (possibly combined with flue-gases from hot-end coating activities) by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of chlorine and fluorine; (ii) Dry or semi-dry scrubbing, in a combination with filtration system","kg/tonne melted glass","0.02","0.03","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The higher levels are associated with the simultaneous treatment of flue-gases from hot-end coating operations.\n\nThe conversion factor for general cases, reported in Table 2 (1,5 × 10 –3 ) has been applied","GLS (2012) - 2012/134/EU","1.2.4",21,21]
[1099,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Domestic glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Hydrogen chloride, expressed as HCl","Hydrogen chloride","BAT is to reduce HCl and HF emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of chlorine and fluorine; (ii) Minimisation of the flourine content in the batch formulation and optimisation of the flourine mass balance; (iii) Dry or semi-dry scrubbing, in combination with a filtration system; (iv) Wet scrubbing ","mg/Nm3","10","20","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The lower levels are associated with the use of electric melting.\n\nIn cases where KCl or NaCl are used as a refining agents, the BAT-AEL is < 30 mg/Nm 3 or < 0,09 kg/tonne melted glass.","GLS (2012) - 2012/134/EU","1.5.4",36,36]
[1089,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Domestic glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Hydrogen chloride, expressed as HCl","Hydrogen chloride","BAT is to reduce HCl and HF emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of chlorine and fluorine; (ii) Minimisation of the flourine content in the batch formulation and optimisation of the flourine mass balance; (iii) Dry or semi-dry scrubbing, in combination with a filtration system; (iv) Wet scrubbing ","kg/tonne melted glass","0.03","0.06","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The lower levels are associated with the use of electric melting.\n\nIn cases where KCl or NaCl are used as a refining agents, the BAT-AEL is < 30 mg/Nm 3 or < 0,09 kg/tonne melted glass.\n\nA conversion factor of 3 × 10 –3 has been applied (see Table 2). However, a case-by-case conversion factor may have to be applied for specific productions.","GLS (2012) - 2012/134/EU","1.5.4",36,36]
[1067,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Filament glass fibre","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Hydrogen chloride, expressed as HCl","Hydrogen chloride","BAT is to reduce HCl and HF emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of chlorine and flourine; (ii) Minimisation of the flourine content in the batch formulation ","mg/Nm3","N/A","10","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.4.4",31,31]
[1063,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Filament glass fibre","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Hydrogen chloride, expressed as HCl","Hydrogen chloride","BAT is to reduce HCl and HF emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of chlorine and flourine; (ii) Minimisation of the flourine content in the batch formulation ","kg/tonne melted glass","N/A","0.05","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The conversion factor reported in Table 2 (4,5 × 10 –3 ) has been applied.","GLS (2012) - 2012/134/EU","1.4.4",31,31]
[1053,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Flat glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes","Emissions to air","Air","Hydrogen chloride, expressed as HCl","Hydrogen chloride","BAT is to reduce emissions to air from the downstream processes by using one or a combination of the following techniques: (i) Minimising the losses of coating products applied to the flat glass by ensuring a good sealing of the application system; (ii) Minimising the losses of SO2 from the annealing ler, by operating the control system in an optimum manner; (iii) Combining the SO2 emissions from the lehr with the waste fas from the melting furnace, when technically feasible and where a secondary treatment system is applied (filter and dry or semi-dry scrubber); (iv) Applying a secondary technique, e.g. wet scrubbing, or dry scrubbing and filtration","mg/Nm3","N/A","10","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3","N/A","Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.3.6",28,28]
[1043,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Flat glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Hydrogen chloride, expressed as HCl","Hydrogen chloride","BAT is to reduce HCl and HF emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of chlorine and flourine; (ii) Dry or semi-dry scrubbing in combination with a filtration system ","mg/Nm3","10","25","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The higher levels of the range are associated with the recycling of filter dust in the batch formulation","GLS (2012) - 2012/134/EU","1.3.4",26,26]
[1041,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Flat glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Hydrogen chloride, expressed as HCl","Hydrogen chloride","BAT is to reduce HCl and HF emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of chlorine and flourine; (ii) Dry or semi-dry scrubbing in combination with a filtration system ","kg/tonne melted glass","0.025","0.0625","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The conversion factor reported in Table 2 (2,5 × 10 –3 ) has been applied.\n\nThe higher levels of the range are associated with the recycling of filter dust in the batch formulation","GLS (2012) - 2012/134/EU","1.3.4",26,26]
[1217,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Frits ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Hydrogen chloride, expressed as HCl","Hydrogen chloride","BAT is to reduce HCl and HF emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of chlorine and fluorine; (ii) Minimisation of the fluorine compounds in the batch formulation when used to ensure the quality of the final product; (iii) Dry or semi-dry scrubbing, in combination with a filtration system","mg/Nm3","N/A","10","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.8.1",56,56]
[1212,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Frits ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Hydrogen chloride, expressed as HCl","Hydrogen chloride","BAT is to reduce HCl and HF emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of chlorine and fluorine; (ii) Minimisation of the fluorine compounds in the batch formulation when used to ensure the quality of the final product; (iii) Dry or semi-dry scrubbing, in combination with a filtration system","kg/tonne melted glass","N/A","0.05","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The conversion factor of 5 × 10 –3 has been used with some values being approximated. A case-by-case conversion factor may have to be applied based on the type of combustion","GLS (2012) - 2012/134/EU","1.8.1",56,56]
[1200,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","HTIW wools","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Hydrogen chloride, expressed as HCl","Hydrogen chloride","BAT is to reduce SO X emissions from the melting furnaces and downstream processes by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of sulphur; (ii) Use of low sulphur content fuel","mg/Nm3","N/A","10","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.8.1",52,52]
[1163,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Mineral wool","Glass wool ","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Hydrogen chloride, expressed as HCl","Hydrogen chloride","BAT is to reduce HCl and HF emissions from the melting furnace by using one or a combination of the following techniques:(i) Selection of raw materials for the batch formulation with a low content of chlorine and fluorine; (ii) Dry or semi-dry scrubbing, in combination with a filtration system","mg/Nm3","5","10","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.7.4",47,47]
[1154,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Mineral wool","Glass wool ","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Hydrogen chloride, expressed as HCl","Hydrogen chloride","BAT is to reduce HCl and HF emissions from the melting furnace by using one or a combination of the following techniques:(i) Selection of raw materials for the batch formulation with a low content of chlorine and fluorine; (ii) Dry or semi-dry scrubbing, in combination with a filtration system","kg/tonne melted glass","0.01","0.02","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The conversion factors of 2 × 10 –3 for glass wool and 2,5 × 10 –3 for stone wool have been used (","GLS (2012) - 2012/134/EU","1.7.4",47,47]
[1165,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Mineral wool","Stone wool","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Hydrogen chloride, expressed as HCl","Hydrogen chloride","BAT is to reduce HCl and HF emissions from the melting furnace by using one or a combination of the following techniques:(i) Selection of raw materials for the batch formulation with a low content of chlorine and fluorine; (ii) Dry or semi-dry scrubbing, in combination with a filtration system","mg/Nm3","10","30","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.7.4",47,47]
[1155,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Mineral wool","Stone wool","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Hydrogen chloride, expressed as HCl","Hydrogen chloride","BAT is to reduce HCl and HF emissions from the melting furnace by using one or a combination of the following techniques:(i) Selection of raw materials for the batch formulation with a low content of chlorine and fluorine; (ii) Dry or semi-dry scrubbing, in combination with a filtration system","kg/tonne melted glass","0.025","0.075","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The conversion factors of 2 × 10 –3 for glass wool and 2,5 × 10 –3 for stone wool have been used","GLS (2012) - 2012/134/EU","1.7.4",47,47]
[1133,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Special glass ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Hydrogen chloride, expressed as HCl","Hydrogen chloride","BAT is to reduce HCl and HF emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of chlorine and fluorine; (ii) Minimisation of the fluorine and/or chlorine compounds in the batch formulation and optimisation of the fluorine and/or chlorine mass balance; (iii) Dry or semi-dry scrubbing, in combination with a filtration system","mg/Nm3","10","20","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The higher levels are associated with the use of materials containing chlorine in the batch formulation.","GLS (2012) - 2012/134/EU","1.6.4",43,43]
[1124,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Special glass ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Hydrogen chloride, expressed as HCl","Hydrogen chloride","BAT is to reduce HCl and HF emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of chlorine and fluorine; (ii) Minimisation of the fluorine and/or chlorine compounds in the batch formulation and optimisation of the fluorine and/or chlorine mass balance; (iii) Dry or semi-dry scrubbing, in combination with a filtration system","kg/tonne melted glass","0.03","0.05","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The higher levels are associated with the use of materials containing chlorine in the batch formulation.\n\nThe conversion factor of 2,5 × 10 –3 (see Table 2) has been used; with some values being approximated. A case-by-case conversion factor may have to be applied based on the type of production.","GLS (2012) - 2012/134/EU","1.6.4",43,43]
[1114,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Domestic glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Acid polishing processes","Emissions to air","Air","Hydrogen flouride, expressed as HF","Hydrogen fluoride (as F) (Ecological - Daily Mean)","For acid polishing processes, BAT is to reduce HF emissions by using one or a combination of the following techniques: (i) Minimising the losses of polishing product by ensuring a good sealing of the application system; (ii) Applying a secondary technique, e.g. wet scrubbing","mg/Nm3","N/A","5","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3","N/A","Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.5.6",39,39]
[1101,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Domestic glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Hydrogen flouride, expressed as HF","Hydrogen fluoride (as F) (Ecological - Daily Mean)","BAT is to reduce HCl and HF emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of chlorine and fluorine; (ii) Minimisation of the flourine content in the batch formulation and optimisation of the flourine mass balance; (iii) Dry or semi-dry scrubbing, in combination with a filtration system; (iv) Wet scrubbing ","mg/Nm3","1","5","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The lower levels are associated with the use of electric melting. The higher levels are associated with the production of opal glass, the recycling of filter dust or where high levels of external cullet are used in the batch formulation.","GLS (2012) - 2012/134/EU","1.5.4",36,36]
[1090,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Domestic glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Hydrogen flouride, expressed as HF","Hydrogen fluoride (as F) (Ecological - Daily Mean)","BAT is to reduce HCl and HF emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of chlorine and fluorine; (ii) Minimisation of the flourine content in the batch formulation and optimisation of the flourine mass balance; (iii) Dry or semi-dry scrubbing, in combination with a filtration system; (iv) Wet scrubbing ","kg/tonne melted glass","0.003","0.015","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The lower levels are associated with the use of electric melting. The higher levels are associated with the production of opal glass, the recycling of filter dust or where high levels of external cullet are used in the batch formulation.\n\nA conversion factor of 3 × 10 –3 has been applied (see Table 2). However, a case-by-case conversion factor may have to be applied for specific productions.","GLS (2012) - 2012/134/EU","1.5.4",36,36]
[1069,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Filament glass fibre","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Hydrogen flouride, expressed as HF","Hydrogen fluoride (as F) (Ecological - Daily Mean)","BAT is to reduce HCl and HF emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of chlorine and flourine; (ii) Minimisation of the flourine content in the batch formulation ","mg/Nm3","5","15","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The higher levels of the range are associated with the use of fluorine compounds in the batch formulation.","GLS (2012) - 2012/134/EU","1.4.4",31,31]
[1064,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Filament glass fibre","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Hydrogen flouride, expressed as HF","Hydrogen fluoride (as F) (Ecological - Daily Mean)","BAT is to reduce HCl and HF emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of chlorine and flourine; (ii) Minimisation of the flourine content in the batch formulation ","kg/tonne melted glass","0.02","0.07","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The conversion factor reported in Table 2 (4,5 × 10 –3 ) has been applied.\n\nThe higher levels of the range are associated with the use of fluorine compounds in the batch formulation.","GLS (2012) - 2012/134/EU","1.4.4",31,31]
[1054,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Flat glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes","Emissions to air","Air","Hydrogen flouride, expressed as HF","Hydrogen fluoride (as F) (Ecological - Daily Mean)","BAT is to reduce emissions to air from the downstream processes by using one or a combination of the following techniques: (i) Minimising the losses of coating products applied to the flat glass by ensuring a good sealing of the application system; (ii) Minimising the losses of SO2 from the annealing ler, by operating the control system in an optimum manner; (iii) Combining the SO2 emissions from the lehr with the waste fas from the melting furnace, when technically feasible and where a secondary treatment system is applied (filter and dry or semi-dry scrubber); (iv) Applying a secondary technique, e.g. wet scrubbing, or dry scrubbing and filtration","mg/Nm3","1","5","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3","N/A","Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.3.6",28,28]
[1045,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Flat glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Hydrogen flouride, expressed as HF","Hydrogen fluoride (as F) (Ecological - Daily Mean)","BAT is to reduce HCl and HF emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of chlorine and flourine; (ii) Dry or semi-dry scrubbing in combination with a filtration system ","mg/Nm3","1","4","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.3.4",26,26]
[1042,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Flat glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Hydrogen flouride, expressed as HF","Hydrogen fluoride (as F) (Ecological - Daily Mean)","BAT is to reduce HCl and HF emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of chlorine and flourine; (ii) Dry or semi-dry scrubbing in combination with a filtration system ","kg/tonne melted glass","0.0025","0.010","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The conversion factor reported in Table 2 (2,5 × 10 –3 ) has been applied.","GLS (2012) - 2012/134/EU","1.3.4",26,26]
[1219,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Frits ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Hydrogen flouride, expressed as HF","Hydrogen fluoride (as F) (Ecological - Daily Mean)","BAT is to reduce HCl and HF emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of chlorine and fluorine; (ii) Minimisation of the fluorine compounds in the batch formulation when used to ensure the quality of the final product; (iii) Dry or semi-dry scrubbing, in combination with a filtration system","mg/Nm3","N/A","5","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.8.1",56,56]
[1213,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Frits ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Hydrogen flouride, expressed as HF","Hydrogen fluoride (as F) (Ecological - Daily Mean)","BAT is to reduce HCl and HF emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of chlorine and fluorine; (ii) Minimisation of the fluorine compounds in the batch formulation when used to ensure the quality of the final product; (iii) Dry or semi-dry scrubbing, in combination with a filtration system","kg/tonne melted glass","N/A","0.03","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The conversion factor of 5 × 10 –3 has been used with some values being approximated. A case-by-case conversion factor may have to be applied based on the type of combustion","GLS (2012) - 2012/134/EU","1.8.1",56,56]
[1201,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","HTIW wools","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Hydrogen flouride, expressed as HF","Hydrogen fluoride (as F) (Ecological - Daily Mean)","BAT is to reduce SO X emissions from the melting furnaces and downstream processes by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of sulphur; (ii) Use of low sulphur content fuel","mg/Nm3","N/A","5","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.8.1",52,52]
[1156,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Mineral wool","All products","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Hydrogen flouride, expressed as HF","Hydrogen fluoride (as F) (Ecological - Daily Mean)","BAT is to reduce HCl and HF emissions from the melting furnace by using one or a combination of the following techniques:(i) Selection of raw materials for the batch formulation with a low content of chlorine and fluorine; (ii) Dry or semi-dry scrubbing, in combination with a filtration system","kg/tonne melted glass","0.002","0.013","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The conversion factors of 2 × 10 –3 and 2,5 × 10 –3 have been used for the determination of the lower and upper values of the BAT-AELs range\n\nThe conversion factors of 2 × 10 –3 for glass wool and 2,5 × 10 –3 for stone wool have been used","GLS (2012) - 2012/134/EU","1.7.4",47,47]
[1167,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Mineral wool","Glass wool ","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Hydrogen flouride, expressed as HF","Hydrogen fluoride (as F) (Ecological - Daily Mean)","BAT is to reduce HCl and HF emissions from the melting furnace by using one or a combination of the following techniques:(i) Selection of raw materials for the batch formulation with a low content of chlorine and fluorine; (ii) Dry or semi-dry scrubbing, in combination with a filtration system","mg/Nm3","1","5","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.7.4",47,47]
[1144,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Special glass ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Acid polishing processes","Emissions to air","Air","Hydrogen flouride, expressed as HF","Hydrogen fluoride (as F) (Ecological - Daily Mean)","For acid polishing processes, BAT is to reduce HF emissions by using one or a combination of the following techniques: (i) Minimising the losses of polishing product by ensuring a good sealing of the application system; (ii) Applying a secondary technique, e.g. wet scrubbing","mg/Nm3","N/A","5","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3","N/A","Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.6.6",44,44]
[1135,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Special glass ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Hydrogen flouride, expressed as HF","Hydrogen fluoride (as F) (Ecological - Daily Mean)","BAT is to reduce HCl and HF emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of chlorine and fluorine; (ii) Minimisation of the fluorine and/or chlorine compounds in the batch formulation and optimisation of the fluorine and/or chlorine mass balance; (iii) Dry or semi-dry scrubbing, in combination with a filtration system","mg/Nm3","1","5","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.6.4",43,43]
[1125,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Special glass ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Hydrogen flouride, expressed as HF","Hydrogen fluoride (as F) (Ecological - Daily Mean)","BAT is to reduce HCl and HF emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of chlorine and fluorine; (ii) Minimisation of the fluorine and/or chlorine compounds in the batch formulation and optimisation of the fluorine and/or chlorine mass balance; (iii) Dry or semi-dry scrubbing, in combination with a filtration system","kg/tonne melted glass","0.003","0.04","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The upper value of the range has been derived from specific reported data.","GLS (2012) - 2012/134/EU","1.6.4",43,43]
[1019,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Container glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Hydrogen fluoride, expressed as HF","Hydrogen fluoride (as F) (Ecological - Daily Mean)","BAT is to reduce HCl and HF emissions from the melting furnace (possibly combined with flue-gases from hot-end coating activities) by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of chlorine and fluorine; (ii) Dry or semi-dry scrubbing, in a combination with filtration system","mg/Nm3","1","5","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.2.4",21,21]
[109,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Container glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Hydrogen fluoride, expressed as HF","Hydrogen fluoride (as F) (Ecological - Daily Mean)","BAT is to reduce HCl and HF emissions from the melting furnace (possibly combined with flue-gases from hot-end coating activities) by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of chlorine and fluorine; (ii) Dry or semi-dry scrubbing, in a combination with filtration system","kg/tonne melted glass","0.001","0.008","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The conversion factor for general cases, reported in Table 2 (1,5 × 10 –3 ) has been applied.\n\nThe higher levels are associated with the simultaneous treatment of flue-gases from hot-end coating operations","GLS (2012) - 2012/134/EU","1.2.4",21,21]
[1169,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Mineral wool","Stone wool","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Hydrogen sulphide, expressed as H2S","Hydrogen sulphide","BAT is to reduce H 2 S emissions from the melting furnace by applying a waste gas incineration system to oxidise hydrogen sulphide to SO 2","mg/Nm3","N/A","2","Amber",0,"273.15","101.3",0.08,"Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.7.5",48,48]
[1157,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Mineral wool","Stone wool","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Hydrogen sulphide, expressed as H2S","Hydrogen sulphide","BAT is to reduce H 2 S emissions from the melting furnace by applying a waste gas incineration system to oxidise hydrogen sulphide to SO 2","kg/tonne melted glass","N/A","0.005","Amber",0,"273.15","101.3",0.08,"Daily average (continuous)","The conversion factor of 2,5 × 10 –3 for stone wool has been applied","GLS (2012) - 2012/134/EU","1.7.5",48,48]
[1113,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Domestic glass","Lead crystal glass","Unspecified","Unspecified","Unspecified","Unspecified","Dusty downstreatm processes ","Emissions to air","Air","Lead compounds, expressed as Pb","Lead","For downstream dusty processes, BAT is to reduce emissions of dust and metals by using one or a combination of the following techniques: (i) Performing dusty operations (e.g. cutting, grinding, polishing) under liquid; (ii) Applying a bag filter system","mg/Nm3","1","1.5","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3","N/A","Daily average (continuous)","The levels refer to downstream operations on lead crystal glass.","GLS (2012) - 2012/134/EU","1.5.6",38,38]
[1108,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Domestic glass","Lead crystal glass","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Lead compounds, expressed as Pb","Lead","When lead compounds are used for the manufacturing of lead crystal glass, BAT is to reduce lead emissions from the melting furnace by using one or a combination of the following techniques: (i) Electric melting; (ii) Bag filter; (iii) Electrostatic precipitator; (iv) Dry or semi-dry scrubbing in combination with a filtration system","mg/Nm3","0.5","1","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The values refer to the sum of lead present in the flue-gases in both solid and gaseous phases.","GLS (2012) - 2012/134/EU","1.5.5",38,38]
[1108,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Domestic glass","Lead crystal glass","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Lead compounds, expressed as Pb","Lead","When lead compounds are used for the manufacturing of lead crystal glass, BAT is to reduce lead emissions from the melting furnace by using one or a combination of the following techniques: (i) Electric melting; (ii) Bag filter; (iii) Electrostatic precipitator; (iv) Dry or semi-dry scrubbing in combination with a filtration system","kg/tonne melted glass",1E-3,3.0000000000000001E-3,"Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The values refer to the sum of lead present in the flue-gases in both solid and gaseous phases.\n\nA conversion factor of 3 × 10 –3 has been applied (see Table 2). However, a case-by-case conversion factor may have to be applied for specific productions.","GLS (2012) - 2012/134/EU","1.5.5",38,38]
[1073,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Filament glass fibre","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Metals (Group 1 + Group 2)","Metals (Group 1 + Group 2)","BAT is to reduce metal emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of metals; (ii) Applying a dry or semi-dry scrubbing in combination with filtration system; (iii) Applying wet scrubbing","mg/Nm3","1","3","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The levels refer to the sum of metals present in the flue-gases in both solid and gaseous phases","GLS (2012) - 2012/134/EU","1.4.5",31,31]
[1066,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Filament glass fibre","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Metals (Group 1 + Group 2)","Metals (Group 1 + Group 2)","BAT is to reduce metal emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of metals; (ii) Applying a dry or semi-dry scrubbing in combination with filtration system; (iii) Applying wet scrubbing","kg/tonne melted glass",4.5000000000000005E-3,1.35E-4,"Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The levels refer to the sum of metals present in the flue-gases in both solid and gaseous phases.\n\nThe conversion factor reported in Table 2 (4,5 × 10 –3 ) has been applied.","GLS (2012) - 2012/134/EU","1.4.5",31,31]
[1057,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Flat glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes","Emissions to air","Air","Metals (Group 1 + Group 2)","Metals (Group 1 + Group 2)","BAT is to reduce emissions to air from the downstream processes by using one or a combination of the following techniques: (i) Minimising the losses of coating products applied to the flat glass by ensuring a good sealing of the application system; (ii) Minimising the losses of SO2 from the annealing ler, by operating the control system in an optimum manner; (iii) Combining the SO2 emissions from the lehr with the waste fas from the melting furnace, when technically feasible and where a secondary treatment system is applied (filter and dry or semi-dry scrubber); (iv) Applying a secondary technique, e.g. wet scrubbing, or dry scrubbing and filtration","mg/Nm3","N/A","5","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3","N/A","Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.3.6",28,28]
[1023,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Container glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Metals (Group 1 + Group 2) ","Metals (Group 1 + Group 2)","BAT is to reduce metal emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of metals; (ii) Minimising the use of metal compounds in the batch formulation, where colouring and decolourising of glass is needed, subject to consumer glass quality requirements; (iii) Applying a filtration system (bag filter or electrostatic precipitator); (iv) Applying a dry or semi-dry scrubbing, in combination with a filtration system","mg/Nm3","1","5","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The levels refer to the sum of metals present in the flue-gases in both solid and gaseous phases.\n\nThe lower levels are BAT-AELs when metal compounds are not intentionally used in the batch formulation.\n\nThe upper levels are associated with the use of metals for colouring or decolourising the glass, or when the flue-gases from the hot-end coating operations are treated together with the melting furnace emissions","GLS (2012) - 2012/134/EU","1.2.5",21,21]
[111,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Container glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Metals (Group 1 + Group 2) ","Metals (Group 1 + Group 2)","BAT is to reduce metal emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of metals; (ii) Minimising the use of metal compounds in the batch formulation, where colouring and decolourising of glass is needed, subject to consumer glass quality requirements; (iii) Applying a filtration system (bag filter or electrostatic precipitator); (iv) Applying a dry or semi-dry scrubbing, in combination with a filtration system","kg/tonne melted glass",1.5E-3,7.4999999999999997E-3,"Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The levels refer to the sum of metals present in the flue-gases in both solid and gaseous phases.\n\nThe lower levels are BAT-AELs when metal compounds are not intentionally used in the batch formulation.\n\nThe upper levels are associated with the use of metals for colouring or decolourising the glass, or when the flue-gases from the hot-end coating operations are treated together with the melting furnace emissions\n\nThe conversion factor for general cases, reported in Table 2 (1,5 × 10 –3 ) has been applied","GLS (2012) - 2012/134/EU","1.2.5",21,21]
[1112,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Domestic glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Dusty downstreatm processes ","Emissions to air","Air","Metals (Group 1 + Group 2) ","Metals (Group 1 + Group 2)","For downstream dusty processes, BAT is to reduce emissions of dust and metals by using one or a combination of the following techniques: (i) Performing dusty operations (e.g. cutting, grinding, polishing) under liquid; (ii) Applying a bag filter system","mg/Nm3","1","5","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3","N/A","Daily average (continuous)","The levels refer to the sum of metals present in the waste gas.","GLS (2012) - 2012/134/EU","1.5.6",38,38]
[1223,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Frits ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Metals (Group 1 + Group 2) ","Metals (Group 1 + Group 2)","BAT is to reduce metal emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of metals; (ii) Minimising of the use of metal compounds in the batch formulation, where colouring is required or other specific characteristics are conferred to the frit; (iii) Dry or semi-dry scrubbing, in combination with a filtration system","mg/Nm3","N/A","5","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The levels refer to the sum of metals present in the flue-gases in both solid and gaseous phases","GLS (2012) - 2012/134/EU","1.8.1",57,57]
[1215,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Frits ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Metals (Group 1 + Group 2) ","Metals (Group 1 + Group 2)","BAT is to reduce metal emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of metals; (ii) Minimising of the use of metal compounds in the batch formulation, where colouring is required or other specific characteristics are conferred to the frit; (iii) Dry or semi-dry scrubbing, in combination with a filtration system","kg/tonne melted glass","N/A",3.6999999999999998E-2,"Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The levels refer to the sum of metals present in the flue-gases in both solid and gaseous phases","GLS (2012) - 2012/134/EU","1.8.1",57,57]
[1205,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","HTIW wools","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes ","Emissions to air","Air","Metals (Group 1 + Group 2) ","Metals (Group 1 + Group 2)","BAT is to reduce metal emissions from the melting furnace and/or downstream processes by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of metals; (ii) Applying a filtration system","mg/Nm3","N/A","5","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3","N/A","Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.8.1",53,53]
[1204,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","HTIW wools","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Metals (Group 1 + Group 2) ","Metals (Group 1 + Group 2)","BAT is to reduce metal emissions from the melting furnace and/or downstream processes by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of metals; (ii) Applying a filtration system","mg/Nm3","N/A","5","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.8.1",53,53]
[1173,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Metals (Group 1 + Group 2) ","Metals (Group 1 + Group 2)","BAT is to reduce metal emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of metals; (ii) Application of a filtration system","mg/Nm3","1","2","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The ranges refer to the sum of metals present in the flue-gases in both solid and gaseous phases\n\nThe conversion factors of 2 × 10 –3 and 2,5 × 10 –3 have been used for the determination of the lower and upper values of the BAT-AELs range\n\nHigher values are associated with the use of cupola furnaces for the production of stone wool.\nEN L 70/48 Official Journal of the European Union 8.3.2012","GLS (2012) - 2012/134/EU","1.7.6",48,48]
[1159,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Metals (Group 1 + Group 2) ","Metals (Group 1 + Group 2)","BAT is to reduce metal emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of metals; (ii) Application of a filtration system","kg/tonne melted glass",2E-3,5.0000000000000001E-3,"Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The ranges refer to the sum of metals present in the flue-gases in both solid and gaseous phases\n\nThe conversion factors of 2 × 10 –3 and 2,5 × 10 –3 have been used for the determination of the lower and upper values of the BAT-AELs range\n","GLS (2012) - 2012/134/EU","1.7.6",48,48]
[1143,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Special glass ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes","Emissions to air","Air","Metals (Group 1 + Group 2) ","Metals (Group 1 + Group 2)","For downstream dusty processes, BAT is to reduce emissions of dust and metals by using one or a combination of the following techniques: (i) Performing dusty operations (e.g. cutting, grinding, polishing) under liquid; (ii) Applying a bag filter system","mg/Nm3","1","5","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3","N/A","Daily average (continuous)","\nBAT-AELs for dust and metal emissions from downstream processes in the special glass sector, when treated separately\n\nThe levels refer to the sum of metals present in the waste gas.\n55.","GLS (2012) - 2012/134/EU","1.6.6",44,44]
[1139,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Special glass ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Metals (Group 1 + Group 2) ","Metals (Group 1 + Group 2)","BAT is to reduce metal emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of metals; (ii) Minimising the use of metal compounds in the batch formulation, through a suitable selection of the raw materials where colouring and decolourising of glass is needed or where specific characteristics are conferred to the glass; (iii) Dry or semi-dry scrubbing, in combination with a filtration system","mg/Nm3","1","5","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The levels refer to the sum of metals present in the flue-gases in both solid and gaseous phases.\n\nThe lower levels are BAT-AELs when metal compounds are not intentionally used in the batch formulation.","GLS (2012) - 2012/134/EU","1.6.5",43,43]
[1127,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Special glass ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Metals (Group 1 + Group 2) ","Metals (Group 1 + Group 2)","BAT is to reduce metal emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of metals; (ii) Minimising the use of metal compounds in the batch formulation, through a suitable selection of the raw materials where colouring and decolourising of glass is needed or where specific characteristics are conferred to the glass; (iii) Dry or semi-dry scrubbing, in combination with a filtration system","kg/tonne melted glass",3.0000000000000001E-3,1.4999999999999999E-2,"Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The levels refer to the sum of metals present in the flue-gases in both solid and gaseous phases.\n\nThe lower levels are BAT-AELs when metal compounds are not intentionally used in the batch formulation.\n\nThe conversion factor of 2,5 × 10 –3 (see Table 2) has been used, with some values indicated in the table having been approximated. A case-by-case conversion factor may have to be applied based on the type of production.","GLS (2012) - 2012/134/EU","1.6.5",43,43]
[1226,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Frits ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes ","Emissions to air","Air","Metals (Group 1)","Metals (Group 1)","For downstream dusty processes, BAT is to reduce emissions by using one or a combination of the following techniques: (i) Applying wet milling techniques; (ii) Operating dry milling and dry product packaging under an efficient extraction system in conjunction with a fabric filter; (iii) Applying a filtration system","mg/Nm3","N/A","1","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3","N/A","Daily average (continuous)","The levels refer to the sum of metals present in the waste gas.","GLS (2012) - 2012/134/EU","1.8.1",57,57]
[1021,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Container glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Metals (Group 1) ","Metals (Group 1)","BAT is to reduce metal emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of metals; (ii) Minimising the use of metal compounds in the batch formulation, where colouring and decolourising of glass is needed, subject to consumer glass quality requirements; (iii) Applying a filtration system (bag filter or electrostatic precipitator); (iv) Applying a dry or semi-dry scrubbing, in combination with a filtration system","mg/Nm3","0.2","1","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The levels refer to the sum of metals present in the flue-gases in both solid and gaseous phases.\n\nThe lower levels are BAT-AELs when metal compounds are not intentionally used in the batch formulation.\n\nThe upper levels are associated with the use of metals for colouring or decolourising the glass, or when the flue-gases from the hot-end coating operations are treated together with the melting furnace emissions\n\nIn specific cases, when high quality flint glass is produced requiring higher amounts of selenium for decolourising (depending on the raw materials), higher values are reported, up to 3","GLS (2012) - 2012/134/EU","1.2.5",21,21]
[110,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Container glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Metals (Group 1) ","Metals (Group 1)","BAT is to reduce metal emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of metals; (ii) Minimising the use of metal compounds in the batch formulation, where colouring and decolourising of glass is needed, subject to consumer glass quality requirements; (iii) Applying a filtration system (bag filter or electrostatic precipitator); (iv) Applying a dry or semi-dry scrubbing, in combination with a filtration system","kg/tonne melted glass",2.9999999999999997E-4,1.5E-3,"Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The levels refer to the sum of metals present in the flue-gases in both solid and gaseous phases.\n\nThe lower levels are BAT-AELs when metal compounds are not intentionally used in the batch formulation.\n\nThe upper levels are associated with the use of metals for colouring or decolourising the glass, or when the flue-gases from the hot-end coating operations are treated together with the melting furnace emissions\n\nThe conversion factor for general cases, reported in Table 2 (1,5 × 10 –3 ) has been applied","GLS (2012) - 2012/134/EU","1.2.5",21,21]
[1111,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Domestic glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Dusty downstreatm processes ","Emissions to air","Air","Metals (Group 1) ","Metals (Group 1)","For downstream dusty processes, BAT is to reduce emissions of dust and metals by using one or a combination of the following techniques: (i) Performing dusty operations (e.g. cutting, grinding, polishing) under liquid; (ii) Applying a bag filter system","mg/Nm3","N/A","1","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3","N/A","Daily average (continuous)","The levels refer to the sum of metals present in the waste gas.","GLS (2012) - 2012/134/EU","1.5.6",38,38]
[1103,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Domestic glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Metals (Group 1) ","Metals (Group 1)","BAT is to reduce metal emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of metals; (ii) Minimising the use of metal compounds in the batch formulation, through a suitable selection of the raw materials where colouring and decolourising of glass is needed or where specific characteristics are conferred to the glass; (iii) Dry or semi-dry scrubbing, in combination with a filtration system ","mg/Nm3","0.2","1","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","BAT-AELs for metal emissions from the melting furnace in the domestic glass sector with the exception of glasses where selenium is used for decolourising\n\nThe levels refer to the sum of metals present in the flue-gases in both solid and gaseous phases.","GLS (2012) - 2012/134/EU","1.5.5",37,37]
[1091,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Domestic glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Metals (Group 1) ","Metals (Group 1)","BAT is to reduce metal emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of metals; (ii) Minimising the use of metal compounds in the batch formulation, through a suitable selection of the raw materials where colouring and decolourising of glass is needed or where specific characteristics are conferred to the glass; (iii) Dry or semi-dry scrubbing, in combination with a filtration system ","kg/tonne melted glass",5.9999999999999995E-4,3.0000000000000001E-3,"Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","BAT-AELs for metal emissions from the melting furnace in the domestic glass sector with the exception of glasses where selenium is used for decolourising\n\nThe levels refer to the sum of metals present in the flue-gases in both solid and gaseous phases.\n\nA conversion factor of 3 × 10 –3 has been applied (see Table 2). However, a case-by-case conversion factor may have to be applied for specific productions.","GLS (2012) - 2012/134/EU","1.5.5",37,37]
[1071,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Filament glass fibre","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Metals (Group 1) ","Metals (Group 1)","BAT is to reduce metal emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of metals; (ii) Applying a dry or semi-dry scrubbing in combination with filtration system; (iii) Applying wet scrubbing","mg/Nm3","0.2","1","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The levels refer to the sum of metals present in the flue-gases in both solid and gaseous phases","GLS (2012) - 2012/134/EU","1.4.5",31,31]
[1065,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Filament glass fibre","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Metals (Group 1) ","Metals (Group 1)","BAT is to reduce metal emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of metals; (ii) Applying a dry or semi-dry scrubbing in combination with filtration system; (iii) Applying wet scrubbing","kg/tonne melted glass",9.0000000000000008E-4,4.5000000000000005E-3,"Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The levels refer to the sum of metals present in the flue-gases in both solid and gaseous phases. \n\nThe conversion factor reported in Table 2 (4,5 × 10 –3 ) has been applied.\n","GLS (2012) - 2012/134/EU","1.4.5",31,31]
[1056,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Flat glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes","Emissions to air","Air","Metals (Group 1) ","Metals (Group 1)","BAT is to reduce emissions to air from the downstream processes by using one or a combination of the following techniques: (i) Minimising the losses of coating products applied to the flat glass by ensuring a good sealing of the application system; (ii) Minimising the losses of SO2 from the annealing ler, by operating the control system in an optimum manner; (iii) Combining the SO2 emissions from the lehr with the waste fas from the melting furnace, when technically feasible and where a secondary treatment system is applied (filter and dry or semi-dry scrubber); (iv) Applying a secondary technique, e.g. wet scrubbing, or dry scrubbing and filtration","mg/Nm3","N/A","1","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3","N/A","Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.3.6",28,28]
[1047,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Flat glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Metals (Group 1) ","Metals (Group 1)","BAT is to reduce metal emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of metals; (ii) Applying a filtration system; (iii) Applying a dry or semi-dry scrubbing in combination with a filtration system ","mg/Nm3","0.2","1","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","BAT-AELs for metal emissions from the melting furnace in the flat glass sector, with the exception of selenium coloured glasses\n\nThe ranges refer to the sum of metals present in the flue-gases in both solid and gaseous phases.","GLS (2012) - 2012/134/EU","1.3.5",26,26]
[1043,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Flat glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Metals (Group 1) ","Metals (Group 1)","BAT is to reduce metal emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of metals; (ii) Applying a filtration system; (iii) Applying a dry or semi-dry scrubbing in combination with a filtration system ","kg/tonne melted glass",5.0000000000000001E-4,2.5000000000000001E-3,"Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","BAT-AELs for metal emissions from the melting furnace in the flat glass sector, with the exception of selenium coloured glasses\n\nThe ranges refer to the sum of metals present in the flue-gases in both solid and gaseous phases.\n\nThe conversion factor reported in Table 2 (2,5 × 10 –3 ) has been applied","GLS (2012) - 2012/134/EU","1.3.5",26,26]
[1221,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Frits ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Metals (Group 1) ","Metals (Group 1)","BAT is to reduce metal emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of metals; (ii) Minimising of the use of metal compounds in the batch formulation, where colouring is required or other specific characteristics are conferred to the frit; (iii) Dry or semi-dry scrubbing, in combination with a filtration system","mg/Nm3","N/A","1","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The levels refer to the sum of metals present in the flue-gases in both solid and gaseous phases","GLS (2012) - 2012/134/EU","1.8.1",57,57]
[1214,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Frits ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Metals (Group 1) ","Metals (Group 1)","BAT is to reduce metal emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of metals; (ii) Minimising of the use of metal compounds in the batch formulation, where colouring is required or other specific characteristics are conferred to the frit; (iii) Dry or semi-dry scrubbing, in combination with a filtration system","kg/tonne melted glass","N/A",7.4999999999999997E-3,"Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The levels refer to the sum of metals present in the flue-gases in both solid and gaseous phases\n\nThe conversion factor of 7,5 × 10 –3 has been used. A case-by-case conversion factor may have to be applied based on the type of combustion","GLS (2012) - 2012/134/EU","1.8.1",57,57]
[1203,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","HTIW wools","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes ","Emissions to air","Air","Metals (Group 1) ","Metals (Group 1)","BAT is to reduce metal emissions from the melting furnace and/or downstream processes by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of metals; (ii) Applying a filtration system","mg/Nm3","N/A","1","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3","N/A","Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.8.1",53,53]
[1202,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","HTIW wools","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Metals (Group 1) ","Metals (Group 1)","BAT is to reduce metal emissions from the melting furnace and/or downstream processes by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of metals; (ii) Applying a filtration system","mg/Nm3","N/A","1","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.8.1",53,53]
[1171,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Metals (Group 1) ","Metals (Group 1)","BAT is to reduce metal emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of metals; (ii) Application of a filtration system","mg/Nm3","0.2","1","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The ranges refer to the sum of metals present in the flue-gases in both solid and gaseous phases\n\nHigher values are associated with the use of cupola furnaces for the production of stone wool","GLS (2012) - 2012/134/EU","1.7.6",48,48]
[1158,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Metals (Group 1) ","Metals (Group 1)","BAT is to reduce metal emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of metals; (ii) Application of a filtration system","kg/tonne melted glass",4.0000000000000002E-4,2.5000000000000001E-3,"Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The ranges refer to the sum of metals present in the flue-gases in both solid and gaseous phases","GLS (2012) - 2012/134/EU","1.7.6",48,48]
[1142,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Special glass ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes","Emissions to air","Air","Metals (Group 1) ","Metals (Group 1)","For downstream dusty processes, BAT is to reduce emissions of dust and metals by using one or a combination of the following techniques: (i) Performing dusty operations (e.g. cutting, grinding, polishing) under liquid; (ii) Applying a bag filter system","mg/Nm3","N/A","1","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3","N/A","Daily average (continuous)","BAT-AELs for dust and metal emissions from downstream processes in the special glass sector, when treated separately\n\nThe levels refer to the sum of metals present in the waste gas.\n55.","GLS (2012) - 2012/134/EU","1.6.6",44,44]
[1137,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Special glass ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Metals (Group 1) ","Metals (Group 1)","BAT is to reduce metal emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of metals; (ii) Minimising the use of metal compounds in the batch formulation, through a suitable selection of the raw materials where colouring and decolourising of glass is needed or where specific characteristics are conferred to the glass; (iii) Dry or semi-dry scrubbing, in combination with a filtration system","mg/Nm3","0.1","1","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The levels refer to the sum of metals present in the flue-gases in both solid and gaseous phases.\n\nThe lower levels are BAT-AELs when metal compounds are not intentionally used in the batch formulation.","GLS (2012) - 2012/134/EU","1.6.5",43,43]
[1126,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Special glass ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Metals (Group 1) ","Metals (Group 1)","BAT is to reduce metal emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of metals; (ii) Minimising the use of metal compounds in the batch formulation, through a suitable selection of the raw materials where colouring and decolourising of glass is needed or where specific characteristics are conferred to the glass; (iii) Dry or semi-dry scrubbing, in combination with a filtration system","kg/tonne melted glass",2.9999999999999997E-4,3.0000000000000001E-3,"Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The levels refer to the sum of metals present in the flue-gases in both solid and gaseous phases.\n\nThe lower levels are BAT-AELs when metal compounds are not intentionally used in the batch formulation.\n\nThe conversion factor of 2,5 × 10 –3 (see Table 2) has been used, with some values indicated in the table having been approximated. A case-by-case conversion factor may have to be applied based on the type of production.","GLS (2012) - 2012/134/EU","1.6.5",43,43]
[1105,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Domestic glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Metals (Group 1+ Group 2) ","Metals (Group 1+ Group 2) ","BAT is to reduce metal emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of metals; (ii) Minimising the use of metal compounds in the batch formulation, through a suitable selection of the raw materials where colouring and decolourising of glass is needed or where specific characteristics are conferred to the glass; (iii) Dry or semi-dry scrubbing, in combination with a filtration system ","mg/Nm3","1","5","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","BAT-AELs for metal emissions from the melting furnace in the domestic glass sector with the exception of glasses where selenium is used for decolourising\n\nThe levels refer to the sum of metals present in the flue-gases in both solid and gaseous phases.","GLS (2012) - 2012/134/EU","1.5.5",37,37]
[1092,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Domestic glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Metals (Group 1+ Group 2) ","Metals (Group 1+ Group 2) ","BAT is to reduce metal emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of metals; (ii) Minimising the use of metal compounds in the batch formulation, through a suitable selection of the raw materials where colouring and decolourising of glass is needed or where specific characteristics are conferred to the glass; (iii) Dry or semi-dry scrubbing, in combination with a filtration system ","kg/tonne melted glass",3.0000000000000001E-3,1.4999999999999999E-2,"Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","BAT-AELs for metal emissions from the melting furnace in the domestic glass sector with the exception of glasses where selenium is used for decolourising \n\nThe levels refer to the sum of metals present in the flue-gases in both solid and gaseous phases.\n\nA conversion factor of 3 × 10 –3 has been applied (see Table 2). However, a case-by-case conversion factor may have to be applied for specific productions.","GLS (2012) - 2012/134/EU","1.5.5",37,37]
[1049,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Flat glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Metals (Group 1+ Group 2) ","Metals (Group 1+ Group 2) ","BAT is to reduce metal emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of metals; (ii) Applying a filtration system; (iii) Applying a dry or semi-dry scrubbing in combination with a filtration system ","mg/Nm3","1","5","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","BAT-AELs for metal emissions from the melting furnace in the flat glass sector, with the exception of selenium coloured glasses\n\nThe ranges refer to the sum of metals present in the flue-gases in both solid and gaseous phases.","GLS (2012) - 2012/134/EU","1.3.5",26,26]
[1044,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Flat glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Metals (Group 1+ Group 2) ","Metals (Group 1+ Group 2) ","BAT is to reduce metal emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of metals; (ii) Applying a filtration system; (iii) Applying a dry or semi-dry scrubbing in combination with a filtration system ","kg/tonne melted glass",2.5000000000000001E-3,1.2500000000000001E-2,"Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","BAT-AELs for metal emissions from the melting furnace in the flat glass sector, with the exception of selenium coloured glasses\n\nThe ranges refer to the sum of metals present in the flue-gases in both solid and gaseous phases.\n\nThe conversion factor reported in Table 2 (2,5 × 10 –3 ) has been applied","GLS (2012) - 2012/134/EU","1.3.5",26,26]
[1227,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Frits ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes ","Emissions to air","Air","Metals (Group 1+ Group 2) ","Metals (Group 1+ Group 2) ","For downstream dusty processes, BAT is to reduce emissions by using one or a combination of the following techniques: (i) Applying wet milling techniques; (ii) Operating dry milling and dry product packaging under an efficient extraction system in conjunction with a fabric filter; (iii) Applying a filtration system","mg/Nm3","N/A","5","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3","N/A","Daily average (continuous)","The levels refer to the sum of metals present in the waste gas.","GLS (2012) - 2012/134/EU","1.8.1",57,57]
[1011,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Container glass","Nitrates in batch formulation","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","NOx expressed as NO2","Nitrogen dioxide","Primary techniques ","mg/Nm3","N/A",1000,"Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","If nitrates are used in the batch formulation for short campaigns or for melting furnaces with a capacity of < 100 t/day","GLS (2012) - 2012/134/EU","1.2.2",19,19]
[105,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Container glass","Nitrates in batch formulation","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","NOx expressed as NO2","Nitrogen dioxide","Primary techniques ","kg/tonne melted glass","N/A",3,"Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","If nitrates are used in the batch formulation for short campaigns or for melting furnaces with a capacity of < 100 t/day","GLS (2012) - 2012/134/EU","1.2.2",19,19]
[1003,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Container glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","NOx expressed as NO2","Nitrogen dioxide","Combustion modifications, special furnace designs","mg/Nm3","500","800","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The lower value refers to the use of special furnace designs, where applicable\n\nThese values should be reconsidered in the occasion of a normal or complete rebuild of the melting furnace","GLS (2012) - 2012/134/EU","1.2.2",19,19]
[101,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Container glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","NOx expressed as NO2","Nitrogen dioxide","Combustion modifications, special furnace designs","kg/tonne melted glass",0.75,1.2,"Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The conversion factor reported in Table 2 for general cases (1,5 × 10 –3 ) has been applied, with the exception of electric melting (specific cases: 3 × 10 –3 )\n\nThe lower value refers to the use of special furnace designs, where applicable\n\nThese values should be reconsidered in the occasion of a normal or complete rebuild of the melting furnace","GLS (2012) - 2012/134/EU","1.2.2",19,19]
[1005,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Container glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","NOx expressed as NO2","Nitrogen dioxide","Electric melting","mg/Nm3","N/A",100,"Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.2.2",19,19]
[102,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Container glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","NOx expressed as NO2","Nitrogen dioxide","Electric melting","kg/tonne melted glass","N/A",0.3,"Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The conversion factor reported in Table 2 for general cases (1,5 × 10 –3 ) has been applied, with the exception of electric melting (specific cases: 3 × 10 –3 )","GLS (2012) - 2012/134/EU","1.2.2",19,19]
[1007,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Container glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","NOx expressed as NO2","Nitrogen dioxide","Oxy-fuel melting","mg/Nm3","N/A","N/A","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The achievable levels depend on the quality of the natural gas and oxygen available (nitrogen content).","GLS (2012) - 2012/134/EU","1.2.2",19,19]
[103,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Container glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","NOx expressed as NO2","Nitrogen dioxide","Oxy-fuel melting","kg/tonne melted glass","0.5","0.8","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The achievable levels depend on the quality of the natural gas and oxygen available (nitrogen content)\n\nThe conversion factor reported in Table 2 for general cases (1,5 × 10 –3 ) has been applied, with the exception of electric melting (specific cases: 3 × 10 –3 )","GLS (2012) - 2012/134/EU","1.2.2",19,19]
[1009,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Container glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","NOx expressed as NO2","Nitrogen dioxide","Secondary techniques","mg/Nm3","N/A",500,"Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.2.2",19,19]
[104,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Container glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","NOx expressed as NO2","Nitrogen dioxide","Secondary techniques","kg/tonne melted glass","N/A",0.75,"Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The achievable levels depend on the quality of the natural gas and oxygen available (nitrogen content)","GLS (2012) - 2012/134/EU","1.2.2",19,19]
[1089,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Domestic glass","Nitrates in batch formulation","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","NOx expressed as NO2","Nitrogen dioxide","When nitrates are used in the batch formulation, BAT is to reduce NO X emissions by minimising the use of these raw materials, in combination with primary or secondary techniques.","mg/Nm3","500","1500","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","BAT-AELs for NO X emissions from the melting furnace in the domestic glass sector, when nitrates are used in the batch formulation for a limited number of short campaigns or for melting furnaces with a capacity < 100 t/day producing special types of soda-lime glasses (clear/ultra-clear glass or coloured glass using selenium) and other special glasses (i.e. borosilicate, glass ceramics, opal glass, crystal and lead crystal\n\nThis BAT-AEL is for the fuel/ar conventional furnaces","GLS (2012) - 2012/134/EU","1.5.2",35,35]
[1084,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Domestic glass","Nitrates in batch formulation","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","NOx expressed as NO2","Nitrogen dioxide","When nitrates are used in the batch formulation, BAT is to reduce NO X emissions by minimising the use of these raw materials, in combination with primary or secondary techniques.","kg/tonne melted glass","1.25","3.75","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","BAT-AELs for NO X emissions from the melting furnace in the domestic glass sector, when nitrates are used in the batch formulation for a limited number of short campaigns or for melting furnaces with a capacity < 100 t/day producing special types of soda-lime glasses (clear/ultra-clear glass or coloured glass using selenium) and other special glasses (i.e. borosilicate, glass ceramics, opal glass, crystal and lead crystal\n\nThis BAT-AEL is for the fuel/ar conventional furnaces\n\nThe conversion factor reported in Table 2 for soda-lime glass (2,5 × 10 –3 ) has been applied.","GLS (2012) - 2012/134/EU","1.5.2",35,35]
[1091,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Domestic glass","Nitrates in batch formulation","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","NOx expressed as NO2","Nitrogen dioxide","When nitrates are used in the batch formulation, BAT is to reduce NO X emissions by minimising the use of these raw materials, in combination with primary or secondary techniques.","mg/Nm3","300","500","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","BAT-AELs for NO X emissions from the melting furnace in the domestic glass sector, when nitrates are used in the batch formulation for a limited number of short campaigns or for melting furnaces with a capacity < 100 t/day producing special types of soda-lime glasses (clear/ultra-clear glass or coloured glass using selenium) and other special glasses (i.e. borosilicate, glass ceramics, opal glass, crystal and lead crystal\n\nThis BAT-AEL is for the electric melting furnace","GLS (2012) - 2012/134/EU","1.5.2",35,35]
[1085,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Domestic glass","Nitrates in batch formulation","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","NOx expressed as NO2","Nitrogen dioxide","When nitrates are used in the batch formulation, BAT is to reduce NO X emissions by minimising the use of these raw materials, in combination with primary or secondary techniques.","kg/tonne melted glass","8","10","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","BAT-AELs for NO X emissions from the melting furnace in the domestic glass sector, when nitrates are used in the batch formulation for a limited number of short campaigns or for melting furnaces with a capacity < 100 t/day producing special types of soda-lime glasses (clear/ultra-clear glass or coloured glass using selenium) and other special glasses (i.e. borosilicate, glass ceramics, opal glass, crystal and lead crystal\n\nThis BAT-AEL is for the electric melting furnace","GLS (2012) - 2012/134/EU","1.5.2",35,35]
[1083,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Domestic glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","NOx expressed as NO2","Nitrogen dioxide","Combustion modifications, special furnace designs","mg/Nm3","500","1000","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.5.2",34,34]
[1081,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Domestic glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","NOx expressed as NO2","Nitrogen dioxide","Combustion modifications, special furnace designs","kg/tonne melted glass","1.25","2.5","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","A conversion factor of 2,5 × 10 –3 has been applied for combustion modifications and special furnace designs and a conversion factor of 3 × 10 –3 has been applied for electric melting (see Table 2). However, a case-by-case conversion factor may have to be applied for specific productions.","GLS (2012) - 2012/134/EU","1.5.2",34,34]
[1085,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Domestic glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","NOx expressed as NO2","Nitrogen dioxide","Electric melting","mg/Nm3","N/A","100","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.5.2",34,34]
[1082,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Domestic glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","NOx expressed as NO2","Nitrogen dioxide","Electric melting","kg/tonne melted glass","N/A","0.3","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","A conversion factor of 2,5 × 10 –3 has been applied for combustion modifications and special furnace designs and a conversion factor of 3 × 10 –3 has been applied for electric melting (see Table 2). However, a case-by-case conversion factor may have to be applied for specific productions.","GLS (2012) - 2012/134/EU","1.5.2",34,34]
[1087,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Domestic glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","NOx expressed as NO2","Nitrogen dioxide","Oxy-fuel melting","mg/Nm3","N/A","N/A","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The achievable levels depend on the quality of the natural gas and oxygen available (nitrogen content).","GLS (2012) - 2012/134/EU","1.5.2",34,34]
[1083,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Domestic glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","NOx expressed as NO2","Nitrogen dioxide","Oxy-fuel melting","kg/tonne melted glass","0.5","1.5","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","A conversion factor of 2,5 × 10 –3 has been applied for combustion modifications and special furnace designs and a conversion factor of 3 × 10 –3 has been applied for electric melting (see Table 2). However, a case-by-case conversion factor may have to be applied for specific productions.\n\nThe achievable levels depend on the quality of the natural gas and oxygen available (nitrogen content).","GLS (2012) - 2012/134/EU","1.5.2",34,34]
[1059,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Filament glass fibre","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","NOx expressed as NO2","Nitrogen dioxide","Combustion modifications","mg/Nm3","600","1000","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.4.2",29,29]
[1059,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Filament glass fibre","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","NOx expressed as NO2","Nitrogen dioxide","Combustion modifications","kg/tonne melted glass","2.7","4.5","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The conversion factor reported in Table 2 (4,5 × 10 –3 ) has been applied.","GLS (2012) - 2012/134/EU","1.4.2",29,29]
[1061,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Filament glass fibre","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","NOx expressed as NO2","Nitrogen dioxide","Oxy-fuel melting","mg/Nm3","N/A","N/A","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The achievable levels depend on the quality of the natural gas and oxygen available (nitrogen content).","GLS (2012) - 2012/134/EU","1.4.2",29,29]
[1060,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Filament glass fibre","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","NOx expressed as NO2","Nitrogen dioxide","Oxy-fuel melting","kg/tonne melted glass","0.5","1.5","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The achievable levels depend on the quality of the natural gas and oxygen available (nitrogen content).","GLS (2012) - 2012/134/EU","1.4.2",29,29]
[1038,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Flat glass","Nitrates in batch formulation","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","NOx expressed as NO2","Nitrogen dioxide","Primary techniques ","mg/Nm3","N/A",1200,"Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","BAT-AEL for NO X emissions from the melting furnace in the flat glass sector, when nitrates are used in the batch formulation for the production of special glasses in a limited number of short campaigns","GLS (2012) - 2012/134/EU","1.3.2",25,25]
[1032,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Flat glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","NOx expressed as NO2","Nitrogen dioxide","Combustion modifications, Fenix process","mg/Nm3",700,800,"Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","Higher emission levels are expected when nitrates are used occasionally for the production of special glasses.\n\nThe lower levels of the range are associated with the application of the Fenix process","GLS (2012) - 2012/134/EU","1.3.2",24,24]
[1031,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Flat glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","NOx expressed as NO2","Nitrogen dioxide","Combustion modifications, Fenix process","kg/tonne melted glass",1.75,2,"Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","Higher emission levels are expected when nitrates are used occasionally for the production of special glasses.\n\nThe lower levels of the range are associated with the application of the Fenix process\n\nThe conversion factor reported in Table 2 (2,5 × 10 –3 ) has been applied","GLS (2012) - 2012/134/EU","1.3.2",24,24]
[1034,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Flat glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","NOx expressed as NO2","Nitrogen dioxide","Oxy-fuel melting","mg/Nm3","N/A","N/A","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","Higher emission levels are expected when nitrates are used occasionally for the production of special glasses.\n\nThe achievable levels depend on the quality of the natural gas and oxygen available (nitrogen content).","GLS (2012) - 2012/134/EU","1.3.2",24,24]
[1032,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Flat glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","NOx expressed as NO2","Nitrogen dioxide","Oxy-fuel melting","kg/tonne melted glass","1.25","2.0","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","Higher emission levels are expected when nitrates are used occasionally for the production of special glasses.\n\nThe achievable levels depend on the quality of the natural gas and oxygen available (nitrogen content).\n\nThe conversion factor reported in Table 2 (2,5 × 10 –3 ) has been applied.","GLS (2012) - 2012/134/EU","1.3.2",24,24]
[1036,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Flat glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","NOx expressed as NO2","Nitrogen dioxide","Secondary techniques","mg/Nm3",400,700,"Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","Higher emission levels are expected when nitrates are used occasionally for the production of special glasses.\n\nThe higher levels of the range are associated with existing plants until a normal or complete rebuild of the melting furnace. The lower levels are associated with newer/retrofitted plants.\n","GLS (2012) - 2012/134/EU","1.3.2",24,24]
[1033,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Flat glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","NOx expressed as NO2","Nitrogen dioxide","Secondary techniques","kg/tonne melted glass",1,1.75,"Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","Higher emission levels are expected when nitrates are used occasionally for the production of special glasses.\n\nThe higher levels of the range are associated with existing plants until a normal or complete rebuild of the melting furnace. The lower levels are associated with newer/retrofitted plants.\n","GLS (2012) - 2012/134/EU","1.3.2",24,24]
[1213,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Frits ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","NOx expressed as NO2","Nitrogen dioxide","Primary techniques: Fuel/air, fuel/oxygen-enriched air combustion, with nitrates ","mg/Nm3","N/A","1600","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The ranges take into account the combination of flue-gases from furnaces applying different melting techniques and producing a variety of frit types, with or without nitrates in the batch formulations, which may be conveyed to a single stack, precluding the possibility of characterising each applied melting technique and the different products.","GLS (2012) - 2012/134/EU","1.8.1",55,55]
[1210,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Frits ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","NOx expressed as NO2","Nitrogen dioxide","Primary techniques: Fuel/air, fuel/oxygen-enriched air combustion, with nitrates ","kg/tonne melted glass","N/A","12","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The ranges take into account the combination of flue-gases from furnaces applying different melting techniques and producing a variety of frit types, with or without nitrates in the batch formulations, which may be conveyed to a single stack, precluding the possibility of characterising each applied melting technique and the different products.\n\nThe conversion factors of 5 × 10 –3 and 7,5 × 10 –3 have been used for the determination of the lower and higher values of the range. However, a case-by-case conversion factor may have to be applied based on the type of combustion","GLS (2012) - 2012/134/EU","1.8.1",55,55]
[1211,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Frits ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","NOx expressed as NO2","Nitrogen dioxide","Primary techniques: Fuel/air, fuel/oxygen-enriched air combustion, without nitrates ","mg/Nm3","500","1000","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The ranges take into account the combination of flue-gases from furnaces applying different melting techniques and producing a variety of frit types, with or without nitrates in the batch formulations, which may be conveyed to a single stack, precluding the possibility of characterising each applied melting technique and the different products.","GLS (2012) - 2012/134/EU","1.8.1",55,55]
[1209,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Frits ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","NOx expressed as NO2","Nitrogen dioxide","Primary techniques: Fuel/air, fuel/oxygen-enriched air combustion, without nitrates ","kg/tonne melted glass","2.5","7.5","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The ranges take into account the combination of flue-gases from furnaces applying different melting techniques and producing a variety of frit types, with or without nitrates in the batch formulations, which may be conveyed to a single stack, precluding the possibility of characterising each applied melting technique and the different products.\n\nThe conversion factors of 5 × 10 –3 and 7,5 × 10 –3 have been used for the determination of the lower and higher values of the range. However, a case-by-case conversion factor may have to be applied based on the type of combustion","GLS (2012) - 2012/134/EU","1.8.1",55,55]
[1208,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Frits ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","NOx expressed as NO2","Nitrogen dioxide","Primary techniques: Oxy fuel firing, with use nitrates","kg/tonne melted glass","5","10","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The ranges take into account the combination of flue-gases from furnaces applying different melting techniques and producing a variety of frit types, with or without nitrates in the batch formulations, which may be conveyed to a single stack, precluding the possibility of characterising each applied melting technique and the different products.\n\nThe conversion factors of 5 × 10 –3 and 7,5 × 10 –3 have been used for the determination of the lower and higher values of the range. However, a case-by-case conversion factor may have to be applied based on the type of combustion","GLS (2012) - 2012/134/EU","1.8.1",55,55]
[1208,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Frits ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","NOx expressed as NO2","Nitrogen dioxide","Primary techniques: Oxy fuel firing, without nitrates","kg/tonne melted glass","2.5","5","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The ranges take into account the combination of flue-gases from furnaces applying different melting techniques and producing a variety of frit types, with or without nitrates in the batch formulations, which may be conveyed to a single stack, precluding the possibility of characterising each applied melting technique and the different products.\n\nThe conversion factors of 5 × 10 –3 and 7,5 × 10 –3 have been used for the determination of the lower and higher values of the range. However, a case-by-case conversion factor may have to be applied based on the type of combustion","GLS (2012) - 2012/134/EU","1.8.1",55,55]
[1197,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","HTIW wools","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Lubricant burn-off oven ","Emissions to air","Air","NOx expressed as NO2","Nitrogen dioxide","BAT is to reduce NO X emissions from the lubricant burn-off oven by applying combustion control and/or modifications","mg/Nm3","100","200","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3","N/A","Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.8.1",52,52]
[1148,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Mineral wool","Glass wool","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","NOx expressed as NO2","Nitrogen dioxide","All types of furnaces","kg/tonne melted glass","1.0","1.25","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The conversion factors of 2 × 10 –3 for glass wool and 2,5 × 10 –3 for stone wool have been used (see Table 2).","GLS (2012) - 2012/134/EU","1.7.1",45,45]
[1147,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Mineral wool","Glass wool","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","NOx expressed as NO2","Nitrogen dioxide","Fuel/air and Electric furnaces","mg/Nm3","200","500","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.7.1",45,45]
[1146,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Mineral wool","Glass wool","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","NOx expressed as NO2","Nitrogen dioxide","Fuel/air and Electric furnaces","kg/tonne melted glass","0.4","1.0","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The conversion factors of 2 × 10 –3 for glass wool and 2,5 × 10 –3 for stone wool have been used","GLS (2012) - 2012/134/EU","1.7.1",45,45]
[1149,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Mineral wool","Glass wool","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","NOx expressed as NO2","Nitrogen dioxide","Oxy-fuel melting","mg/Nm3","N/A","N/A","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The achievable levels depend on the quality of the natural gas and oxygen available (nitrogen content).","GLS (2012) - 2012/134/EU","1.7.1",45,45]
[1147,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Mineral wool","Glass wool","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","NOx expressed as NO2","Nitrogen dioxide","Oxy-fuel melting","kg/tonne melted glass","N/A","N/A","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The conversion factors of 2 × 10 –3 for glass wool and 2,5 × 10 –3 for stone wool have been used\n\nThe achievable levels depend on the quality of the natural gas and oxygen available (nitrogen content).","GLS (2012) - 2012/134/EU","1.7.1",45,45]
[1153,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Mineral wool","Nitrates in batch formulation","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","NOx expressed as NO2","Nitrogen dioxide","Minimisation of nitrate input in the batch formulation, combined with primary techniques","mg/Nm3","500","700","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.7.2",46,46]
[1149,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Mineral wool","Nitrates in batch formulation","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","NOx expressed as NO2","Nitrogen dioxide","Minimisation of nitrate input in the batch formulation, combined with primary techniques","kg/tonne melted glass","1.0","1.4","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The conversion factor of 2 × 10 –3 has been used\n\nThe lower levels of the ranges are associated with the application of oxy-fuel melting.","GLS (2012) - 2012/134/EU","1.7.2",46,46]
[1151,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Mineral wool","Stone wool","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","NOx expressed as NO2","Nitrogen dioxide","All types of furnaces","mg/Nm3","400","500","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.7.1",45,45]
[1193,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes- Curing oven emissions ","Emissions to air","Air","NOx expressed as NO2","Nitrogen dioxide","BAT is to reduce emissions from downstream processes by using one or a combination of the following techniques: (i) Impact jets and cyclones; (ii) Wet scrubbers; (iii) Wet electrostatic precipitators; (iv) Stone wool filters; (v) Waste gas incineration","mg/Nm3","100","200","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3","N/A","Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.7.7",50,50]
[1187,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes- Curing oven emissions ","Emissions to air","Air","NOx expressed as NO2","Nitrogen dioxide","BAT is to reduce emissions from downstream processes by using one or a combination of the following techniques: (i) Impact jets and cyclones; (ii) Wet scrubbers; (iii) Wet electrostatic precipitators; (iv) Stone wool filters; (v) Waste gas incineration","kg/tonne melted glass","N/A","1","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3","N/A","Daily average (continuous)","The specific mass emissions refer to 1 tonne of produced glass","GLS (2012) - 2012/134/EU","1.7.7",50,50]
[1127,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Special glass ","Nitrates in batch formulation","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","NOx expressed as NO2","Nitrogen dioxide","Minimisation of nitrate input in the batch formulation combined with primary or secondary techniques","mg/Nm3","500","1000","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The lower levels are associated with the use of electric melting.","GLS (2012) - 2012/134/EU","1.6.2",41,41]
[1121,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Special glass ","Nitrates in batch formulation","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","NOx expressed as NO2","Nitrogen dioxide","Minimisation of nitrate input in the batch formulation combined with primary or secondary techniques","kg/tonne melted glass","1","6","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The lower levels are associated with the use of electric melting.\n\nThe conversion factors of 2,5 × 10 –3 and 6,5 × 10 –3 have been used for the determination of the lower and upper value of the BAT- AEL range respectively, with values being approximated. A case-by-case conversion factor may have to be applied based on the type of production.","GLS (2012) - 2012/134/EU","1.6.2",41,41]
[1119,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Special glass ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","NOx expressed as NO2","Nitrogen dioxide","Combustion modifications","mg/Nm3","600","800","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.6.2",41,41]
[1117,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Special glass ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","NOx expressed as NO2","Nitrogen dioxide","Combustion modifications","kg/tonne melted glass","1.5","3.2","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The conversion factors of 2,5 × 10 –3 and 4 × 10 –3 have been used for the determination of the lower and upper value of the BAT-AEL range (see Table 2), with some values being approximated. However, a case-by-case conversion factor needs to be applied based on the type of production.","GLS (2012) - 2012/134/EU","1.6.2",41,41]
[1121,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Special glass ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","NOx expressed as NO2","Nitrogen dioxide","Electric melting","mg/Nm3","N/A","100","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.6.2",41,41]
[1118,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Special glass ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","NOx expressed as NO2","Nitrogen dioxide","Electric melting","kg/tonne melted glass","0.25","0.4","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The conversion factors of 2,5 × 10 –3 and 4 × 10 –3 have been used for the determination of the lower and upper value of the BAT-AEL range (see Table 2), with some values being approximated. However, a case-by-case conversion factor needs to be applied based on the type of production.","GLS (2012) - 2012/134/EU","1.6.2",41,41]
[1123,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Special glass ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","NOx expressed as NO2","Nitrogen dioxide","Oxy-fuel melting","mg/Nm3","N/A","N/A","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The higher values are related to a special production of borosilicate glass tubes for pharmaceutical use.\n\nThe achievable levels depend on the quality of the natural gas and oxygen available (nitrogen content).","GLS (2012) - 2012/134/EU","1.6.2",41,41]
[1119,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Special glass ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","NOx expressed as NO2","Nitrogen dioxide","Oxy-fuel melting","kg/tonne melted glass","1","3","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The conversion factors of 2,5 × 10 –3 and 4 × 10 –3 have been used for the determination of the lower and upper value of the BAT-AEL range (see Table 2), with some values being approximated. However, a case-by-case conversion factor needs to be applied based on the type of production.\n\nThe higher values are related to a special production of borosilicate glass tubes for pharmaceutical use.\n\nThe achievable levels depend on the quality of the natural gas and oxygen available (nitrogen content).","GLS (2012) - 2012/134/EU","1.6.2",41,41]
[1125,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Special glass ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","NOx expressed as NO2","Nitrogen dioxide","Secondary techniques","mg/Nm3","N/A","500","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.6.2",41,41]
[1120,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Special glass ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","NOx expressed as NO2","Nitrogen dioxide","Secondary techniques","kg/tonne melted glass","1","3","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The conversion factors of 2,5 × 10 –3 and 4 × 10 –3 have been used for the determination of the lower and upper value of the BAT-AEL range (see Table 2), with some values being approximated. However, a case-by-case conversion factor needs to be applied based on the type of production.","GLS (2012) - 2012/134/EU","1.6.2",41,41]
[1183,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes- Curing oven emissions ","Emissions to air","Air","Phenol","Phenol","BAT is to reduce emissions from downstream processes by using one or a combination of the following techniques: (i) Impact jets and cyclones; (ii) Wet scrubbers; (iii) Wet electrostatic precipitators; (iv) Stone wool filters; (v) Waste gas incineration","mg/Nm3","2","5","Amber",0,"273.15","101.3","N/A","Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.7.7",50,50]
[1182,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes- Curing oven emissions ","Emissions to air","Air","Phenol","Phenol","BAT is to reduce emissions from downstream processes by using one or a combination of the following techniques: (i) Impact jets and cyclones; (ii) Wet scrubbers; (iii) Wet electrostatic precipitators; (iv) Stone wool filters; (v) Waste gas incineration","kg/tonne melted glass","N/A","0.03","Amber",0,"273.15","101.3","N/A","Daily average (continuous)","The specific mass emissions refer to 1 tonne of produced glass","GLS (2012) - 2012/134/EU","1.7.7",50,50]
[1176,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes- Forming area ","Emissions to air","Air","Phenol","Phenol","BAT is to reduce emissions from downstream processes by using one or a combination of the following techniques: (i) Impact jets and cyclones; (ii) Wet scrubbers; (iii) Wet electrostatic precipitators; (iv) Stone wool filters; (v) Waste gas incineration","mg/Nm3","5","10","Amber",0,"273.15","101.3","N/A","Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.7.7",49,49]
[1107,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Domestic glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Selenium compounds expressed as Se","Selenium and compounds, except hydrogen selenide (as Se)","When selenium compounds are used for decolourising the glass, BAT is to reduce selenium emissions from the melting furnace by using one or a combination of the following techniques: (i) Minimising the use of selenium compounds in the batch formulation, through a suitable selection of the raw materials; (ii) Dry or semi-dry scrubbing, in combination with a filtration system","mg/Nm3","N/A","1","Amber",0,"273.15","101.3",0.08,"Daily average (continuous)","The values refer to the sum of selenium present in the flue-gases in both solid and gaseous phases.","GLS (2012) - 2012/134/EU","1.5.5",37,37]
[1051,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Flat glass","Colored Glass","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","Selenium compounds expressed as Se","Selenium and compounds, except hydrogen selenide (as Se)","When selenium compounds are used for colouring the glass, BAT is to reduce selenium emissions from the melting furnace by using one or a combination of the following techniques: (i) Minimising the evaporation of selenium from the batch composition by selecting raw material with a higher retention efficiency in the glass and reduced volatilisation; (ii) Applying a filtration system; (iii) Applying a dry or semi-dry scrubbing in combination with a filtration system","mg/Nm3","1","3","Amber",0,"273.15","101.3",0.08,"Daily average (continuous)","BAT-AELs for selenium emissions from the melting furnace in the flat glass sector for the production of coloured glass\n\nThe lower levels correspond to conditions where the reduction of Se emissions is a priority over a lower production of solid waste from filter dust. In this case, a high stoichiometric ratio (reagent/pollutant) is applied and a significant solid waste stream is generated.\n\n","GLS (2012) - 2012/134/EU","1.3.5",27,27]
[1013,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Container glass","Unspecified","Unspecified","Unspecified","Natural gas ","Unspecified","Melting furnace","Emissions to air","Air","SOX expressed as SO2","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce Sox emissions from the melting furnace by using one or a combination of the following techniques: (i) Dry or semi-dry scrubbing with a filtration system; (ii) minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance; (iii) Use of low sulphur content fuels","mg/Nm3","200","500","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","For special types of coloured glasses (e.g. reduced green glasses), concerns related to the achievable emission levels may require investigating the sulphur balance. Values reported in the table may be difficult to achieve in combination with filter dust recycling and the rate of recycling of external cullet.\n\nThe lower levels are associated with conditions where the reduction of SO X is a high priority over a lower production of solid waste corresponding to the sulphate-rich filter dust.","GLS (2012) - 2012/134/EU","1.2.3",20,20]
[1029,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Container glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes","Emissions to air","Air","SOX expressed as SO2","Sulphur Dioxide (24 Hour Mean)","When SO 3 is used for surface treatment operations, BAT is to reduce SO X emissions by using one or a combination of the following techniques: (i) minimising the product losses by ensuring a good sealing of the application system; (ii) applying a secondary technique, e.g. wet scrubbing","mg/Nm3","100","200","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3","N/A","Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.2.6",22,22]
[1097,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Domestic glass","Unspecified","Unspecified","Unspecified","Electric melting","Unspecified","Melting furnace","Emissions to air","Air","SOX expressed as SO2","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance; (ii) Use of low sulphur content; (iii) Dry or semi-dry scrubbing in combination with a filtration system ","mg/Nm3","N/A","100","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.5.3",35,35]
[1088,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Domestic glass","Unspecified","Unspecified","Unspecified","Electric melting","Unspecified","Melting furnace","Emissions to air","Air","SOX expressed as SO2","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance; (ii) Use of low sulphur content; (iii) Dry or semi-dry scrubbing in combination with a filtration system ","kg/tonne melted glass","N/A","0.25","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","A conversion factor of 2,5 × 10 –3 has been applied (see Table 2). However, a case-by-case conversion factor may have to be applied for specific productions.","GLS (2012) - 2012/134/EU","1.5.3",35,35]
[1095,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Domestic glass","Unspecified","Unspecified","Unspecified","Fuel oil","Unspecified","Melting furnace","Emissions to air","Air","SOX expressed as SO2","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance; (ii) Use of low sulphur content; (iii) Dry or semi-dry scrubbing in combination with a filtration system ","mg/Nm3","N/A","1000","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The levels are related to the use of 1 % sulphur fuel oil in combination with secondary abatement techniques.","GLS (2012) - 2012/134/EU","1.5.3",35,35]
[1087,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Domestic glass","Unspecified","Unspecified","Unspecified","Fuel oil","Unspecified","Melting furnace","Emissions to air","Air","SOX expressed as SO2","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance; (ii) Use of low sulphur content; (iii) Dry or semi-dry scrubbing in combination with a filtration system ","kg/tonne melted glass","N/A","2.5","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The levels are related to the use of 1 % sulphur fuel oil in combination with secondary abatement techniques.\n\nA conversion factor of 2,5 × 10 –3 has been applied (see Table 2). However, a case-by-case conversion factor may have to be applied for specific productions.","GLS (2012) - 2012/134/EU","1.5.3",35,35]
[1093,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Domestic glass","Unspecified","Unspecified","Unspecified","Natural gas ","Unspecified","Melting furnace","Emissions to air","Air","SOX expressed as SO2","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance; (ii) Use of low sulphur content; (iii) Dry or semi-dry scrubbing in combination with a filtration system ","mg/Nm3","200","300","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.5.3",35,35]
[1086,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Domestic glass","Unspecified","Unspecified","Unspecified","Natural gas ","Unspecified","Melting furnace","Emissions to air","Air","SOX expressed as SO2","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance; (ii) Use of low sulphur content; (iii) Dry or semi-dry scrubbing in combination with a filtration system ","kg/tonne melted glass","0.5","0.75","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","A conversion factor of 2,5 × 10 –3 has been applied (see Table 2). However, a case-by-case conversion factor may have to be applied for specific productions.","GLS (2012) - 2012/134/EU","1.5.3",35,35]
[1065,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Filament glass fibre","Unspecified","Unspecified","Unspecified","Fuel oil","Unspecified","Melting furnace","Emissions to air","Air","SOX expressed as SO2","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance; (ii) Use of low sulphur content fuels; (iii) Dry or semi dry scrubbing in combination wtih a filtration system; (iv) Use of wet scrubbing ","mg/Nm3","500","1000","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The higher levels of the range are associated with the use of sulphates in the batch formulation for refining the glass.\n\nThe associated emission levels are related to the use of 1 % sulphur fuel oil in combination with secondary abatement techniques.\n\nThe lower levels correspond to conditions where the reduction of SO X is a priority over a lower production of solid waste corresponding to the sulphate-rich filter dust. In this case, the lower levels are associated with the use of a bag filter.","GLS (2012) - 2012/134/EU","1.4.3",30,30]
[1062,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Filament glass fibre","Unspecified","Unspecified","Unspecified","Fuel oil","Unspecified","Melting furnace","Emissions to air","Air","SOX expressed as SO2","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance; (ii) Use of low sulphur content fuels; (iii) Dry or semi dry scrubbing in combination wtih a filtration system; (iv) Use of wet scrubbing ","kg/tonne melted glass","2.25","4.5","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The higher levels of the range are associated with the use of sulphates in the batch formulation for refining the glass.\n\nThe conversion factor reported in Table 2 (4,5 × 10 –3 ) has been applied.\n\nThe associated emission levels are related to the use of 1 % sulphur fuel oil in combination with secondary abatement techniques.\n\nThe lower levels correspond to conditions where the reduction of SO X is a priority over a lower production of solid waste corresponding to the sulphate-rich filter dust. In this case, the lower levels are associated with the use of a bag filter.","GLS (2012) - 2012/134/EU","1.4.3",30,30]
[1063,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Filament glass fibre","Unspecified","Unspecified","Unspecified","Natural gas ","Unspecified","Melting furnace","Emissions to air","Air","SOX expressed as SO2","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance; (ii) Use of low sulphur content fuels; (iii) Dry or semi dry scrubbing in combination wtih a filtration system; (iv) Use of wet scrubbing ","mg/Nm3","200","800","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","Values at levels of < 30 mg/Nm 3 (< 0,14 kg/tonne melted glass) have been reported for boron-free formulations, with the application of primary techniques.\n\nFor oxy-fuel furnaces with the application of wet scrubbing, the BAT-AEL is reported to be < 0,1 kg/tonne melted glass of SO X , expressed as SO 2 .","GLS (2012) - 2012/134/EU","1.4.3",30,30]
[1061,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Filament glass fibre","Unspecified","Unspecified","Unspecified","Natural gas ","Unspecified","Melting furnace","Emissions to air","Air","SOX expressed as SO2","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance; (ii) Use of low sulphur content fuels; (iii) Dry or semi dry scrubbing in combination wtih a filtration system; (iv) Use of wet scrubbing ","kg/tonne melted glass","0.9","3.6","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The higher levels of the range are associated with the use of sulphates in the batch formulation for refining the glass.\n\nThe conversion factor reported in Table 2 (4,5 × 10 –3 ) has been applied.\n\nFor oxy-fuel furnaces with the application of wet scrubbing, the BAT-AEL is reported to be < 0,1 kg/tonne melted glass of SO X , expressed as SO 2 .","GLS (2012) - 2012/134/EU","1.4.3",30,30]
[1041,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Flat glass","Unspecified","Unspecified","Unspecified","Fuel oil","Unspecified","Melting furnace","Emissions to air","Air","SOX expressed as SO2","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Dry or semi-dry scrubbing, in combination with a filtration system; (ii) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance; (iii) Use of low sulphur content fuels","mg/Nm3",500,1300,"Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The lower levels are associated with conditions where the reduction of SO X has a high priority over a lower production of solid waste corresponding to the sulphate-rich filter dust.\n\nThe associated emission levels are related to the use of 1 % sulphur fuel oil in combination with secondary abatement techniques\n\nFor large flat glass furnaces, concerns related to the achievable emission levels may require investigating the sulphur balance. Values reported in the table may be difficult to achieve in combination with filter dust recycling\n\n","GLS (2012) - 2012/134/EU","1.3.3",25,25]
[1040,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Flat glass","Unspecified","Unspecified","Unspecified","Fuel oil","Unspecified","Melting furnace","Emissions to air","Air","SOX expressed as SO2","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Dry or semi-dry scrubbing, in combination with a filtration system; (ii) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance; (iii) Use of low sulphur content fuels","kg/tonne melted glass",1.25,3.25,"Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The lower levels are associated with conditions where the reduction of SO X has a high priority over a lower production of solid waste corresponding to the sulphate-rich filter dust.\n\nThe associated emission levels are related to the use of 1 % sulphur fuel oil in combination with secondary abatement techniques\n\nFor large flat glass furnaces, concerns related to the achievable emission levels may require investigating the sulphur balance. Values reported in the table may be difficult to achieve in combination with filter dust recycling\n\nThe associated emission levels are related to the use of 1 % sulphur fuel oil in combination with secondary abatement techniques.\n\n","GLS (2012) - 2012/134/EU","1.3.3",25,25]
[1039,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Flat glass","Unspecified","Unspecified","Unspecified","Natural gas ","Unspecified","Melting furnace","Emissions to air","Air","SOX expressed as SO2","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Dry or semi-dry scrubbing, in combination with a filtration system; (ii) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance; (iii) Use of low sulphur content fuels","mg/Nm3","300","500","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The lower levels are associated with conditions where the reduction of SO X has a high priority over a lower production of solid waste corresponding to the sulphate-rich filter dust.\n\n","GLS (2012) - 2012/134/EU","1.3.3",25,25]
[1039,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Flat glass","Unspecified","Unspecified","Unspecified","Natural gas ","Unspecified","Melting furnace","Emissions to air","Air","SOX expressed as SO2","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Dry or semi-dry scrubbing, in combination with a filtration system; (ii) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance; (iii) Use of low sulphur content fuels","kg/tonne melted glass","0.75","1.25","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The lower levels are associated with conditions where the reduction of SO X has a high priority over a lower production of solid waste corresponding to the sulphate-rich filter dust.\n\nThe conversion factor reported in Table 2 (2,5 × 10 –3 ) has been applied.","GLS (2012) - 2012/134/EU","1.3.3",25,25]
[1055,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Flat glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes","Emissions to air","Air","SOX expressed as SO2","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce emissions to air from the downstream processes by using one or a combination of the following techniques: (i) Minimising the losses of coating products applied to the flat glass by ensuring a good sealing of the application system; (ii) Minimising the losses of SO2 from the annealing ler, by operating the control system in an optimum manner; (iii) Combining the SO2 emissions from the lehr with the waste fas from the melting furnace, when technically feasible and where a secondary treatment system is applied (filter and dry or semi-dry scrubber); (iv) Applying a secondary technique, e.g. wet scrubbing, or dry scrubbing and filtration","mg/Nm3","N/A","200","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3","N/A","Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.3.6",28,28]
[1215,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Frits ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","SOX expressed as SO2","Sulphur Dioxide (24 Hour Mean)","BAT is to control SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of sulphur; (ii) Dry or semi dry scrubbing in combination with a filtration system; (iii) Use of low sulphur content fuels ","mg/Nm3","50","200","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.8.1",55,55]
[1211,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Frits ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","SOX expressed as SO2","Sulphur Dioxide (24 Hour Mean)","BAT is to control SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of sulphur; (ii) Dry or semi dry scrubbing in combination with a filtration system; (iii) Use of low sulphur content fuels ","kg/tonne melted glass","0.25","1.5","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The conversion factors of 5 × 10 –3 and 7,5 × 10 –3 have been used; however, the values indicated in the table may have been approximated. A case-by-case conversion factor may have to be applied based on the type of combustion","GLS (2012) - 2012/134/EU","1.8.1",55,55]
[1199,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","HTIW wools","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes ","Emissions to air","Air","SOX expressed as SO2","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnaces and downstream processes by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of sulphur; (ii) Use of low sulphur content fuel","mg/Nm3","N/A","50","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3","N/A","Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.8.1",52,52]
[1198,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","HTIW wools","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","SOX expressed as SO2","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnaces and downstream processes by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of sulphur; (ii) Use of low sulphur content fuel","mg/Nm3","N/A","50","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.8.1",52,52]
[1155,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Mineral wool","Glass wool ","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","SOX expressed as SO2","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance ; (ii) Use of low sulphur content fuels' (iii) Dry or semi-dry scrubbing, in combination with a filtration system; (iv) Use of wet scrubbing","mg/Nm3","50","150","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The lower levels of the ranges are associated with the use of electric melting. The higher levels are associated with high levels of cullet recycling.","GLS (2012) - 2012/134/EU","1.7.3",47,47]
[1150,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Mineral wool","Glass wool ","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","SOX expressed as SO2","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance ; (ii) Use of low sulphur content fuels' (iii) Dry or semi-dry scrubbing, in combination with a filtration system; (iv) Use of wet scrubbing","kg/tonne melted glass","0.1","0.3","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","This BATL-AEL is for gas-fired and elctric furnaces\n\nThe lower levels of the ranges are associated with the use of electric melting. The higher levels are associated with high levels of cullet recycling.\n\nThe conversion factors of 2 × 10 –3 for glass wool and 2,5 × 10 –3 for stone wool have been used","GLS (2012) - 2012/134/EU","1.7.3",47,47]
[1157,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Mineral wool","Stone wool","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","SOX expressed as SO2","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance ; (ii) Use of low sulphur content fuels' (iii) Dry or semi-dry scrubbing, in combination with a filtration system; (iv) Use of wet scrubbing","mg/Nm3","N/A","350","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","This BATL-AEL is for gas-fired and elctric furnaces","GLS (2012) - 2012/134/EU","1.7.3",47,47]
[1151,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Mineral wool","Stone wool","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","SOX expressed as SO2","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance ; (ii) Use of low sulphur content fuels' (iii) Dry or semi-dry scrubbing, in combination with a filtration system; (iv) Use of wet scrubbing","kg/tonne melted glass","N/A","0.9","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","This BATL-AEL is for gas-fired and elctric furnaces\n\nThe conversion factors of 2 × 10 –3 for glass wool and 2,5 × 10 –3 for stone wool have been used","GLS (2012) - 2012/134/EU","1.7.3",47,47]
[1159,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Mineral wool","Stone wool","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","SOX expressed as SO2","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance ; (ii) Use of low sulphur content fuels' (iii) Dry or semi-dry scrubbing, in combination with a filtration system; (iv) Use of wet scrubbing","mg/Nm3","N/A","400","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","This BATL-AEL is for Cupola furnaces, no briquettes or slag recycling\n\nThe BAT-AEL is associated with conditions where the reduction of SO X emissions has a high priority over a lower production of solid waste.","GLS (2012) - 2012/134/EU","1.7.3",47,47]
[1152,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Mineral wool","Stone wool","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","SOX expressed as SO2","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance ; (ii) Use of low sulphur content fuels' (iii) Dry or semi-dry scrubbing, in combination with a filtration system; (iv) Use of wet scrubbing","kg/tonne melted glass","N/A","1.0","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","This BATL-AEL is for Cupola furnaces, no briquettes or slag recycling\n\nThe BAT-AEL is associated with conditions where the reduction of SO X emissions has a high priority over a lower production of solid waste.\n\nThe conversion factors of 2 × 10 –3 for glass wool and 2,5 × 10 –3 for stone wool have been used","GLS (2012) - 2012/134/EU","1.7.3",47,47]
[1161,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Mineral wool","Stone wool","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","SOX expressed as SO2","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance ; (ii) Use of low sulphur content fuels' (iii) Dry or semi-dry scrubbing, in combination with a filtration system; (iv) Use of wet scrubbing","mg/Nm3","N/A","1400","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","This BATL-AEL is for Cupola furnaces, with cement briquettes or slag recycling\n\nWhen reduction of waste has a high priority over SO X emissions, higher emission values may be expected. The achievable levels should be based on a sulphur balance.","GLS (2012) - 2012/134/EU","1.7.3",47,47]
[1153,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Mineral wool","Stone wool","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","SOX expressed as SO2","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance ; (ii) Use of low sulphur content fuels' (iii) Dry or semi-dry scrubbing, in combination with a filtration system; (iv) Use of wet scrubbing","kg/tonne melted glass","N/A","3.5","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","This BATL-AEL is for Cupola furnaces, with cement briquettes or slag recycling\n\nWhen reduction of waste has a high priority over SO X emissions, higher emission values may be expected. The achievable levels should be based on a sulphur balance.\n\nThe conversion factors of 2 × 10 –3 for glass wool and 2,5 × 10 –3 for stone wool have been used","GLS (2012) - 2012/134/EU","1.7.3",47,47]
[1131,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Special glass ","Unspecified","Unspecified","Unspecified","Fuel oil","Unspecified","Melting furnace","Emissions to air","Air","SOX expressed as SO2","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance; (ii) Use of low sulphur content fuels; (iii) Dry or semi-dry scrubbing, in combustion with a filtration system ","mg/Nm3","500","800","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The ranges take into account the variable sulphur balances associated with the type of glass produced.\n\nThe associated emission levels are related to the use of 1 % sulphur fuel oil in combination with secondary abatement techniques.","GLS (2012) - 2012/134/EU","1.6.3",42,42]
[1123,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Special glass ","Unspecified","Unspecified","Unspecified","Fuel oil","Unspecified","Melting furnace","Emissions to air","Air","SOX expressed as SO2","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance; (ii) Use of low sulphur content fuels; (iii) Dry or semi-dry scrubbing, in combustion with a filtration system ","kg/tonne melted glass","1.25","2","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The ranges take into account the variable sulphur balances associated with the type of glass produced.\n\nThe associated emission levels are related to the use of 1 % sulphur fuel oil in combination with secondary abatement techniques.\n\nThe conversion factor of 2,5 × 10 –3 (see Table 2) has been used. However, a case-by-case conversion factor may have to be applied based on the type of production.","GLS (2012) - 2012/134/EU","1.6.3",42,42]
[1129,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Special glass ","Unspecified","Unspecified","Unspecified","Natural gas, Electric melting","Unspecified","Melting furnace","Emissions to air","Air","SOX expressed as SO2","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance; (ii) Use of low sulphur content fuels; (iii) Dry or semi-dry scrubbing, in combustion with a filtration system ","mg/Nm3","30","200","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The ranges take into account the variable sulphur balances associated with the type of glass produced.\n\nThe lower levels are associated with the use of electric melting and batch formulations without sulphates.","GLS (2012) - 2012/134/EU","1.6.3",42,42]
[1122,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Special glass ","Unspecified","Unspecified","Unspecified","Natural gas, Electric melting","Unspecified","Melting furnace","Emissions to air","Air","SOX expressed as SO2","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance; (ii) Use of low sulphur content fuels; (iii) Dry or semi-dry scrubbing, in combustion with a filtration system ","kg/tonne melted glass","0.08","0.5","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The ranges take into account the variable sulphur balances associated with the type of glass produced.\n\nThe lower levels are associated with the use of electric melting and batch formulations without sulphates.\n\nThe conversion factor of 2,5 × 10 –3 (see Table 2) has been used. However, a case-by-case conversion factor may have to be applied based on the type of production.","GLS (2012) - 2012/134/EU","1.6.3",42,42]
[106,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Container glass","Unspecified","Unspecified","Unspecified","Natural gas ","Unspecified","Melting furnace","Emissions to air","Air","SOX expressed as SO3","SOX expressed as SO3","BAT is to reduce Sox emissions from the melting furnace by using one or a combination of the following techniques: (i) Dry or semi-dry scrubbing with a filtration system; (ii) minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance; (iii) Use of low sulphur content fuels","kg/tonne melted glass","0.3","0.75","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","For special types of coloured glasses (e.g. reduced green glasses), concerns related to the achievable emission levels may require investigating the sulphur balance. Values reported in the table may be difficult to achieve in combination with filter dust recycling and the rate of recycling of external cullet.\n\nThe lower levels are associated with conditions where the reduction of SO X is a high priority over a lower production of solid waste corresponding to the sulphate-rich filter dust.\n\nThe conversion factor reported in Table 2 for general cases (1,5 × 10 –3 ) has been applied.","GLS (2012) - 2012/134/EU","1.2.3",20,20]
[1015,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Container glass","Unspecified","Unspecified","Unspecified","Fuel oil","Unspecified","Melting furnace","Emissions to air","Air","SOX expressed as SO4","SOX expressed as SO4","BAT is to reduce Sox emissions from the melting furnace by using one or a combination of the following techniques: (i) Dry or semi-dry scrubbing with a filtration system; (ii) minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance; (iii) Use of low sulphur content fuels","mg/Nm3","500","1200","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","For special types of coloured glasses (e.g. reduced green glasses), concerns related to the achievable emission levels may require investigating the sulphur balance. Values reported in the table may be difficult to achieve in combination with filter dust recycling and the rate of recycling of external cullet.\n\nThe lower levels are associated with conditions where the reduction of SO X is a high priority over a lower production of solid waste corresponding to the sulphate-rich filter dust.\n\nThe associated emission levels are related to the use of 1 % sulphur fuel oil in combination with secondary abatement techniques","GLS (2012) - 2012/134/EU","1.2.3",20,20]
[107,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Container glass","Unspecified","Unspecified","Unspecified","Fuel oil","Unspecified","Melting furnace","Emissions to air","Air","SOX expressed as SO5","SOX expressed as SO5","BAT is to reduce Sox emissions from the melting furnace by using one or a combination of the following techniques: (i) Dry or semi-dry scrubbing with a filtration system; (ii) minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance; (iii) Use of low sulphur content fuels","kg/tonne melted glass","0.75","1.8","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","For special types of coloured glasses (e.g. reduced green glasses), concerns related to the achievable emission levels may require investigating the sulphur balance. Values reported in the table may be difficult to achieve in combination with filter dust recycling and the rate of recycling of external cullet.\n\nThe lower levels are associated with conditions where the reduction of SO X is a high priority over a lower production of solid waste corresponding to the sulphate-rich filter dust.\n\nThe associated emission levels are related to the use of 1 % sulphur fuel oil in combination with secondary abatement techniques\n\nThe conversion factor reported in Table 2 for general cases (1,5 × 10 –3 ) has been applied.","GLS (2012) - 2012/134/EU","1.2.3",20,20]
[1027,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Container glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes","Emissions to air","Air","Tin compounds, including organotin, expressed as Sn","Tin compounds, including organotin, expressed as Sn","When tin, organotin or titanium compounds are used for hot-end coating operations, BAT is to reduce emissions by using one or a combination of the following techniques: (i) Minimising the losses of the coating product by ensuring a good sealing of the application system and applying an effective extracting hood; (ii) Combining the flue-gas from the coating operations with the waste gas from the melting furnace or with the combustion air of the furnace, when a secondary treatment system is applied (filter and dry or semi-dry scrubber); (iii) Applying a secondary technique, e.g. wet scrubbing, dry scrubbing plus filtration","mg/Nm3","N/A","5","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3","N/A","Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.2.6",22,22]
[1026,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Container glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes","Emissions to air","Air","Titanium compounds expressed as Ti","Titanium compounds expressed as Ti","When tin, organotin or titanium compounds are used for hot-end coating operations, BAT is to reduce emissions by using one or a combination of the following techniques: (i) Minimising the losses of the coating product by ensuring a good sealing of the application system and applying an effective extracting hood; (ii) Combining the flue-gas from the coating operations with the waste gas from the melting furnace or with the combustion air of the furnace, when a secondary treatment system is applied (filter and dry or semi-dry scrubber); (iii) Applying a secondary technique, e.g. wet scrubbing, dry scrubbing plus filtration","mg/Nm3","N/A",5,"Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3","N/A","Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.2.6",22,22]
[1181,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes- Curing oven emissions ","Emissions to air","Air","Total particulate matter","Particulates (PM10) (24 hr Mean)","BAT is to reduce emissions from downstream processes by using one or a combination of the following techniques: (i) Impact jets and cyclones; (ii) Wet scrubbers; (iii) Wet electrostatic precipitators; (iv) Stone wool filters; (v) Waste gas incineration","mg/Nm3","5","30","Amber",0,"273.15","101.3","N/A","Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.7.7",50,50]
[1181,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes- Curing oven emissions ","Emissions to air","Air","Total particulate matter","Particulates (PM10) (24 hr Mean)","BAT is to reduce emissions from downstream processes by using one or a combination of the following techniques: (i) Impact jets and cyclones; (ii) Wet scrubbers; (iii) Wet electrostatic precipitators; (iv) Stone wool filters; (v) Waste gas incineration","kg/tonne melted glass","N/A","0.2","Amber",0,"273.15","101.3","N/A","Daily average (continuous)","The specific mass emissions refer to 1 tonne of produced glass","GLS (2012) - 2012/134/EU","1.7.7",50,50]
[1175,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes- Forming area ","Emissions to air","Air","Total particulate matter","Particulates (PM10) (24 hr Mean)","BAT is to reduce emissions from downstream processes by using one or a combination of the following techniques: (i) Impact jets and cyclones; (ii) Wet scrubbers; (iii) Wet electrostatic precipitators; (iv) Stone wool filters; (v) Waste gas incineration","mg/Nm3","20","50","Amber",0,"273.15","101.3","N/A","Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.7.7",49,49]
[1191,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes- Curing oven emissions ","Emissions to air","Air","Total Volatile Organic compounds expressed as C","VOC","BAT is to reduce emissions from downstream processes by using one or a combination of the following techniques: (i) Impact jets and cyclones; (ii) Wet scrubbers; (iii) Wet electrostatic precipitators; (iv) Stone wool filters; (v) Waste gas incineration","mg/Nm3","N/A","10","Amber",0,"273.15","101.3","N/A","Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.7.7",50,50]
[1186,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes- Curing oven emissions ","Emissions to air","Air","Total Volatile Organic compounds expressed as C","VOC","BAT is to reduce emissions from downstream processes by using one or a combination of the following techniques: (i) Impact jets and cyclones; (ii) Wet scrubbers; (iii) Wet electrostatic precipitators; (iv) Stone wool filters; (v) Waste gas incineration","kg/tonne melted glass","N/A","0.065","Amber",0,"273.15","101.3","N/A","Daily average (continuous)","The specific mass emissions refer to 1 tonne of produced glass","GLS (2012) - 2012/134/EU","1.7.7",50,50]
[1180,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes- Forming area ","Emissions to air","Air","Total Volatile Organic compounds expressed as C","VOC","BAT is to reduce emissions from downstream processes by using one or a combination of the following techniques: (i) Impact jets and cyclones; (ii) Wet scrubbers; (iii) Wet electrostatic precipitators; (iv) Stone wool filters; (v) Waste gas incineration","mg/Nm3","10","30","Amber",0,"273.15","101.3","N/A","Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.7.7",50,50]
[1206,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","HTIW wools","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Emissions to air","Air","VOC","VOC","Primary and/or secondary techniques","mg/Nm3","10","20","Amber",0,"273.15","101.3",0.08,"Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.8.1",53,53]
[1231,"Iron and steel","2. Production and processing of metals","1.3. Coke production","Coke Oven Plants",0,"Unspecified","Unspecified","Unspecified","Unspecified",0,"Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","BAT for the coke oven underfiring is to reduce the emissions by using the following techniques: (i) preventing leakage between the oven chamber and the heating chamber by means of regular coke oven operation; (ii) repairing leakage between the oven chamber and the heating chamber (only applicable to existing plants); (iii) incorporating low-nitrogen oxides (NOX) techniques in the construction of new batteries, such as staged combustion\nand the use of thinner bricks and refractory with a better thermal conductivity (only applicable to new plants); (iv) using desulphurised coke oven gas (COG) process gases ","mg/Nm3",1,20,"Green","Discontinuous ",0,0,0.05,"Daily mean average",0,"IS (2012)\n2012/135/EU",1.4,87,25]
[1239,"Iron and steel","2. Production and processing of metals","1.3. Coke production","Coke Oven Plants",0,"Unspecified","Unspecified","Unspecified","Unspecified","Coke grading and handling","Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","BAT for coke grading and handling is to prevent or reduce dust emissions by using the following techniques in combination: (i)use of building or device enclosures; (ii) efficient extraction and subsequent dry dedusting ","mg/Nm3","N/A",10,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0,"IS (2012)\n2012/135/EU",1.4,88,26]
[1235,"Iron and steel","2. Production and processing of metals","1.3. Coke production","Coke Oven Plants",0,"Unspecified","Unspecified","Unspecified","Unspecified","Coke pushing","Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","BAT for coke pushing is to reduce dust emissions by using the following techniques: (i)  extraction by means of an integrated coke transfer machine equipped with a hood; (ii) using a one point or a mobile quenching car","mg/Nm3","N/A",20,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0,"IS (2012)\n2012/135/EU",1.4,87,25]
[1234,"Iron and steel","2. Production and processing of metals","1.3. Coke production","Coke Oven Plants",0,"Unspecified","Unspecified","Unspecified","Unspecified","Coke pushing","Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","BAT for coke pushing is to reduce dust emissions by using the following techniques: (i) using land-based extraction gas treatment with a bag filter or other abatement systems","mg/Nm3","N/A",10,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0,"IS (2012)\n2012/135/EU",1.4,87,25]
[1236,"Iron and steel","2. Production and processing of metals","1.3. Coke production","Coke Oven Plants",0,"Unspecified","Unspecified","Unspecified","Unspecified","Coke quenching","Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","BAT for coke quenching is to reduce dust emissions by using one of the following techniques: (i) using coke dry quenching (CDQ) with the recovery of sensible heat and the removal of dust from charging, handling\nand screening operations by means of a bag filter","mg/Nm3","N/A",20,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0,"IS (2012)\n2012/135/EU",1.4,88,26]
[1238,"Iron and steel","2. Production and processing of metals","1.3. Coke production","Coke Oven Plants",0,"Unspecified","Unspecified","Unspecified","Unspecified","Coke quenching","Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","BAT for coke quenching is to reduce dust emissions by using one of the following techniques: (i) using coke stabilisation quenching (CSQ)","g/t","N/A",10,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0,"IS (2012)\n2012/135/EU",1.4,88,26]
[1237,"Iron and steel","2. Production and processing of metals","1.3. Coke production","Coke Oven Plants",0,"Unspecified","Unspecified","Unspecified","Unspecified","Coke quenching","Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","BAT for coke quenching is to reduce dust emissions by using one of the following techniques: (i) using emission-minimised conventional wet quenching","g/t","N/A",25,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0,"IS (2012)\n2012/135/EU",1.4,88,26]
[1259,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.",0,0,"Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: Basic oxygen furnace (BOF) gas recovery by supressed combustion","Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","BAT for basic oxygen furnace (BOF) gas recovery by suppressed combustion is to extract the BOF gas during blowing as much as possible and to clean it by using the following techniques in combination: (i) use of a suppressed combustion process; (ii) prededusting to remove coarse dust by means of dry separation techniques (e.g. deflector, cyclone) or wet separators; (iii) dust abatement by means of dry dedusting for new and existing plants or wet dedusting for existing plants\n","mg/Nm3",10,30,"Green","Continuous",0,0,"Unspecified ",0,"This BAT AEL is for dust abatement by dry dedusting","IS (2012)\n2012/135/EU",1.6,93,31]
[1260,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.",0,0,"Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: Basic oxygen furnace (BOF) gas recovery by supressed combustion","Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","BAT for basic oxygen furnace (BOF) gas recovery by suppressed combustion is to extract the BOF gas during blowing as much as possible and to clean it by using the following techniques in combination: (i) use of a suppressed combustion process; (ii) prededusting to remove coarse dust by means of dry separation techniques (e.g. deflector, cyclone) or wet separators; (iii) dust abatement by means of dry dedusting for new and existing plants or wet dedusting for existing plants\n","mg/Nm3","N/A",50,"Green","Continuous",0,0,"Unspecified ",0,"This BAT AEL is for dust abatement by wet dedusting","IS (2012)\n2012/135/EU",1.6,93,31]
[1261,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.",0,0,"Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: Basic oxygen furnace (BOF) gas recovery during oxygen blowing in the case of full combustion","Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","BAT for basic oxygen furnace (BOF) gas recovery during oxygen blowing in the case of full combustion is to\nreduce dust emissions by using one of the following techniques:  dry dedusting (e.g. ESP or bag filter) for new and existing plants","mg/Nm3",10,30,"Green","Continuous",0,0,"Unspecified ","Average over the sampling period",0,"IS (2012)\n2012/135/EU",1.6,93,31]
[1262,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.",0,0,"Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: Basic oxygen furnace (BOF) gas recovery during oxygen blowing in the case of full combustion","Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","BAT for basic oxygen furnace (BOF) gas recovery during oxygen blowing in the case of full combustion is to\nreduce dust emissions by using one of the following techniques:  wet dedusting (e.g. ESP or bag filter) for existing plants","mg/Nm3","N/A",50,"Green","Continuous",0,0,"Unspecified ","Average over the sampling period",0,"IS (2012)\n2012/135/EU",1.6,93,31]
[1267,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.",0,0,"Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: On-site slag processing ","Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","BAT for on-site slag processing is to reduce dust emissions by using one or a combination of the following\ntechniques: (i) Efficient extraction of the slag crusher and screening devices with subsequent off-gas cleaning, if relevant; (ii) transport of untreated slag by shovel loaders; (iii) extraction or wetting of conveyor transfer points for broken material; (iv) wetting of slag storage heaps; (v) use of water fogs when broken slag is loaded\n","mg/Nm3",10,20,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0,"IS (2012)\n2012/135/EU",1.6,94,32]
[1263,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.",0,0,"Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: Secondary dusting, reladling of hot metal from the torpedo ladle, hot metal pretreatment, BOF-related processes, secondary metallurgy and continuous casting","Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","BAT is to minimise dust emissions by means of process integrated techniques, such as general techniques to prevent or control\ndiffuse or fugitive emissions, and by using appropriate enclosures and hoods with efficient extraction and a subsequent\noff-gas cleaning by means of a bag filter or an ESP.","mg/Nm3",1,15,"Green","Discontinuous ",0,0,"Unspecified ","Daily mean value","This BAT-AEL is in the case of bag filters ","IS (2012)\n2012/135/EU",1.6,93,31]
[1264,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.",0,0,"Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: Secondary dusting, reladling of hot metal from the torpedo ladle, hot metal pretreatment, BOF-related processes, secondary metallurgy and continuous casting","Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","BAT is to minimise dust emissions by means of process integrated techniques, such as general techniques to prevent or control\ndiffuse or fugitive emissions, and by using appropriate enclosures and hoods with efficient extraction and a subsequent\noff-gas cleaning by means of a bag filter or an ESP.","mg/Nm3","N/A",20,"Green","Continuous",0,0,"Unspecified ","Daily mean value","This BAT-AEL is in the case of electrostatic precipitators ","IS (2012)\n2012/135/EU",1.6,93,31]
[1265,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.",0,0,"Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: Secondary dusting, reladling of hot metal from the torpedo ladle, hot metal pretreatment, BOF-related processes, secondary metallurgy and continuous casting","Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","BAT is to minimise dust emissions by means of process integrated techniques, such as general techniques to prevent or control\ndiffuse or fugitive emissions, and by using appropriate enclosures and hoods with efficient extraction and a subsequent\noff-gas cleaning by means of a bag filter or an ESP.","mg/Nm3",1,10,"Green","Continuous",0,0,"Unspecified ","Daily mean value","This BAT-AEL is in the case of bag filters if the emissions from hot metal pretreatment and the secondary metallurgy are treated separately ","IS (2012)\n2012/135/EU",1.6,93,31]
[1266,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.",0,0,"Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: Secondary dusting, reladling of hot metal from the torpedo ladle, hot metal pretreatment, BOF-related processes, secondary metallurgy and continuous casting","Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","BAT is to minimise dust emissions by means of process integrated techniques, such as general techniques to prevent or control\ndiffuse or fugitive emissions, and by using appropriate enclosures and hoods with efficient extraction and a subsequent\noff-gas cleaning by means of a bag filter or an ESP.","mg/Nm3","N/A",20,"Green","Continuous",0,0,"Unspecified ","Daily mean value","This BAT-AEL is in the case of electrostatic precipitators if the emissions from hot metal pretreatment and the secondary metallurgy are treated separately ","IS (2012)\n2012/135/EU",1.6,93,31]
[1268,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.",0,0,"Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: Waste water from continous casting machines ","Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","BAT is to minimise the waste water discharge from continuous casting by using the following techniques in combination: (i) the removal of solids by flocculation, sedimentation and/or filtration; (ii) the removal of oil in skimming tanks or any other effective device; (iii) the recirculation of cooling water and water from vacuum generation as much as possible.","mg/l","N/A",20,"Green","Discontinuous ",0,0,"Unspecified ","Random sample or a 24 hour composite sample ",0,"IS (2012)\n2012/135/EU",1.6,95,33]
[1269,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.",0,0,"Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: Waste water from continous casting machines ","Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","BAT is to minimise the waste water discharge from continuous casting by using the following techniques in combination: (i) the removal of solids by flocculation, sedimentation and/or filtration; (ii) the removal of oil in skimming tanks or any other effective device; (iii) the recirculation of cooling water and water from vacuum generation as much as possible.","mg/l","N/A",5,"Green","Discontinuous ",0,0,"Unspecified ","Random sample or a 24 hour composite sample ",0,"IS (2012)\n2012/135/EU",1.6,95,33]
[1270,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.",0,0,"Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: Waste water from continous casting machines ","Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","BAT is to minimise the waste water discharge from continuous casting by using the following techniques in combination: (i) the removal of solids by flocculation, sedimentation and/or filtration; (ii) the removal of oil in skimming tanks or any other effective device; (iii) the recirculation of cooling water and water from vacuum generation as much as possible.","mg/l","N/A",2,"Green","Discontinuous ",0,0,"Unspecified ","Random sample or a 24 hour composite sample ",0,"IS (2012)\n2012/135/EU",1.6,95,33]
[1271,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.",0,0,"Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: Waste water from continous casting machines ","Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","BAT is to minimise the waste water discharge from continuous casting by using the following techniques in combination: (i) the removal of solids by flocculation, sedimentation and/or filtration; (ii) the removal of oil in skimming tanks or any other effective device; (iii) the recirculation of cooling water and water from vacuum generation as much as possible.","mg/l","N/A",0.5,"Green","Discontinuous ",0,0,"Unspecified ","Random sample or a 24 hour composite sample ",0,"IS (2012)\n2012/135/EU",1.6,95,33]
[1272,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.",0,0,"Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: Waste water from continous casting machines ","Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","BAT is to minimise the waste water discharge from continuous casting by using the following techniques in combination: (i) the removal of solids by flocculation, sedimentation and/or filtration; (ii) the removal of oil in skimming tanks or any other effective device; (iii) the recirculation of cooling water and water from vacuum generation as much as possible.","mg/l","N/A",0.5,"Green","Discontinuous ",0,0,"Unspecified ","Random sample or a 24 hour composite sample ",0,"IS (2012)\n2012/135/EU",1.6,95,33]
[1273,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.",0,0,"Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: Waste water from continous casting machines ","Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","BAT is to minimise the waste water discharge from continuous casting by using the following techniques in combination: (i) the removal of solids by flocculation, sedimentation and/or filtration; (ii) the removal of oil in skimming tanks or any other effective device; (iii) the recirculation of cooling water and water from vacuum generation as much as possible.","mg/l","N/A",5,"Green","Discontinuous ",0,0,"Unspecified ","Random sample or a 24 hour composite sample ",0,"IS (2012)\n2012/135/EU",1.6,95,33]
[1250,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.",0,0,"Unspecified","Unspecified","Unspecified","Unspecified","Blast Furnaces: Blast furnace gas ","Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","BAT is to reduce dust emissions from the blast furnace gas by using one or a combination of the following techniques:\n\nUsing dry predusting devices: (i) deflectors; (ii) dust catchers; (iii) cyclones; (iv) electrostatic precipitators.\n\nSubsequent dust abatement: (i) hurdle-type scrubbers; (ii) venturi scrubbers; (iii) annular gap scrubbers; (iv) wet electrostatic precipitators; (v) disintegrators ","mg/Nm3","N/A",10,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0,"IS (2012)\n2012/135/EU",1.5,90,28]
[1249,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.",0,0,"Unspecified","Unspecified","Unspecified","Unspecified","Blast Furnaces: casting house ","Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","BAT for casting house (tap holes, runners, torpedo ladles charging points, skimmers) is to prevent or reduce diffuse dust emissions by using the following techniques: (i) Covering runners; (ii) optimising the capture efficiency for diffuse dust emissions and fumes with subsequent off-gas cleaning by means of\nan electrostatic precipitator or bag filter; (iii) ume suppression using nitrogen while tapping, where applicable and where no collecting and dedusting system for\ntapping emissions is installed.\n","mg/Nm3",1,15,"Amber",0,0,0,"Unspecified ","Daily mean value",0,"IS (2012)\n2012/135/EU",1.5,90,28]
[1252,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.",0,0,"Unspecified","Unspecified","Unspecified","Unspecified","Blast Furnaces: Hot blast stoves","Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","BAT for hot blast stoves is to reduce emissions by using desulphurised and dedusted surplus coke oven gas, dedusted blast furnace gas, dedusted basic oxygen furnace gas and natural gas, individually or in combination.","mg/Nm3","N/A",10,"Green","Discontinuous ",0,0,0.03,"Daily mean values",0,"IS (2012)\n2012/135/EU",1.5,91,29]
[1248,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.",0,0,"Unspecified","Unspecified","Unspecified","Unspecified","Blast Furnaces: Loading from the storage bunkers of the coal injection unit","Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","BAT for displaced air during loading from the storage bunkers of the coal injection unit is to capture dust emissions and perform subsequent dry dedusting.","mg/Nm3","N/A",20,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0,"IS (2012)\n2012/135/EU",1.4,89,27]
[1274,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.",0,0,"Unspecified","Unspecified","Unspecified","Unspecified","Electric arc furnace steelmaking and casting: Electric Arc Furnace (EAF) primary and secondary dedusting","Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","BAT for the electric arc furnace (EAF) primary and secondary dedusting (including scrap preheating, charging, melting, tapping, ladle furnace and secondary metallurgy) is to achieve an efficient extraction of all emission sources by using one of the techniques listed below and to use subsequent dedusting by means of a bag filter: (i) a combination of direct off-gas extraction (4th or 2nd hole) and hood systems; (ii) direct gas extraction and doghouse systems; (iii) direct gas extraction and total building evacuation (low-capacity electric arc furnaces (EAF) may not require direct gas\nextraction to achieve the same extraction efficiency)\n\n","mg/Nm3","N/A",5,"Green","Continuous",0,0,"Unspecified ","Daily mean value",0,"IS (2012)\n2012/135/EU",1.7,96,34]
[1277,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.",0,0,"Unspecified","Unspecified","Unspecified","Unspecified","Electric arc furnace steelmaking and casting: On-site slag processing ","Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","BAT for on-site slag processing is to reduce dust emissions by using one or a combination of the following techniques: (i) efficient extraction of the slag crusher and screening devices with subsequent off-gas cleaning, if relevant; (ii) transport of untreated slag by shovel loaders; (iii) extraction or wetting of conveyor transfer points for broken material; (iv) wetting of slag storage heaps; (v) use of water fogs when broken slag is loaded","mg/Nm3",10,20,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0,"IS (2012)\n2012/135/EU",1.7,97,35]
[1215,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.","Pelletisation plans",0,"Unspecified","Unspecified","Unspecified","Unspecified","Crushing. Grinding and drying","Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","BAT is to reduce the dust emissions in the waste gases by using one or a combination of the following techniques: (i) an electrostatic precipitator; (ii) a bag filter; (iii) a wet scrubber","mg/Nm3","N/A",20,"Green","Discontinuous ",0,0,"Unspecified ","Daily mean values",0,"IS (2012)\n2012/135/EU",1.3,83,21]
[1216,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.","Pelletisation plans",0,"Unspecified","Unspecified","Unspecified","Unspecified","Induration strand; Pellet handling and screening ","Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","BAT is to reduce the dust emissions in the waste gases by using one or a combination of the following techniques: (i) an electrostatic precipitator; (ii) a bag filter; (iii) a wet scrubber","mg/Nm3",10,15,"Green","Discontinuous ",0,0,"Unspecified ","Daily mean values",0,"IS (2012)\n2012/135/EU",1.3,83,21]
[1201,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.","Sinter Plant",0,"Unspecified","Unspecified","Unspecified","Unspecified","Sinter strand","Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","BAT for primary emissions for existing plants is to reduce dust emissions from the sinter strand waste gas by using\nadvanced electrostatic precipitators when bag filters are not applicable.","mg/Nm3",20,40,"Green","Continuous",0,0,"Unspecified ","Daily mean value","The advanced electrostatic precipitator  should be designed and operated to achieve these values","IS (2012)\n2012/135/EU",1.2,77,15]
[1200,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.","Sinter Plant",0,"Unspecified","Unspecified","Unspecified","Unspecified","Sinter strand","Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","BAT for primary emissions from sinter plants is to reduce dust emissions from the sinter strand waste gas by means of a bag filter.\n\n","mg/Nm3",1,15,"Green","Continuous",0,0,"Unspecified ","Daily mean value",0,"IS (2012)\n2012/135/EU",1.2,77,15]
[1211,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.","Sinter Plant",0,"Unspecified","Unspecified","Unspecified","Unspecified","Sinter strand","Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","BAT for secondary emissions from sinter strand discharge, sinter crushing, cooling, screening and conveyor transfer points is to prevent dust emissions and/or to achieve an efficient extraction and subsequently to reduce dust emissions by using : an electrostatic precipitator or a bag filter","mg/Nm3","N/A",30,"Green","Continuous",0,0,"Unspecified ","Daily mean value",0,"IS (2012)\n2012/135/EU",1.2,81,19]
[1210,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.","Sinter Plant",0,"Unspecified","Unspecified","Unspecified","Unspecified","Sinter strand","Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","BAT for secondary emissions from sinter strand discharge, sinter crushing, cooling, screening and conveyor transfer points is to prevent dust emissions and/or to achieve an efficient extraction and subsequently to reduce dust emissions by using : Hooding and/or enclosure","mg/Nm3","N/A",10,"Green","Continuous",0,0,"Unspecified ","Daily mean value",0,"IS (2012)\n2012/135/EU",1.2,81,19]
[1226,"Iron and steel","2. Production and processing of metals","1.3. Coke production","Coke Oven Plants",0,"Unspecified","Unspecified","Unspecified","Unspecified","Coal charging systems ","Emissions to air ","Air","Dust ","Particulates (PM10) (24 hr Mean)","BAT is to charge coke oven chambers with emission-reduced charging systems. \n\nIf, however, the gases are extracted and treated outside the coke oven, charging with a land-based treatment of the\nextracted gases is the preferred method. Treatment should consist of an efficient extraction of the emissions with\nsubsequent combustion to reduce organic compounds and the use of a bag filter to reduce particulates.","g/t","N/A",5,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0,"IS (2012)\n2012/135/EU",1.4,85,23]
[1227,"Iron and steel","2. Production and processing of metals","1.3. Coke production","Coke Oven Plants",0,"Unspecified","Unspecified","Unspecified","Unspecified","Coal charging systems ","Emissions to air ","Air","Dust ","Particulates (PM10) (24 hr Mean)","BAT is to charge coke oven chambers with emission-reduced charging systems. \n\nIf, however, the gases are extracted and treated outside the coke oven, charging with a land-based treatment of the\nextracted gases is the preferred method. Treatment should consist of an efficient extraction of the emissions with\nsubsequent combustion to reduce organic compounds and the use of a bag filter to reduce particulates.","mg/Nm3","N/A",50,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0,"IS (2012)\n2012/135/EU",1.4,85,23]
[1225,"Iron and steel","2. Production and processing of metals","1.3. Coke production","Coke Oven Plants",0,"Unspecified","Unspecified","Unspecified","Unspecified","Storage and handling of pulverised coal","Emissions to air ","Air","Dust ","Particulates (PM10) (24 hr Mean)","BAT for storage and handling of pulverised coal is to prevent or reduce diffuse dust emissions by using one or a combination of the following techniques: (i) storing pulverised materials in bunkers and warehouses; (ii) using closed or enclosed conveyors; (iii)  minimising the drop heights depending on the plant size and construction; (iv) reducing emissions from charging of the coal tower and the charging car; (v) using efficient extraction and subsequent dedusting\n","mg/Nm3",10,20,"Amber",0,0,0,"Unspecified ","Average over the sampling period",0,"IS (2012)\n2012/135/EU",1.4,85,23]
[1219,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.","Pelletisation plans",0,"Unspecified","Unspecified","Unspecified","Unspecified","Induration strand","Emissions to air ","Air","Hydrogen chloride, expressed as HCl","Hydrogen chloride","BAT is to reduce the sulphur oxides (SOX), hydrogen chloride (HCl) and hydrogen fluoride (HF) emissions from the\ninduration strand waste gas by using one of the following techniques: (i) a wet scrubber; (ii) semi-dry absorption with a subsequent dedusting system","mg/Nm3",1,3,"Green","Discontinuous ","Unspecified ","Unspecified ","Unspecified ","Daily mean values",0,"IS (2012)\n2012/135/EU",1.3,83,21]
[1218,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.","Pelletisation plans",0,"Unspecified","Unspecified","Unspecified","Unspecified","Induration strand","Emissions to air ","Air","Hydrogen fluoride (HF)","Hydrogen fluoride (as F) (Ecological - Daily Mean)","BAT is to reduce the sulphur oxides (SOX), hydrogen chloride (HCl) and hydrogen fluoride (HF) emissions from the\ninduration strand waste gas by using one of the following techniques: (i) a wet scrubber; (ii) semi-dry absorption with a subsequent dedusting system","mg/Nm3",1,3,"Green","Discontinuous ","Unspecified ","Unspecified ","Unspecified ","Daily mean values",0,"IS (2012)\n2012/135/EU",1.3,83,21]
[1279,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.",0,0,"Unspecified","Unspecified","Unspecified","Unspecified","Electric arc furnace steelmaking and casting: Waste water from continous casting machines ","Emissions to air ","Air","Iron","Iron","BAT is to minimise the waste water discharge from continuous casting by using the following techniques in combination: (i) the removal of solids by flocculation, sedimentation and/or filtration; (ii) the removal of oil in skimming tanks or any other effective device; (iii) the recirculation of cooling water and water from vacuum generation as much as possible","mg/Nm3","N/A",5,"Green","Discontinuous ",0,0,"Unspecified ","Qualified random sample or a 24 hour composite",0,"IS (2012)\n2012/135/EU",1.7,97,35]
[1275,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.",0,0,"Unspecified","Unspecified","Unspecified","Unspecified","Electric arc furnace steelmaking and casting: Electric Arc Furnace (EAF) primary and secondary dedusting","Emissions to air ","Air","Mercury","Mercury and compounds, except mercury alkyls, (as","BAT for the electric arc furnace (EAF) primary and secondary dedusting (including scrap preheating, charging, melting, tapping, ladle furnace and secondary metallurgy) is to achieve an efficient extraction of all emission sources by using one of the techniques listed below and to use subsequent dedusting by means of a bag filter: (i) a combination of direct off-gas extraction (4th or 2nd hole) and hood systems; (ii) direct gas extraction and doghouse systems; (iii) direct gas extraction and total building evacuation (low-capacity electric arc furnaces (EAF) may not require direct gas\nextraction to achieve the same extraction efficiency)\n\n","mg/Nm3","N/A",0.05,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0,"IS (2012)\n2012/135/EU",1.7,96,34]
[1202,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.","Sinter Plant",0,"Unspecified","Unspecified","Unspecified","Unspecified","Sinter strand","Emissions to air ","Air","Mercury","Mercury and compounds, except mercury alkyls, (as","BAT for primary emissions from sinter strands is to prevent or reduce mercury emissions by selecting raw materials with a low mercury content or to treat waste gases in combination with activated carbon or\nactivated lignite coke injection.","mg/Nm3",0.03,0.05,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period","Discontinuous measurement, spot samples for at least half an hour","IS (2012)\n2012/135/EU",1.2,78,16]
[1281,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.",0,0,"Unspecified","Unspecified","Unspecified","Unspecified","Electric arc furnace steelmaking and casting: Waste water from continous casting machines ","Emissions to air ","Air","Nickel","Nickel (total Ni compounds in the PM10 fraction)","BAT is to minimise the waste water discharge from continuous casting by using the following techniques in combination: (i) the removal of solids by flocculation, sedimentation and/or filtration; (ii) the removal of oil in skimming tanks or any other effective device; (iii) the recirculation of cooling water and water from vacuum generation as much as possible","mg/Nm3","N/A",0.5,"Green","Discontinuous ",0,0,"Unspecified ","Qualified random sample or a 24 hour composite",0,"IS (2012)\n2012/135/EU",1.7,97,35]
[1232,"Iron and steel","2. Production and processing of metals","1.3. Coke production","Coke Oven Plants",0,"Unspecified","New or substantially revamped","Unspecified","Unspecified",0,"Emissions to air ","Air","Nitrogen oxides (NOx)","Nitrogen dioxide","BAT for the coke oven underfiring is to reduce the emissions by using the following techniques: (i) preventing leakage between the oven chamber and the heating chamber by means of regular coke oven operation; (ii) repairing leakage between the oven chamber and the heating chamber (only applicable to existing plants); (iii) incorporating low-nitrogen oxides (NOX) techniques in the construction of new batteries, such as staged combustion\nand the use of thinner bricks and refractory with a better thermal conductivity (only applicable to new plants); (iv) using desulphurised coke oven gas (COG) process gases ","mg/Nm3",350,500,"Green","Discontinuous ",0,0,0.05,"Daily mean average","This BAT is for new or substantially revamped\nplants (less than 10 years old)","IS (2012)\n2012/135/EU",1.4,87,25]
[1233,"Iron and steel","2. Production and processing of metals","1.3. Coke production","Coke Oven Plants",0,"Unspecified","Old","Unspecified","Unspecified",0,"Emissions to air ","Air","Nitrogen oxides (NOx)","Nitrogen dioxide","BAT for the coke oven underfiring is to reduce the emissions by using the following techniques: (i) preventing leakage between the oven chamber and the heating chamber by means of regular coke oven operation; (ii) repairing leakage between the oven chamber and the heating chamber (only applicable to existing plants); (iii) incorporating low-nitrogen oxides (NOX) techniques in the construction of new batteries, such as staged combustion\nand the use of thinner bricks and refractory with a better thermal conductivity (only applicable to new plants); (iv) using desulphurised coke oven gas (COG) process gases ","mg/Nm3",500,650,"Green","Discontinuous ",0,0,0.05,"Daily mean average","This BAT is for older plants with well maintained batteries and incorporated low- nitrogen oxides (NOX) techniques.","IS (2012)\n2012/135/EU",1.4,87,25]
[1205,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.","Sinter Plant",0,"Unspecified","Unspecified","Unspecified","Unspecified","Sinter strand","Emissions to air ","Air","Nitrogen oxides (NOx)","Nitrogen dioxide","BAT for primary emissions from sinter strands is to reduce total nitrogen oxides (NOX) emissions by using one or\na combination of the following techniques:\n\nProcess integrated measures which can include: (i) waste gas recirculation; (ii) other primary measures, such as the use of anthracite or the use of low-NOX burners for ignition\n\n","mg/Nm3","N/A",500,"Green","Continuous",0,0,"Unspecified ","Daily mean value",0,"IS (2012)\n2012/135/EU",1.2,79,17]
[1207,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.","Sinter Plant",0,"Unspecified","Unspecified","Unspecified","Unspecified","Sinter strand","Emissions to air ","Air","Nitrogen oxides (NOx)","Nitrogen dioxide","End-of-pipe techniques which can include:  selective catalytic reduction (SCR)","mg/Nm3","N/A",120,"Green","Continuous",0,0,0.15,"Daily mean value",0,"IS (2012)\n2012/135/EU",1.2,79,17]
[1206,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.","Sinter Plant",0,"Unspecified","Unspecified","Unspecified","Unspecified","Sinter strand","Emissions to air ","Air","Nitrogen oxides (NOx)","Nitrogen dioxide","End-of-pipe techniques which can include: the regenerative activated carbon (RAC) process","mg/Nm3","N/A",250,"Green","Continuous",0,0,0.15,"Daily mean value",0,"IS (2012)\n2012/135/EU",1.2,79,17]
[1253,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.",0,0,"Unspecified","Unspecified","Unspecified","Unspecified","Blast Furnaces: Hot blast stoves","Emissions to air ","Air","Nitrogen oxides (NOx), expressed as Nitrogen dioxide (NO2)","Nitrogen dioxide","BAT for hot blast stoves is to reduce emissions by using desulphurised and dedusted surplus coke oven gas, dedusted blast furnace gas, dedusted basic oxygen furnace gas and natural gas, individually or in combination.","mg/Nm3","N/A",100,"Green","Discontinuous ",0,0,0.03,"Daily mean values",0,"IS (2012)\n2012/135/EU",1.5,91,29]
[1276,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.",0,0,"Unspecified","Unspecified","Unspecified","Unspecified","Electric arc furnace steelmaking and casting: Electric Arc Furnace (EAF) primary and secondary dedusting","Emissions to air ","Air","Polychlorinated dibenzodioxins/furans (PCDD/F)","PCDD/F","BAT for the electric arc furnace (EAF) primary and secondary dedusting (including scrap preheating, charging, melting, tapping, ladle furnace and secondary metallurgy) is to prevent and reduce polychlorinated dibenzodioxins/furans (PCDD/F) and polychlorinated biphenyls (PCB) emissions by avoiding, as much as possible, raw materials which contain PCDD/F and PCB or their precursors (see BAT 6 and 7) and using one or a combination of the following techniques, in conjunction with an appropriate dust removal system: (i) appropriate post-combustion; (ii) appropriate rapid quenching; (iii) injection of adequate adsorption agents into the duct before dedusting.","ng I-TEQ/Nm3","N/A",0.1,"Green","Discontinuous ",0,0,"Unspecified ","6-8 hour random sample","In some cases, the BAT-associated emission level can be achieved with primary measures only.","IS (2012)\n2012/135/EU",1.7,97,35]
[1208,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.","Sinter Plant",0,"Unspecified","Unspecified","Unspecified","Unspecified","Sinter strand","Emissions to air ","Air","Polychlorinated dibenzodioxins/furans (PCDD/F)","PCDD/F","BAT for primary emissions from sinter strands is to reduce emissions of polychlorinated dibenzodioxins/furans (PCDD/F) and polychlorinated biphenyls (PCB) by the injection of adequate adsorption agents into the waste gas duct of the sinter strand before dedusting with a bag filter ","ng I-TEQ/Nm3",0.05,0.2,"Green","Discontinuous ",0,0,0,0,0,"IS (2012)\n2012/135/EU",1.2,80,18]
[1209,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.","Sinter Plant",0,"Unspecified","Unspecified","Unspecified","Unspecified","Sinter strand","Emissions to air ","Air","Polychlorinated dibenzodioxins/furans (PCDD/F)","PCDD/F","BAT for primary emissions from sinter strands is to reduce emissions of polychlorinated dibenzodioxins/furans (PCDD/F) and polychlorinated biphenyls (PCB) by the injection of adequate adsorption agents into the waste gas duct of the sinter strand before dedusting with an advanced electrostatic precipitators when bag filters are not applicable","ng I-TEQ/Nm3",0.2,0.4,"Green","Discontinuous ",0,0,"Unspecified ","6-8 hour random sample",0,"IS (2012)\n2012/135/EU",1.2,80,18]
[1228,"Iron and steel","2. Production and processing of metals","1.3. Coke production","Coke Oven Plants",0,"Unspecified","Unspecified","Unspecified","Unspecified","Coke oven gas (COG)","Emissions to air ","Air","Residual hydrogen sulphide (H2S)","Hydrogen sulphide","BAT is to reduce the sulphur content of the coke oven gas (COG) by: (i) desulphurisation by absorption systems","mg/Nm3",300,1000,"Green","Discontinuous ",0,0,"Unspecified ","Daily mean average",0,"IS (2012)\n2012/135/EU",1.4,87,25]
[1229,"Iron and steel","2. Production and processing of metals","1.3. Coke production","Coke Oven Plants",0,"Unspecified","Unspecified","Unspecified","Unspecified","Coke oven gas (COG)","Emissions to air ","Air","Residual hydrogen sulphide (H2S)","Hydrogen sulphide","BAT is to reduce the sulphur content of the coke oven gas (COG) by: (ii)  wet oxidative desulphurisation","mg/Nm3","N/A",10,"Green","Discontinuous ",0,0,"Unspecified ","Daily mean average",0,"IS (2012)\n2012/135/EU",1.4,87,25]
[1203,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.","Sinter Plant",0,"Unspecified","Unspecified","Unspecified","Unspecified","Sinter strand","Emissions to air ","Air","SOx","Sulphur Dioxide (24 Hour Mean)","BAT for primary emissions from sinter strands is to reduce sulphur oxide (SOX) emissions by using one or a\ncombination of the following techniques: (i)lowering the sulphur input by using coke breeze with a low sulphur content; (ii) lowering the sulphur input by minimisation of coke breeze consumption; (iii)  lowering the sulphur input by using iron ore with a low sulphur content; (iv) injection of adequate adsorption agents into the waste gas duct of the sinter strand before dedusting by bag filter","mg/Nm3",350,500,"Green","Continuous",0,0,"Unspecified ","Daily mean value","The lower value is assoviated with BAT (iv) ","IS (2012)\n2012/135/EU",1.2,78,16]
[1204,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.","Sinter Plant",0,"Unspecified","Unspecified","Unspecified","Unspecified","Sinter strand","Emissions to air ","Air","SOx","Sulphur Dioxide (24 Hour Mean)","Wet desulphurisation or regenerative activated carbon (RAC) process (with particular consideration for the prerequisites for application)","mg/Nm3","N/A",100,"Green","Continuous",0,0,"Unspecified ","Daily mean value",0,"IS (2012)\n2012/135/EU",1.2,78,16]
[1230,"Iron and steel","2. Production and processing of metals","1.3. Coke production","Coke Oven Plants",0,"Unspecified","Unspecified","Unspecified","Unspecified",0,"Emissions to air ","Air","Sulphur oxides (SOx)","Sulphur Dioxide (24 Hour Mean)","BAT for the coke oven underfiring is to reduce the emissions by using the following techniques: (i) preventing leakage between the oven chamber and the heating chamber by means of regular coke oven operation; (ii) repairing leakage between the oven chamber and the heating chamber (only applicable to existing plants); (iii) incorporating low-nitrogen oxides (NOX) techniques in the construction of new batteries, such as staged combustion\nand the use of thinner bricks and refractory with a better thermal conductivity (only applicable to new plants); (iv) using desulphurised coke oven gas (COG) process gases ","mg/Nm3",200,500,"Green","Discontinuous ",0,0,0.05,"Daily mean average",0,"IS (2012)\n2012/135/EU",1.4,87,25]
[1217,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.","Pelletisation plans",0,"Unspecified","Unspecified","Unspecified","Unspecified","Induration strand","Emissions to air ","Air","Sulphur oxides (SOx)","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce the sulphur oxides (SOX), hydrogen chloride (HCl) and hydrogen fluoride (HF) emissions from the\ninduration strand waste gas by using one of the following techniques: (i) a wet scrubber; (ii) semi-dry absorption with a subsequent dedusting system","mg/Nm3",30,50,"Green","Continuous",0,0,"Unspecified ","Daily mean values",0,"IS (2012)\n2012/135/EU",1.3,83,21]
[1251,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.",0,0,"Unspecified","Unspecified","Unspecified","Unspecified","Blast Furnaces: Hot blast stoves","Emissions to air ","Air","Sulphur oxides (SOx) expressed as Sulphur dioxide (SO2)","Sulphur Dioxide (24 Hour Mean)","BAT for hot blast stoves is to reduce emissions by using desulphurised and dedusted surplus coke oven gas, dedusted blast furnace gas, dedusted basic oxygen furnace gas and natural gas, individually or in combination.","mg/Nm3","N/A",200,"Green","Discontinuous ",0,0,0.03,"Daily mean values",0,"IS (2012)\n2012/135/EU",1.5,91,29]
[1278,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.",0,0,"Unspecified","Unspecified","Unspecified","Unspecified","Electric arc furnace steelmaking and casting: Waste water from continous casting machines ","Emissions to water","Water","Suspended solids","Suspended solids","BAT is to minimise the waste water discharge from continuous casting by using the following techniques in combination: (i) the removal of solids by flocculation, sedimentation and/or filtration; (ii) the removal of oil in skimming tanks or any other effective device; (iii) the recirculation of cooling water and water from vacuum generation as much as possible","mg/Nm3","N/A",20,"Green","Discontinuous ",0,0,"Unspecified ","Qualified random sample or a 24 hour composite",0,"IS (2012)\n2012/135/EU",1.7,97,35]
[1282,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.",0,0,"Unspecified","Unspecified","Unspecified","Unspecified","Electric arc furnace steelmaking and casting: Waste water from continous casting machines ","Emissions to air ","Air","Total chromium","Chromium (VI) compounds (as Cr)","BAT is to minimise the waste water discharge from continuous casting by using the following techniques in combination: (i) the removal of solids by flocculation, sedimentation and/or filtration; (ii) the removal of oil in skimming tanks or any other effective device; (iii) the recirculation of cooling water and water from vacuum generation as much as possible","mg/Nm3","N/A",0.5,"Green","Discontinuous ",0,0,"Unspecified ","Qualified random sample or a 24 hour composite",0,"IS (2012)\n2012/135/EU",1.7,97,35]
[1283,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.",0,0,"Unspecified","Unspecified","Unspecified","Unspecified","Electric arc furnace steelmaking and casting: Waste water from continous casting machines ","Emissions to air ","Air","Total hydrocarbons","Total hydrocarbons","BAT is to minimise the waste water discharge from continuous casting by using the following techniques in combination: (i) the removal of solids by flocculation, sedimentation and/or filtration; (ii) the removal of oil in skimming tanks or any other effective device; (iii) the recirculation of cooling water and water from vacuum generation as much as possible","mg/Nm3","N/A",5,"Green","Discontinuous ",0,0,"Unspecified ","Qualified random sample or a 24 hour composite",0,"IS (2012)\n2012/135/EU",1.7,97,35]
[1280,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.",0,0,"Unspecified","Unspecified","Unspecified","Unspecified","Electric arc furnace steelmaking and casting: Waste water from continous casting machines ","Emissions to air ","Air","Zinc","Zinc","BAT is to minimise the waste water discharge from continuous casting by using the following techniques in combination: (i) the removal of solids by flocculation, sedimentation and/or filtration; (ii) the removal of oil in skimming tanks or any other effective device; (iii) the recirculation of cooling water and water from vacuum generation as much as possible","mg/Nm3","N/A",2,"Green","Discontinuous ",0,0,"Unspecified ","Qualified random sample or a 24 hour composite",0,"IS (2012)\n2012/135/EU",1.7,97,35]
[1241,"Iron and steel","2. Production and processing of metals","1.3. Coke production","Coke Oven Plants",0,"Unspecified","Unspecified","Unspecified","Unspecified","Blast Furnaces: Pretreated waste water from the coking process and coke oven gas (COG)","Emissions to water","Water","Biological Oxygen Demand for 5 days (BOD5)","Ammonia (ecological receptor - Sensitive Lichens)","BAT for pretreated waste water from the coking process and coke oven gas (COG) cleaning is to use biological waste water treatment with integrated denitrification/nitrification stages.","mg/l","N/A",20,"Green","Discontinuous ",0,0,"Unspecified ",0,0,"IS (2012)\n2012/135/EU",1.4,89,27]
[1240,"Iron and steel","2. Production and processing of metals","1.3. Coke production","Coke Oven Plants",0,"Unspecified","Unspecified","Unspecified","Unspecified","Blast Furnaces: Pretreated waste water from the coking process and coke oven gas (COG)","Emissions to water","Water","Chemical oxygen demand (COD)","Ammonia (ecological receptor - Sensitive Lichens)","BAT for pretreated waste water from the coking process and coke oven gas (COG) cleaning is to use biological waste water treatment with integrated denitrification/nitrification stages.","mg/l","N/A",220,"Green","Discontinuous ",0,0,"Unspecified ",0,0,"IS (2012)\n2012/135/EU",1.4,89,27]
[1221,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.","Pelletisation plans",0,"Unspecified","Unspecified","Unspecified","Unspecified",0,"Emissions to water","Water","Chemical oxygen demand (COD)","Ammonia (ecological receptor - Sensitive Lichens)","BAT for pelletisation plants is to treat the effluent water prior to discharge by using a combination of the following techniques: (i) neutralisation; (ii) flocculation; (iii) sedimentation; (iv) sand filtration; (v) Heavy metal precipitation ","mg/l","N/A",160,"Green","Discontinuous ",0,0,"Unspecified ","Random sample of 24 hour composite sample ",0,"IS (2012)\n2012/135/EU",1.3,84,22]
[1213,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.","Sinter Plant",0,"Unspecified","Unspecified","Unspecified","Unspecified","Sinter strand","Emissions to water","Water","Chemical oxygen demand (COD)","Ammonia (ecological receptor - Sensitive Lichens)","BAT is to treat the effluent water from sinter plants where rinsing water is used or where a wet waste gas treatment system is applied, with the exception of cooling water prior to discharge by using a combination of the following techniques: (i) Heavy metal precipitation; (ii) neutralisation; (iii) sand filtration","mg/l","N/A",100,"Green","Discontinuous ",0,0,"Unspecified ","Random sample of 24 hour composite sample ","Sum of arsenic (As), cadmium (Cd), chromium (Cr), copper (Cu), mercury (Hg), nickel (Ni), lead (Pb), and zinc (Zn)","IS (2012)\n2012/135/EU",1.2,81,19]
[1244,"Iron and steel","2. Production and processing of metals","1.3. Coke production","Coke Oven Plants",0,"Unspecified","Unspecified","Unspecified","Unspecified","Blast Furnaces: Pretreated waste water from the coking process and coke oven gas (COG)","Emissions to water","Water","Cyanide (CN), easily released","Ammonia (ecological receptor - Sensitive Lichens)","BAT for pretreated waste water from the coking process and coke oven gas (COG) cleaning is to use biological waste water treatment with integrated denitrification/nitrification stages.","mg/l","N/A",0.1,"Green","Discontinuous ",0,0,"Unspecified ","Random sample or a 24 hour composite sample ",0,"IS (2012)\n2012/135/EU",1.4,89,27]
[1258,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.",0,0,"Unspecified","Unspecified","Unspecified","Unspecified","Blast Furnaces: Blast furnace gas ","Emissions to water","Water","Cyanide (CN), easily released","Ammonia (ecological receptor - Sensitive Lichens)","BAT for treating waste water from blast furnace gas treatment is to use flocculation (coagulation) and sedimentation and the reduction of easily released cyanide, if necessary.","mg/l","N/A",0.4,"Green","Discontinuous ",0,0,"Unspecified ","Random sample or a 24 hour composite sample ",0,"IS (2012)\n2012/135/EU",1.5,91,29]
[1224,"Iron and steel","2. Production and processing of metals","1.3. Coke production","Coke Oven Plants",0,"Unspecified","Unspecified","Unspecified","Unspecified","Coal grinding plants ","Emissions to air","Air","Dust","Particulates (PM10) (24 hr Mean)","BAT for coal grinding plants (coal preparation including crushing, grinding, pulverising and screening) is to prevent or reduce dust emissions by using one or a combination of the following techniques: (i) building and/or device enclosure (crusher, pulveriser, sieves); (ii) efficient extraction and use of a subsequent dry dedusting systems.","mg/Nm3",10,20,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0,"IS (2012)\n2012/135/EU",1.4,85,23]
[1214,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.","Sinter Plant",0,"Unspecified","Unspecified","Unspecified","Unspecified","Sinter strand","Emissions to water","Water","Heavy metals (sum of arsenic (As), cadmium (Cd), chromium (Cr), copper (Cu), mercury (Hg), nickel (Ni), lead (Pb), zinc (Zn))","Ammonia (ecological receptor - Sensitive Lichens)","BAT is to treat the effluent water from sinter plants where rinsing water is used or where a wet waste gas treatment system is applied, with the exception of cooling water prior to discharge by using a combination of the following techniques: (i) Heavy metal precipitation; (ii) neutralisation; (iii) sand filtration","mg/l","N/A",0.1,"Green","Discontinuous ",0,0,"Unspecified ","Random sample of 24 hour composite sample ","Sum of arsenic (As), cadmium (Cd), chromium (Cr), copper (Cu), mercury (Hg), nickel (Ni), lead (Pb), and zinc (Zn)","IS (2012)\n2012/135/EU",1.2,81,19]
[1223,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.","Pelletisation plans",0,"Unspecified","Unspecified","Unspecified","Unspecified",0,"Emissions to water","Water","Heavy metals (sum of arsenic (As), cadmium (Cd), chromium (Cr), copper (Cu), mercury (Hg), nickel (Ni), lead (Pb), zinc (Zn))","Ammonia (ecological receptor - Sensitive Lichens)","BAT for pelletisation plants is to treat the effluent water prior to discharge by using a combination of the following techniques: (i) neutralisation; (ii) flocculation; (iii) sedimentation; (iv) sand filtration; (v) Heavy metal precipitation ","mg/l","N/A",0.55000000000000004,"Green","Discontinuous ",0,0,"Unspecified ","Random sample of 24 hour composite sample ",0,"IS (2012)\n2012/135/EU",1.3,84,22]
[1255,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.",0,0,"Unspecified","Unspecified","Unspecified","Unspecified","Blast Furnaces: Blast furnace gas ","Emissions to water","Water","Iron","Ammonia (ecological receptor - Sensitive Lichens)","BAT for treating waste water from blast furnace gas treatment is to use flocculation (coagulation) and sedimentation and the reduction of easily released cyanide, if necessary.","mg/l","N/A",5,"Green","Discontinuous ",0,0,"Unspecified ","Random sample or a 24 hour composite sample ",0,"IS (2012)\n2012/135/EU",1.5,91,29]
[1222,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.","Pelletisation plans",0,"Unspecified","Unspecified","Unspecified","Unspecified",0,"Emissions to water","Water","Kjeldahl nitrogen","Ammonia (ecological receptor - Sensitive Lichens)","BAT for pelletisation plants is to treat the effluent water prior to discharge by using a combination of the following techniques: (i) neutralisation; (ii) flocculation; (iii) sedimentation; (iv) sand filtration; (v) Heavy metal precipitation ","mg/l","N/A",45,"Green","Discontinuous ",0,0,"Unspecified ","Random sample of 24 hour composite sample ",0,"IS (2012)\n2012/135/EU",1.3,84,22]
[1256,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.",0,0,"Unspecified","Unspecified","Unspecified","Unspecified","Blast Furnaces: Blast furnace gas ","Emissions to water","Water","Lead","Ammonia (ecological receptor - Sensitive Lichens)","BAT for treating waste water from blast furnace gas treatment is to use flocculation (coagulation) and sedimentation and the reduction of easily released cyanide, if necessary.","mg/l","N/A",0.5,"Green","Discontinuous ",0,0,"Unspecified ","Random sample or a 24 hour composite sample ",0,"IS (2012)\n2012/135/EU",1.5,91,29]
[1246,"Iron and steel","2. Production and processing of metals","1.3. Coke production","Coke Oven Plants",0,"Unspecified","Unspecified","Unspecified","Unspecified","Blast Furnaces: Pretreated waste water from the coking process and coke oven gas (COG)","Emissions to water","Water","Phenols","Ammonia (ecological receptor - Sensitive Lichens)","BAT for pretreated waste water from the coking process and coke oven gas (COG) cleaning is to use biological waste water treatment with integrated denitrification/nitrification stages.","mg/l","N/A",0.5,"Green","Discontinuous ",0,0,"Unspecified ","Random sample or a 24 hour composite sample ",0,"IS (2012)\n2012/135/EU",1.4,89,27]
[1245,"Iron and steel","2. Production and processing of metals","1.3. Coke production","Coke Oven Plants",0,"Unspecified","Unspecified","Unspecified","Unspecified","Blast Furnaces: Pretreated waste water from the coking process and coke oven gas (COG)","Emissions to water","Water","Polycyclic aromatic hydrocarbons (PAH)\n\n(sum of Fluoranthene, Benzo[b]fluoranthene,\nBenzo[k]fluoranthene, Benzo[a]pyrene,\nIndeno[1,2,3-cd]pyrene and Benzo[g,h,i]perylene","Ammonia (ecological receptor - Sensitive Lichens)","BAT for pretreated waste water from the coking process and coke oven gas (COG) cleaning is to use biological waste water treatment with integrated denitrification/nitrification stages.","mg/l","N/A",0.05,"Green","Discontinuous ",0,0,"Unspecified ","Random sample or a 24 hour composite sample ",0,"IS (2012)\n2012/135/EU",1.4,89,27]
[1242,"Iron and steel","2. Production and processing of metals","1.3. Coke production","Coke Oven Plants",0,"Unspecified","Unspecified","Unspecified","Unspecified","Blast Furnaces: Pretreated waste water from the coking process and coke oven gas (COG)","Emissions to water","Water","Sulphides, easily released","Ammonia (ecological receptor - Sensitive Lichens)","BAT for pretreated waste water from the coking process and coke oven gas (COG) cleaning is to use biological waste water treatment with integrated denitrification/nitrification stages.","mg/l","N/A",0.1,"Green","Discontinuous ",0,0,"Unspecified ",0,0,"IS (2012)\n2012/135/EU",1.4,89,27]
[1247,"Iron and steel","2. Production and processing of metals","1.3. Coke production","Coke Oven Plants",0,"Unspecified","Unspecified","Unspecified","Unspecified","Blast Furnaces: Pretreated waste water from the coking process and coke oven gas (COG)","Emissions to water","Water","sum of ammonia-nitrogen (NH4 +-N), nitrate-nitrogen (NO3 - -N) and nitrite-nitrogen (NO2 - -N)","Ammonia (ecological receptor - Sensitive Lichens)","BAT for pretreated waste water from the coking process and coke oven gas (COG) cleaning is to use biological waste water treatment with integrated denitrification/nitrification stages.","mg/l",15,50,"Green","Discontinuous ",0,0,"Unspecified ","Random sample or a 24 hour composite sample ","Regarding the sum of ammonia-nitrogen (NH4 +-N), nitrate-nitrogen (NO3 - -N) and nitrite-nitrogen (NO2 - -N), values of < 35 mg/l are usually associated with the application of advanced biological waste water treatment plants with predenitrification/nitrification and post-denitrification.","IS (2012)\n2012/135/EU",1.4,89,27]
[1254,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.",0,0,"Unspecified","Unspecified","Unspecified","Unspecified","Blast Furnaces: Blast furnace gas ","Emissions to water","Water","Total Suspended Solids (TSS) ","Ammonia (ecological receptor - Sensitive Lichens)","BAT for treating waste water from blast furnace gas treatment is to use flocculation (coagulation) and sedimentation and the reduction of easily released cyanide, if necessary.","mg/l","N/A",30,"Green","Discontinuous ",0,0,"Unspecified ","Random sample or a 24 hour composite sample ",0,"IS (2012)\n2012/135/EU",1.5,91,29]
[1220,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.","Pelletisation plans",0,"Unspecified","Unspecified","Unspecified","Unspecified",0,"Emissions to water","Water","Total Suspended Solids (TSS) ","Ammonia (ecological receptor - Sensitive Lichens)","BAT for pelletisation plants is to treat the effluent water prior to discharge by using a combination of the following techniques: (i) neutralisation; (ii) flocculation; (iii) sedimentation; (iv) sand filtration; (v) Heavy metal precipitation ","mg/l","N/A",50,"Green","Discontinuous ",0,0,"Unspecified ","Random sample of 24 hour composite sample ",0,"IS (2012)\n2012/135/EU",1.3,84,22]
[1212,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.","Sinter Plant",0,"Unspecified","Unspecified","Unspecified","Unspecified","Sinter strand","Emissions to water","Water","Total Suspended Solids (TSS) ","Ammonia (ecological receptor - Sensitive Lichens)","BAT is to treat the effluent water from sinter plants where rinsing water is used or where a wet waste gas treatment system is applied, with the exception of cooling water prior to discharge by using a combination of the following techniques: (i) Heavy metal precipitation; (ii) neutralisation; (iii) sand filtration","mg/l","N/A",30,"Green","Discontinuous ","Unspecified ","Unspecified ","Unspecified ","Random sample of 24 hour composite sample ","Sum of arsenic (As), cadmium (Cd), chromium (Cr), copper (Cu), mercury (Hg), nickel (Ni), lead (Pb), and zinc (Zn)","IS (2012)\n2012/135/EU",1.2,81,19]
[1243,"Iron and steel","2. Production and processing of metals","1.3. Coke production","Coke Oven Plants",0,"Unspecified","Unspecified","Unspecified","Unspecified","Blast Furnaces: Pretreated waste water from the coking process and coke oven gas (COG)","Emissions to water","Water","Thiocyanate (SCN-)","Ammonia (ecological receptor - Sensitive Lichens)","BAT for pretreated waste water from the coking process and coke oven gas (COG) cleaning is to use biological waste water treatment with integrated denitrification/nitrification stages.","mg/l","N/A",4,"Green","Discontinuous ",0,0,"Unspecified ","Random sample or a 24 hour composite sample ",0,"IS (2012)\n2012/135/EU",1.4,89,27]
[1257,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.",0,0,"Unspecified","Unspecified","Unspecified","Unspecified","Blast Furnaces: Blast furnace gas ","Emissions to water","Water","Zinc","Ammonia (ecological receptor - Sensitive Lichens)","BAT for treating waste water from blast furnace gas treatment is to use flocculation (coagulation) and sedimentation and the reduction of easily released cyanide, if necessary.","mg/l","N/A",2,"Green","Discontinuous ",0,0,"Unspecified ","Random sample or a 24 hour composite sample ",0,"IS (2012)\n2012/135/EU",1.5,91,29]
[854,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Unspecified","Unspecified ","Co-incineration of waste with coal and/or lignite","< 300 MWth ",0,"Emissions to air ","Air","Cd + Tl","Cadmium and its compounds (as Cd)","In order to reduce dust and particulate-bound metal emissions to air from the co-incineration of waste with coal and/or lignite, BAT is to use one or a combination of the techniques given in BAT 22.","ug/Nm3",5,"12","Green","Once every 6 months",0,0,0.06,"Average over the sampling period",0,"LCP (2017)\n2017/1696","6.1.5",72,72]
[856,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Unspecified","Unspecified ","Co-incineration of waste with coal and/or lignite","≥ 300 MWth",0,"Emissions to air ","Air","Cd + Tl","Cadmium and its compounds (as Cd)","In order to reduce dust and particulate-bound metal emissions to air from the co-incineration of waste with coal and/or lignite, BAT is to use one or a combination of the techniques given in BAT 22.","ug/Nm3",5,"6","Green","Once every 3 months ",0,0,0.06,"Average of samples obtained during one year",0,"LCP (2017)\n2017/1698","6.1.5",72,72]
[858,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Unspecified","Unspecified ","Co-incineration of waste with biomass and/or peat","Unspecified ",0,"Emissions to air ","Air","Cd + Tl","Cadmium and its compounds (as Cd)","In order to reduce dust and particulate-bound metal emissions to air from the co-incineration of waste with biomass and/or peat, BAT is to use one or a combination of the techniques given in BAT 26.","ug/Nm3","N/A","5","Amber",0,0,0,0.06,"Average of samples obtained during one year",0,"LCP (2017)\n2017/1700","6.1.5",72,72]
[631,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","Plants operated ≥ 1 500 h/yr or for new combustion plants","Coal and/or lignite ","≥ 300 MWth",0,"Emissions to air ","Air","Carbon monoxide, expressed as CO","Carbon monoxide",0,"mg/Nm3",30,"140","Amber","Continuous ",0,0,0.06,"Yearly ",0,"LCP (2017)\n2017/1473","2.1.3",31,31]
[633,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Coal-fired PC boiler","Plants operated ≥ 1 500 h/yr or for new combustion plants","Coal and/or lignite ","≥ 300 MWth",0,"Emissions to air ","Air","Carbon monoxide, expressed as CO","Carbon monoxide",0,"mg/Nm3",5,"100","Amber","Continuous ",0,0,0.06,"Yearly ","The higher end of the range may be up to 140 mg/Nm3 in the case of limitations due to boiler design, and/or in the case of fluidised bed boilers not fitted with secondary abatement techniques for NOX emissions reduction.","LCP (2017)\n2017/1475","2.1.3",31,31]
[632,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"FBC boiler combusting coal and/or lignite and lignite-fired PC boiler","Plants operated ≥ 1 500 h/yr or for new combustion plants","Coal and/or lignite ","≥ 300 MWth",0,"Emissions to air ","Air","Carbon monoxide, expressed as CO","Carbon monoxide",0,"mg/Nm3",30,"100","Amber","Continuous ",0,0,0.06,"Yearly ","The higher end of the range may be up to 140 mg/Nm3 in the case of limitations due to boiler design, and/or in the case of fluidised bed boilers not fitted with secondary abatement techniques for NOX emissions reduction.","LCP (2017)\n2017/1474","2.1.3",31,31]
[659,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","Existing","Coal and/or lignite ","<100 MWth",0,"Emissions to air ","Air","Dust","Particulates (PM10) (Annual Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below.; (ii) Bag filter; (iii) Boiler sorbent injection (in-furnace or in- bed); (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",2,18,"Green","Continuous ",0,0,0.06,"Yearly","These BAT-AELs do not apply to plants operated < 1 500 h/yr.","LCP (2017)\n2017/1501","2.1.5",34,34]
[661,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","Existing","Coal and/or lignite ","<100 MWth",0,"Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below.; (ii) Bag filter; (iii) Boiler sorbent injection (in-furnace or in- bed); (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",4,22,"Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ","For plants operated < 500 h/yr, these levels are indicative.\n\nThe higher end of the BAT-AEL range is 28 mg/Nm3 for plants put into operation no later than 7 January 2014.","LCP (2017)\n2017/1503","2.1.5",34,34]
[671,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","Existing","Coal and/or lignite ","≥ 1 000 MWth",0,"Emissions to air ","Air","Dust","Particulates (PM10) (Annual Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below.; (ii) Bag filter; (iii) Boiler sorbent injection (in-furnace or in- bed); (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",2,8,"Green","Continuous ",0,0,0.06,"Yearly",0,"LCP (2017)\n2017/1513","2.1.5",34,34]
[673,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","Existing","Coal and/or lignite ","≥ 1 000 MWth",0,"Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below.; (ii) Bag filter; (iii) Boiler sorbent injection (in-furnace or in- bed); (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",3,11,"Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ","The higher end of the BAT-AEL range is 14 mg/Nm3 for plants put into operation no later than 7 January 2014.","LCP (2017)\n2017/1515","2.1.5",34,34]
[663,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","Existing","Coal and/or lignite ","100-300 MWth",0,"Emissions to air ","Air","Dust","Particulates (PM10) (Annual Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below.; (ii) Bag filter; (iii) Boiler sorbent injection (in-furnace or in- bed); (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",2,14,"Green","Continuous ",0,0,0.06,"Yearly",0,"LCP (2017)\n2017/1505","2.1.5",34,34]
[665,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","Existing","Coal and/or lignite ","100-300 MWth",0,"Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below.; (ii) Bag filter; (iii) Boiler sorbent injection (in-furnace or in- bed); (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",4,22,"Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ","The higher end of the BAT-AEL range is 25 mg/Nm3 for plants put into operation no later than 7 January 2014.","LCP (2017)\n2017/1507","2.1.5",34,34]
[667,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","Existing","Coal and/or lignite ","300-1000 MWth",0,"Emissions to air ","Air","Dust","Particulates (PM10) (Annual Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below.; (ii) Bag filter; (iii) Boiler sorbent injection (in-furnace or in- bed); (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",2,10,"Green","Continuous ",0,0,0.06,"Yearly","The higher end of the BAT-AEL range is 12 mg/Nm3 for plants put into operation no later than 7 January 2014.","LCP (2017)\n2017/1509","2.1.5",34,34]
[669,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","Existing","Coal and/or lignite ","300-1000 MWth",0,"Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below.; (ii) Bag filter; (iii) Boiler sorbent injection (in-furnace or in- bed); (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",3,11,"Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ","The higher end of the BAT-AEL range is 20 mg/Nm3 for plants put into operation no later than 7 January 2014.","LCP (2017)\n2017/1511","2.1.5",34,34]
[725,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","Existing","Solid biomass and/or peat","< 100 MWth",0,"Emissions to air ","Air","Dust","Particulates (PM10) (Annual Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Dry or semi-dry FGD system; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Fuel choice","mg/Nm3",2,"15","Green","Continuous ",0,0,0.06,"Yearly","These BAT-AELs do not apply to plants operated < 1 500 h/yr.","LCP (2017)\n2017/1567","2.2.4",40,40]
[727,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","Existing","Solid biomass and/or peat","< 100 MWth",0,"Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Dry or semi-dry FGD system; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Fuel choice","mg/Nm3",2,"22","Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ","For plants operated < 500 h/yr, these levels are indicative.","LCP (2017)\n2017/1569","2.2.4",40,40]
[733,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","Existing","Solid biomass and/or peat","≥ 300 MWth",0,"Emissions to air ","Air","Dust","Particulates (PM10) (Annual Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Dry or semi-dry FGD system; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Fuel choice","mg/Nm3",2,"10","Green","Continuous ",0,0,0.06,"Yearly","These BAT-AELs do not apply to plants operated < 1 500 h/yr.","LCP (2017)\n2017/1575","2.2.4",40,40]
[735,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","Existing","Solid biomass and/or peat","≥ 300 MWth",0,"Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Dry or semi-dry FGD system; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Fuel choice","mg/Nm3",2,"16","Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ","For plants operated < 500 h/yr, these levels are indicative.","LCP (2017)\n2017/1577","2.2.4",40,40]
[729,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","Existing","Solid biomass and/or peat","100-300 MWth",0,"Emissions to air ","Air","Dust","Particulates (PM10) (Annual Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Dry or semi-dry FGD system; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Fuel choice","mg/Nm3",2,"12","Green","Continuous ",0,0,0.06,"Yearly","These BAT-AELs do not apply to plants operated < 1 500 h/yr.","LCP (2017)\n2017/1571","2.2.4",40,40]
[731,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","Existing","Solid biomass and/or peat","100-300 MWth",0,"Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Dry or semi-dry FGD system; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Fuel choice","mg/Nm3",2,"18","Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ","For plants operated < 500 h/yr, these levels are indicative.","LCP (2017)\n2017/1573","2.2.4",40,40]
[658,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","New","Coal and/or lignite ","<100 MWth",0,"Emissions to air ","Air","Dust","Particulates (PM10) (Annual Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below.; (ii) Bag filter; (iii) Boiler sorbent injection (in-furnace or in- bed); (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",2,5,"Green","Continuous ",0,0,0.06,"Yearly",0,"LCP (2017)\n2017/1500","2.1.5",34,34]
[660,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","New","Coal and/or lignite ","<100 MWth",0,"Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below.; (ii) Bag filter; (iii) Boiler sorbent injection (in-furnace or in- bed); (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",4,16,"Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ",0,"LCP (2017)\n2017/1502","2.1.5",34,34]
[670,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","New","Coal and/or lignite ","≥ 1 000 MWth",0,"Emissions to air ","Air","Dust","Particulates (PM10) (Annual Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below.; (ii) Bag filter; (iii) Boiler sorbent injection (in-furnace or in- bed); (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",2,5,"Green","Continuous ",0,0,0.06,"Yearly",0,"LCP (2017)\n2017/1512","2.1.5",34,34]
[672,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","New","Coal and/or lignite ","≥ 1 000 MWth",0,"Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below.; (ii) Bag filter; (iii) Boiler sorbent injection (in-furnace or in- bed); (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",3,10,"Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ",0,"LCP (2017)\n2017/1514","2.1.5",34,34]
[662,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","New","Coal and/or lignite ","100-300 MWth",0,"Emissions to air ","Air","Dust","Particulates (PM10) (Annual Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below.; (ii) Bag filter; (iii) Boiler sorbent injection (in-furnace or in- bed); (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",2,5,"Green","Continuous ",0,0,0.06,"Yearly",0,"LCP (2017)\n2017/1504","2.1.5",34,34]
[664,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","New","Coal and/or lignite ","100-300 MWth",0,"Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below.; (ii) Bag filter; (iii) Boiler sorbent injection (in-furnace or in- bed); (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",3,15,"Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ",0,"LCP (2017)\n2017/1506","2.1.5",34,34]
[666,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","New","Coal and/or lignite ","300-1000 MWth",0,"Emissions to air ","Air","Dust","Particulates (PM10) (Annual Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below.; (ii) Bag filter; (iii) Boiler sorbent injection (in-furnace or in- bed); (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",2,5,"Green","Continuous ",0,0,0.06,"Yearly",0,"LCP (2017)\n2017/1508","2.1.5",34,34]
[668,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","New","Coal and/or lignite ","300-1000 MWth",0,"Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below.; (ii) Bag filter; (iii) Boiler sorbent injection (in-furnace or in- bed); (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",3,10,"Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ",0,"LCP (2017)\n2017/1510","2.1.5",34,34]
[724,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","New","Solid biomass and/or peat","< 100 MWth",0,"Emissions to air ","Air","Dust","Particulates (PM10) (Annual Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Dry or semi-dry FGD system; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Fuel choice","mg/Nm3",2,"5","Green","Continuous ",0,0,0.06,"Yearly ",0,"LCP (2017)\n2017/1566","2.2.4",40,40]
[726,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","New","Solid biomass and/or peat","< 100 MWth",0,"Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Dry or semi-dry FGD system; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Fuel choice","mg/Nm3",2,"10","Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ",0,"LCP (2017)\n2017/1568","2.2.4",40,40]
[732,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","New","Solid biomass and/or peat","≥ 300 MWth",0,"Emissions to air ","Air","Dust","Particulates (PM10) (Annual Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Dry or semi-dry FGD system; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Fuel choice","mg/Nm3",2,"5","Green","Continuous ",0,0,0.06,"Yearly ",0,"LCP (2017)\n2017/1574","2.2.4",40,40]
[734,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","New","Solid biomass and/or peat","≥ 300 MWth",0,"Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Dry or semi-dry FGD system; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Fuel choice","mg/Nm3",2,"10","Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ",0,"LCP (2017)\n2017/1576","2.2.4",40,40]
[728,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","New","Solid biomass and/or peat","100-300 MWth",0,"Emissions to air ","Air","Dust","Particulates (PM10) (Annual Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Dry or semi-dry FGD system; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Fuel choice","mg/Nm3",2,"5","Green","Continuous ",0,0,0.06,"Yearly ",0,"LCP (2017)\n2017/1570","2.2.4",40,40]
[730,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","New","Solid biomass and/or peat","100-300 MWth",0,"Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Dry or semi-dry FGD system; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Fuel choice","mg/Nm3",2,"10","Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ",0,"LCP (2017)\n2017/1572","2.2.4",40,40]
[819,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Boilers","Unspecified","100% iron and steel process gases ","Unspecified ",0,"Emissions to air ","Air","Dust","Particulates (PM10) (Annual Mean)","In order to reduce dust emissions to air from the combustion of iron and steel process gases, BAT is to use one or a combination of the techniques given below: (i) Fuel choice/management; (ii) Blast furnace gas pretreatment at the iron- and steel-works; (iii) Basic oxygen furnace gas pretreatment at the iron- and steel- works; (iv) Electrostatic precipitator (ESP); (v) Bag filter","mg/Nm3",2,"7","Green","Continuous ",0,0,0.03,"Yearly","For existing plants operated < 1 500 h/yr, these BAT-AELs do not apply.","LCP (2017)\n2017/1661","4.2.4",61,61]
[820,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Boilers","Unspecified","100% iron and steel process gases ","Unspecified ",0,"Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","In order to reduce dust emissions to air from the combustion of iron and steel process gases, BAT is to use one or a combination of the techniques given below: (i) Fuel choice/management; (ii) Blast furnace gas pretreatment at the iron- and steel-works; (iii) Basic oxygen furnace gas pretreatment at the iron- and steel- works; (iv) Electrostatic precipitator (ESP); (v) Bag filter","mg/Nm3",2,"10","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ","For existing plants operated < 500 h/yr, these levels are indicative","LCP (2017)\n2017/1662","4.2.4",61,61]
[844,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Boilers","Existing","100 % process fuels from the chemical industry in boilers","< 300 MWth ",0,"Emissions to air ","Air","Dust","Particulates (PM10) (Annual Mean)","In order to reduce emissions to air of dust, particulate-bound metals, and trace species from the combustion of process fuels from the chemical industry in boilers, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Fuel choice; (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",2,"15","Green","Continuous ",0,0,0.03,"Yearly","For plants operated < 1 500 h/yr, these BAT-AELs do not apply.","LCP (2017)\n2017/1686","5.1.5",69,69]
[846,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Boilers","Existing","100 % process fuels from the chemical industry in boilers","< 300 MWth ",0,"Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","In order to reduce emissions to air of dust, particulate-bound metals, and trace species from the combustion of process fuels from the chemical industry in boilers, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Fuel choice; (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",2,"22","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ","For plants operated < 500 h/yr, these levels are indicative.\n\nFor plants operated < 500 h/yr, these levels are indicative.","LCP (2017)\n2017/1688","5.1.5",69,69]
[848,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Boilers","Existing","100 % process fuels from the chemical industry in boilers","≥ 300 MWth",0,"Emissions to air ","Air","Dust","Particulates (PM10) (Annual Mean)","In order to reduce emissions to air of dust, particulate-bound metals, and trace species from the combustion of process fuels from the chemical industry in boilers, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Fuel choice; (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",2,"10","Green","Continuous ",0,0,0.03,"Yearly","For plants operated < 1 500 h/yr, these BAT-AELs do not apply.\n\nFor plants put into operation no later than 7 January 2014, the higher end of the BAT-AEL range is 15 mg/Nm3.","LCP (2017)\n2017/1690","5.1.5",69,69]
[850,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Boilers","Existing","100 % process fuels from the chemical industry in boilers","≥ 300 MWth",0,"Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","In order to reduce emissions to air of dust, particulate-bound metals, and trace species from the combustion of process fuels from the chemical industry in boilers, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Fuel choice; (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",2,"11","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ","For plants operated < 500 h/yr, these levels are indicative.\n\nFor plants put into operation no later than 7 January 2014, the higher end of the BAT-AEL range is 25 mg/Nm3.","LCP (2017)\n2017/1692","5.1.5",69,69]
[754,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Boilers","Existing","HFO and/or gas oil in boilers","< 300 MWth ",0,"Emissions to air ","Air","Dust","Particulates (PM10) (Annual Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Multicyclones; (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD); (vi) Fuel choice","mg/Nm3",2,"20","Green","Continuous ",0,0,0.03,"Yearly","These BAT-AELs do not apply to plants operated < 1 500 h/yr.","LCP (2017)\n2017/1596","3.1.4",45,45]
[756,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Boilers","Existing","HFO and/or gas oil in boilers","< 300 MWth ",0,"Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Multicyclones; (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD); (vi) Fuel choice","mg/Nm3",7,"22","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ","For plants operated < 500 h/yr, these levels are indicative.\n\nThe higher end of the BAT-AEL range is 25 mg/Nm3 for plants put into operation no later than 7 January 2014.","LCP (2017)\n2017/1598","3.1.4",45,45]
[758,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Boilers","Existing","HFO and/or gas oil in boilers","≥ 300 MWth",0,"Emissions to air ","Air","Dust","Particulates (PM10) (Annual Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Multicyclones; (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD); (vi) Fuel choice","mg/Nm3",2,"10","Green","Continuous ",0,0,0.03,"Yearly","These BAT-AELs do not apply to plants operated < 1 500 h/yr.","LCP (2017)\n2017/1600","3.1.4",45,45]
[760,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Boilers","Existing","HFO and/or gas oil in boilers","≥ 300 MWth",0,"Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Multicyclones; (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD); (vi) Fuel choice","mg/Nm3",7,"11","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ","For plants operated < 500 h/yr, these levels are indicative.\n\nThe higher end of the BAT-AEL range is 15 mg/Nm3 for plants put into operation no later than 7 January 2014.","LCP (2017)\n2017/1602","3.1.4",45,45]
[843,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Boilers","New","100 % process fuels from the chemical industry in boilers","< 300 MWth ",0,"Emissions to air ","Air","Dust","Particulates (PM10) (Annual Mean)","In order to reduce emissions to air of dust, particulate-bound metals, and trace species from the combustion of process fuels from the chemical industry in boilers, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Fuel choice; (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",2,"5","Green","Continuous ",0,0,0.03,"Yearly",0,"LCP (2017)\n2017/1685","5.1.5",69,69]
[845,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Boilers","New","100 % process fuels from the chemical industry in boilers","< 300 MWth ",0,"Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","In order to reduce emissions to air of dust, particulate-bound metals, and trace species from the combustion of process fuels from the chemical industry in boilers, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Fuel choice; (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",2,"10","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ",0,"LCP (2017)\n2017/1687","5.1.5",69,69]
[847,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Boilers","New","100 % process fuels from the chemical industry in boilers","≥ 300 MWth",0,"Emissions to air ","Air","Dust","Particulates (PM10) (Annual Mean)","In order to reduce emissions to air of dust, particulate-bound metals, and trace species from the combustion of process fuels from the chemical industry in boilers, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Fuel choice; (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",2,"5","Green","Continuous ",0,0,0.03,"Yearly",0,"LCP (2017)\n2017/1689","5.1.5",69,69]
[849,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Boilers","New","100 % process fuels from the chemical industry in boilers","≥ 300 MWth",0,"Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","In order to reduce emissions to air of dust, particulate-bound metals, and trace species from the combustion of process fuels from the chemical industry in boilers, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Fuel choice; (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",2,"10","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ",0,"LCP (2017)\n2017/1691","5.1.5",69,69]
[753,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Boilers","New","HFO and/or gas oil in boilers","< 300 MWth ",0,"Emissions to air ","Air","Dust","Particulates (PM10) (Annual Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Multicyclones; (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD); (vi) Fuel choice","mg/Nm3",2,"10","Green","Continuous ",0,0,0.03,"Yearly",0,"LCP (2017)\n2017/1595","3.1.4",45,45]
[755,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Boilers","New","HFO and/or gas oil in boilers","< 300 MWth ",0,"Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Multicyclones; (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD); (vi) Fuel choice","mg/Nm3",7,"18","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ",0,"LCP (2017)\n2017/1597","3.1.4",45,45]
[757,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Boilers","New","HFO and/or gas oil in boilers","≥ 300 MWth",0,"Emissions to air ","Air","Dust","Particulates (PM10) (Annual Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Multicyclones; (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD); (vi) Fuel choice","mg/Nm3",2,"5","Green","Continuous ",0,0,0.03,"Yearly",0,"LCP (2017)\n2017/1599","3.1.4",45,45]
[759,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Boilers","New","HFO and/or gas oil in boilers","≥ 300 MWth",0,"Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Multicyclones; (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD); (vi) Fuel choice","mg/Nm3",7,"10","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ",0,"LCP (2017)\n2017/1601","3.1.4",45,45]
[821,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"CCGT","Unspecified","100% iron and steel process gases ","Unspecified ",0,"Emissions to air ","Air","Dust","Particulates (PM10) (Annual Mean)","In order to reduce dust emissions to air from the combustion of iron and steel process gases, BAT is to use one or a combination of the techniques given below: (i) Fuel choice/management; (ii) Blast furnace gas pretreatment at the iron- and steel-works; (iii) Basic oxygen furnace gas pretreatment at the iron- and steel- works; (iv) Electrostatic precipitator (ESP); (v) Bag filter","mg/Nm3",2,"5","Amber","Continuous ",0,0,0,"Yearly","For existing plants operated < 1 500 h/yr, these BAT-AELs do not apply.","LCP (2017)\n2017/1663","4.2.4",62,62]
[822,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"CCGT","Unspecified","100% iron and steel process gases ","Unspecified ",0,"Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","In order to reduce dust emissions to air from the combustion of iron and steel process gases, BAT is to use one or a combination of the techniques given below: (i) Fuel choice/management; (ii) Blast furnace gas pretreatment at the iron- and steel-works; (iii) Basic oxygen furnace gas pretreatment at the iron- and steel- works; (iv) Electrostatic precipitator (ESP); (v) Bag filter","mg/Nm3",2,"5","Amber","Continuous ",0,0,0,"Daily average or average over the sampling period ","For existing plants operated < 500 h/yr, these levels are indicative","LCP (2017)\n2017/1664","4.2.4",62,62]
[770,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Fired engines ","Existing","HFO and/or gas oil in reciprocating engines","≥ 50 MWth",0,"Emissions to air ","Air","Dust","Particulates (PM10) (Annual Mean)","In order to prevent or reduce dust and particulate-bound metal emissions from the combustion of HFO and/or gas oil in reciprocating engines, BAT is to use one or a combination of the techniques given below: (i) Fuel choice; (ii) Electrostatic precipitator (ESP); (iii) Bag filter ","mg/Nm3",5,"35","Green","Continuous ",0,0,0.15,"Yearly","These BAT-AELs do not apply to plants operated < 1 500 h/yr.","LCP (2017)\n2017/1612","3.2.4",48,48]
[772,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Fired engines ","Existing","HFO and/or gas oil in reciprocating engines","≥ 50 MWth",0,"Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","In order to prevent or reduce dust and particulate-bound metal emissions from the combustion of HFO and/or gas oil in reciprocating engines, BAT is to use one or a combination of the techniques given below: (i) Fuel choice; (ii) Electrostatic precipitator (ESP); (iii) Bag filter ","mg/Nm3",10,"45","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period ","For plants operated < 500 h/yr, these levels are indicative.","LCP (2017)\n2017/1614","3.2.4",48,48]
[769,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Fired engines ","New","HFO and/or gas oil in reciprocating engines","≥ 50 MWth",0,"Emissions to air ","Air","Dust","Particulates (PM10) (Annual Mean)","In order to prevent or reduce dust and particulate-bound metal emissions from the combustion of HFO and/or gas oil in reciprocating engines, BAT is to use one or a combination of the techniques given below: (i) Fuel choice; (ii) Electrostatic precipitator (ESP); (iii) Bag filter ","mg/Nm3",5,"10","Green","Continuous ",0,0,0.15,"Yearly",0,"LCP (2017)\n2017/1611","3.2.4",48,48]
[771,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Fired engines ","New","HFO and/or gas oil in reciprocating engines","≥ 50 MWth",0,"Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","In order to prevent or reduce dust and particulate-bound metal emissions from the combustion of HFO and/or gas oil in reciprocating engines, BAT is to use one or a combination of the techniques given below: (i) Fuel choice; (ii) Electrostatic precipitator (ESP); (iii) Bag filter ","mg/Nm3",10,"20","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period ",0,"LCP (2017)\n2017/1613","3.2.4",48,48]
[867,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"IGCC","Unspecified ","Unspecified","≥ 100 MWth",0,"Emissions to air ","Air","Dust and particulate-bound metal emissions","Particulates (PM10) (24 hr Mean)",0,"mg/Nm3","N/A","0.025","Green","Continuous",0,0,0.15,"Average over the sampling period",0,"LCP (2017)\n2017/1709","7.1.4",76,76]
[868,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"IGCC","Unspecified ","Unspecified","≥ 100 MWth",0,"Emissions to air ","Air","Dust and particulate-bound metal emissions","Particulates (PM10) (24 hr Mean)",0,"ug/Nm3","N/A","1","Green","Continuous",0,0,0.15,"Average over the sampling period",0,"LCP (2017)\n2017/1710","7.1.4",76,76]
[869,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"IGCC","Unspecified ","Unspecified","≥ 100 MWth",0,"Emissions to air ","Air","Dust and particulate-bound metal emissions","Particulates (PM10) (Annual Mean)",0,"mg/Nm3","N/A","2.5","Green","Continuous",0,0,0.15,"Yearly average",0,"LCP (2017)\n2017/1711","7.1.4",76,76]
[804,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Spark-ignited lean-burn gas engine","Unspecified","Natural gas ","≥ 50 MWth",0,"Emissions to air ","Air","Formaldehyde and CH4","Formaldehyde and CH4",0,"mg/Nm3",5,"15","Green","Once every year",0,0,0.15,"Average over the sampling period","For existing plants operated < 500 h/yr, these levels are indicative.","LCP (2017)\n2017/1646","4.1.2",56,56]
[805,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Spark-ignited lean-burn gas engine","New","Natural gas ","≥ 50 MWth",0,"Emissions to air ","Air","Formaldehyde and CH5","Formaldehyde and CH4",0,"mg/Nm3",215,"500","Green","Once every year",0,0,0.15,"Average over the sampling period","This BAT-AEL is expressed as C at full load operation.","LCP (2017)\n2017/1647","4.1.2",56,56]
[806,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Spark-ignited lean-burn gas engine","Existing","Natural gas ","≥ 50 MWth",0,"Emissions to air ","Air","Formaldehyde and CH6","Formaldehyde and CH4",0,"mg/Nm3",215,"560","Green","Once every year",0,0,0.15,"Average over the sampling period","For existing plants operated < 500 h/yr, these levels are indicative.\n\nThis BAT-AEL is expressed as C at full load operation.","LCP (2017)\n2017/1648","4.1.2",56,56]
[651,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","Existing","Coal and/or lignite ","< 100 MWth",0,"Emissions to air ","Air","Hydrogen chloride, expressed as HCl","Hydrogen chloride","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD; (viii) Combined techniques for NOX and SOX reduction; (ix) Replacement or removal of the gas- gas heater located downstream of the wet FGD; (x) Fuel choice","mg/Nm3",2,10,"Green","Once every three months ",0,0,0.06,"Yearly average or average of samples obtained during one year ","The lower end of these BAT-AEL ranges may be difficult to achieve in the case of plants fitted with wet FGD and a downstream gas-gas heater.\n\nThe higher end of the BAT-AEL range is 20 mg/Nm3 in the following cases: plants combusting fuels where the average chlorine content is 1 000 mg/kg (dry) or higher; plants operated < 1 500 h/yr; FBC boilers. For plants operated < 500 h/yr, these levels are indicative.","LCP (2017)\n2017/1493","2.1.4",33,33]
[653,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","Existing","Coal and/or lignite ","≥ 100 MWth",0,"Emissions to air ","Air","Hydrogen chloride, expressed as HCl","Hydrogen chloride","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD; (viii) Combined techniques for NOX and SOX reduction; (ix) Replacement or removal of the gas- gas heater located downstream of the wet FGD; (x) Fuel choice","mg/Nm3",1,5,"Green","Once every three months ",0,0,0.06,"Yearly average or average of samples obtained during one year ","The lower end of these BAT-AEL ranges may be difficult to achieve in the case of plants fitted with wet FGD and a downstream gas-gas heater.\n\nThe higher end of the BAT-AEL range is 20 mg/Nm3 in the following cases: plants combusting fuels where the average chlorine content is 1 000 mg/kg (dry) or higher; plants operated < 1 500 h/yr; FBC boilers. For plants operated < 500 h/yr, these levels are indicative.\n\nIn the case of plants fitted with wet FGD with a downstream gas-gas heater, the higher end of the BAT-AEL range is 7 mg/Nm3.","LCP (2017)\n2017/1495","2.1.4",33,33]
[707,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","Existing","Solid biomass and/or peat","< 100 MWth ",0,"Emissions to air ","Air","Hydrogen chloride, expressed as HCl","Hydrogen chloride","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3",1,"15","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ","For plants burning fuels where the average chlorine content is ≥ 0,1 wt-% (dry), or for existing plants co-combusting biomass with sulphur-rich fuel (e.g. peat) or using alkali chloride-converting additives (e.g. elemental sulphur), the higher end of the BAT-AEL range for the yearly average for new plants is 15 mg/Nm3, the higher end of the BAT-AEL range for the yearly average for existing plants is 25 mg/Nm3. The daily average BAT-AEL range does not apply to these plants.\n\nThe daily average BAT-AEL range does not apply to plants operated < 1 500 h/yr. The higher end of the BAT-AEL range for the yearly average for new plants operated < 1 500 h/yr is 15 mg/Nm3.\n\nThese BAT-AELs do not apply to plants operated < 1 500 h/yr.\n\nThe lower end of these BAT-AEL ranges may be difficult to achieve in the case of plants fitted with wet FGD and a downstream gas-gas heater.","LCP (2017)\n2017/1549","2.2.2",39,39]
[709,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","Existing","Solid biomass and/or peat","< 100 MWth ",0,"Emissions to air ","Air","Hydrogen chloride, expressed as HCl","Hydrogen chloride","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3",1,"35","Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ","For plants burning fuels where the average chlorine content is ≥ 0,1 wt-% (dry), or for existing plants co-combusting biomass with sulphur-rich fuel (e.g. peat) or using alkali chloride-converting additives (e.g. elemental sulphur), the higher end of the BAT-AEL range for the yearly average for new plants is 15 mg/Nm3, the higher end of the BAT-AEL range for the yearly average for existing plants is 25 mg/Nm3. The daily average BAT-AEL range does not apply to these plants.\n\nThe daily average BAT-AEL range does not apply to plants operated < 1 500 h/yr. The higher end of the BAT-AEL range for the yearly average for new plants operated < 1 500 h/yr is 15 mg/Nm3.\n\nFor plants operated < 500 h/yr, these levels are indicative","LCP (2017)\n2017/1551","2.2.2",39,39]
[715,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","Existing","Solid biomass and/or peat","≥ 300 MWth",0,"Emissions to air ","Air","Hydrogen chloride, expressed as HCl","Hydrogen chloride","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3",1,"5","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ","For plants burning fuels where the average chlorine content is ≥ 0,1 wt-% (dry), or for existing plants co-combusting biomass with sulphur-rich fuel (e.g. peat) or using alkali chloride-converting additives (e.g. elemental sulphur), the higher end of the BAT-AEL range for the yearly average for new plants is 15 mg/Nm3, the higher end of the BAT-AEL range for the yearly average for existing plants is 25 mg/Nm3. The daily average BAT-AEL range does not apply to these plants.\n\nThe daily average BAT-AEL range does not apply to plants operated < 1 500 h/yr. The higher end of the BAT-AEL range for the yearly average for new plants operated < 1 500 h/yr is 15 mg/Nm3.\n\nThese BAT-AELs do not apply to plants operated < 1 500 h/yr.\n\nThe lower end of these BAT-AEL ranges may be difficult to achieve in the case of plants fitted with wet FGD and a downstream gas-gas heater.","LCP (2017)\n2017/1557","2.2.2",39,39]
[717,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","Existing","Solid biomass and/or peat","≥ 300 MWth",0,"Emissions to air ","Air","Hydrogen chloride, expressed as HCl","Hydrogen chloride","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3",1,"12","Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ","For plants burning fuels where the average chlorine content is ≥ 0,1 wt-% (dry), or for existing plants co-combusting biomass with sulphur-rich fuel (e.g. peat) or using alkali chloride-converting additives (e.g. elemental sulphur), the higher end of the BAT-AEL range for the yearly average for new plants is 15 mg/Nm3, the higher end of the BAT-AEL range for the yearly average for existing plants is 25 mg/Nm3. The daily average BAT-AEL range does not apply to these plants.\n\nThe daily average BAT-AEL range does not apply to plants operated < 1 500 h/yr. The higher end of the BAT-AEL range for the yearly average for new plants operated < 1 500 h/yr is 15 mg/Nm3.\n\nFor plants operated < 500 h/yr, these levels are indicative","LCP (2017)\n2017/1559","2.2.2",39,39]
[711,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","Existing","Solid biomass and/or peat","100-300 MWth",0,"Emissions to air ","Air","Hydrogen chloride, expressed as HCl","Hydrogen chloride","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3",1,"9","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ","For plants burning fuels where the average chlorine content is ≥ 0,1 wt-% (dry), or for existing plants co-combusting biomass with sulphur-rich fuel (e.g. peat) or using alkali chloride-converting additives (e.g. elemental sulphur), the higher end of the BAT-AEL range for the yearly average for new plants is 15 mg/Nm3, the higher end of the BAT-AEL range for the yearly average for existing plants is 25 mg/Nm3. The daily average BAT-AEL range does not apply to these plants.\n\nThe daily average BAT-AEL range does not apply to plants operated < 1 500 h/yr. The higher end of the BAT-AEL range for the yearly average for new plants operated < 1 500 h/yr is 15 mg/Nm3.\n\nThese BAT-AELs do not apply to plants operated < 1 500 h/yr.\n\nThe lower end of these BAT-AEL ranges may be difficult to achieve in the case of plants fitted with wet FGD and a downstream gas-gas heater.","LCP (2017)\n2017/1553","2.2.2",39,39]
[713,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","Existing","Solid biomass and/or peat","100-300 MWth",0,"Emissions to air ","Air","Hydrogen chloride, expressed as HCl","Hydrogen chloride","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3",1,"12","Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ","For plants burning fuels where the average chlorine content is ≥ 0,1 wt-% (dry), or for existing plants co-combusting biomass with sulphur-rich fuel (e.g. peat) or using alkali chloride-converting additives (e.g. elemental sulphur), the higher end of the BAT-AEL range for the yearly average for new plants is 15 mg/Nm3, the higher end of the BAT-AEL range for the yearly average for existing plants is 25 mg/Nm3. The daily average BAT-AEL range does not apply to these plants.\n\nThe daily average BAT-AEL range does not apply to plants operated < 1 500 h/yr. The higher end of the BAT-AEL range for the yearly average for new plants operated < 1 500 h/yr is 15 mg/Nm3.\n\nFor plants operated < 500 h/yr, these levels are indicative","LCP (2017)\n2017/1555","2.2.2",39,39]
[650,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","New","Coal and/or lignite ","< 100 MWth",0,"Emissions to air ","Air","Hydrogen chloride, expressed as HCl","Hydrogen chloride","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD; (viii) Combined techniques for NOX and SOX reduction; (ix) Replacement or removal of the gas- gas heater located downstream of the wet FGD; (x) Fuel choice","mg/Nm3",1,6,"Green","Once every three months ",0,0,0.06,"Yearly average or average of samples obtained during one year ",0,"LCP (2017)\n2017/1492","2.1.4",33,33]
[652,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","New","Coal and/or lignite ","≥ 100 MWth",0,"Emissions to air ","Air","Hydrogen chloride, expressed as HCl","Hydrogen chloride","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD; (viii) Combined techniques for NOX and SOX reduction; (ix) Replacement or removal of the gas- gas heater located downstream of the wet FGD; (x) Fuel choice","mg/Nm3",1,3,"Green","Once every three months ",0,0,0.06,"Yearly average or average of samples obtained during one year ",0,"LCP (2017)\n2017/1494","2.1.4",33,33]
[706,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","New","Solid biomass and/or peat","< 100 MWth ",0,"Emissions to air ","Air","Hydrogen chloride, expressed as HCl","Hydrogen chloride","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3",1,"7","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ","For plants burning fuels where the average chlorine content is ≥ 0,1 wt-% (dry), or for existing plants co-combusting biomass with sulphur-rich fuel (e.g. peat) or using alkali chloride-converting additives (e.g. elemental sulphur), the higher end of the BAT-AEL range for the yearly average for new plants is 15 mg/Nm3, the higher end of the BAT-AEL range for the yearly average for existing plants is 25 mg/Nm3. The daily average BAT-AEL range does not apply to these plants.\n\nThe daily average BAT-AEL range does not apply to plants operated < 1 500 h/yr. The higher end of the BAT-AEL range for the yearly average for new plants operated < 1 500 h/yr is 15 mg/Nm3.","LCP (2017)\n2017/1548","2.2.2",39,39]
[708,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","New","Solid biomass and/or peat","< 100 MWth ",0,"Emissions to air ","Air","Hydrogen chloride, expressed as HCl","Hydrogen chloride","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3",1,"12","Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ","For plants burning fuels where the average chlorine content is ≥ 0,1 wt-% (dry), or for existing plants co-combusting biomass with sulphur-rich fuel (e.g. peat) or using alkali chloride-converting additives (e.g. elemental sulphur), the higher end of the BAT-AEL range for the yearly average for new plants is 15 mg/Nm3, the higher end of the BAT-AEL range for the yearly average for existing plants is 25 mg/Nm3. The daily average BAT-AEL range does not apply to these plants.\n\nThe daily average BAT-AEL range does not apply to plants operated < 1 500 h/yr. The higher end of the BAT-AEL range for the yearly average for new plants operated < 1 500 h/yr is 15 mg/Nm3.","LCP (2017)\n2017/1550","2.2.2",39,39]
[714,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","New","Solid biomass and/or peat","≥ 300 MWth",0,"Emissions to air ","Air","Hydrogen chloride, expressed as HCl","Hydrogen chloride","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3",1,"5","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ","For plants burning fuels where the average chlorine content is ≥ 0,1 wt-% (dry), or for existing plants co-combusting biomass with sulphur-rich fuel (e.g. peat) or using alkali chloride-converting additives (e.g. elemental sulphur), the higher end of the BAT-AEL range for the yearly average for new plants is 15 mg/Nm3, the higher end of the BAT-AEL range for the yearly average for existing plants is 25 mg/Nm3. The daily average BAT-AEL range does not apply to these plants.\n\nThe daily average BAT-AEL range does not apply to plants operated < 1 500 h/yr. The higher end of the BAT-AEL range for the yearly average for new plants operated < 1 500 h/yr is 15 mg/Nm3.\n\nThese BAT-AELs do not apply to plants operated < 1 500 h/yr.\n\nThe lower end of these BAT-AEL ranges may be difficult to achieve in the case of plants fitted with wet FGD and a downstream gas-gas heater.","LCP (2017)\n2017/1556","2.2.2",39,39]
[716,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","New","Solid biomass and/or peat","≥ 300 MWth",0,"Emissions to air ","Air","Hydrogen chloride, expressed as HCl","Hydrogen chloride","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3",1,"12","Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ","For plants burning fuels where the average chlorine content is ≥ 0,1 wt-% (dry), or for existing plants co-combusting biomass with sulphur-rich fuel (e.g. peat) or using alkali chloride-converting additives (e.g. elemental sulphur), the higher end of the BAT-AEL range for the yearly average for new plants is 15 mg/Nm3, the higher end of the BAT-AEL range for the yearly average for existing plants is 25 mg/Nm3. The daily average BAT-AEL range does not apply to these plants.\n\nThe daily average BAT-AEL range does not apply to plants operated < 1 500 h/yr. The higher end of the BAT-AEL range for the yearly average for new plants operated < 1 500 h/yr is 15 mg/Nm3.","LCP (2017)\n2017/1558","2.2.2",39,39]
[710,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","New","Solid biomass and/or peat","100-300 MWth",0,"Emissions to air ","Air","Hydrogen chloride, expressed as HCl","Hydrogen chloride","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3",1,"5","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ","For plants burning fuels where the average chlorine content is ≥ 0,1 wt-% (dry), or for existing plants co-combusting biomass with sulphur-rich fuel (e.g. peat) or using alkali chloride-converting additives (e.g. elemental sulphur), the higher end of the BAT-AEL range for the yearly average for new plants is 15 mg/Nm3, the higher end of the BAT-AEL range for the yearly average for existing plants is 25 mg/Nm3. The daily average BAT-AEL range does not apply to these plants.\n\nThe daily average BAT-AEL range does not apply to plants operated < 1 500 h/yr. The higher end of the BAT-AEL range for the yearly average for new plants operated < 1 500 h/yr is 15 mg/Nm3.","LCP (2017)\n2017/1552","2.2.2",39,39]
[712,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","New","Solid biomass and/or peat","100-300 MWth",0,"Emissions to air ","Air","Hydrogen chloride, expressed as HCl","Hydrogen chloride","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3",1,"12","Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ","For plants burning fuels where the average chlorine content is ≥ 0,1 wt-% (dry), or for existing plants co-combusting biomass with sulphur-rich fuel (e.g. peat) or using alkali chloride-converting additives (e.g. elemental sulphur), the higher end of the BAT-AEL range for the yearly average for new plants is 15 mg/Nm3, the higher end of the BAT-AEL range for the yearly average for existing plants is 25 mg/Nm3. The daily average BAT-AEL range does not apply to these plants.\n\nThe daily average BAT-AEL range does not apply to plants operated < 1 500 h/yr. The higher end of the BAT-AEL range for the yearly average for new plants operated < 1 500 h/yr is 15 mg/Nm3.","LCP (2017)\n2017/1554","2.2.2",39,39]
[836,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Boilers","Existing","Process fuels from the chemical industry","< 100 MWth",0,"Emissions to air ","Air","Hydrogen chloride, expressed as HCl","Hydrogen chloride","In order to reduce SOX, HCl and HF emissions to air from the combustion of process fuels from the chemical industry in boilers, BAT is to use one or a combination of the techniques given below: (i) Fuel choice; (ii) Boiler sorbent injection (in-furnace or in-bed); (iii) Duct sorbent injection (DSI); (iv) Spray dry absorber (SDA); (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD Table","mg/Nm3",2,"15","Green","Once every three months ",0,0,0.03,"Average of samples obtained during one year","For plants operated < 500 h/yr, these levels are indicative.\n\nIn the case of plants operated < 1 500 h/yr, the higher end of the BAT-AEL range is 20 mg/Nm3.","LCP (2017)\n2017/1678","5.1.4",68,68]
[840,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Boilers","Existing","Process fuels from the chemical industry","≥ 100 MWth",0,"Emissions to air ","Air","Hydrogen chloride, expressed as HCl","Hydrogen chloride","In order to reduce SOX, HCl and HF emissions to air from the combustion of process fuels from the chemical industry in boilers, BAT is to use one or a combination of the techniques given below: (i) Fuel choice; (ii) Boiler sorbent injection (in-furnace or in-bed); (iii) Duct sorbent injection (DSI); (iv) Spray dry absorber (SDA); (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD Table","mg/Nm3",1,"9","Green","Once every three months ",0,0,0.03,"Average of samples obtained during one year","For plants operated < 500 h/yr, these levels are indicative.\n\nIn the case of plants operated < 1 500 h/yr, the higher end of the BAT-AEL range is 20 mg/Nm3.","LCP (2017)\n2017/1682","5.1.4",68,68]
[835,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Boilers","New","Process fuels from the chemical industry","< 100 MWth",0,"Emissions to air ","Air","Hydrogen chloride, expressed as HCl","Hydrogen chloride","In order to reduce SOX, HCl and HF emissions to air from the combustion of process fuels from the chemical industry in boilers, BAT is to use one or a combination of the techniques given below: (i) Fuel choice; (ii) Boiler sorbent injection (in-furnace or in-bed); (iii) Duct sorbent injection (DSI); (iv) Spray dry absorber (SDA); (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD Table","mg/Nm3",1,"7","Green","Once every three months ",0,0,0.03,"Average of samples obtained during one year",0,"LCP (2017)\n2017/1677","5.1.4",68,68]
[839,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Boilers","New","Process fuels from the chemical industry","≥ 100 MWth",0,"Emissions to air ","Air","Hydrogen chloride, expressed as HCl","Hydrogen chloride","In order to reduce SOX, HCl and HF emissions to air from the combustion of process fuels from the chemical industry in boilers, BAT is to use one or a combination of the techniques given below: (i) Fuel choice; (ii) Boiler sorbent injection (in-furnace or in-bed); (iii) Duct sorbent injection (DSI); (iv) Spray dry absorber (SDA); (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD Table","mg/Nm3",1,"5","Green","Once every three months ",0,0,0.03,"Average of samples obtained during one year",0,"LCP (2017)\n2017/1681","5.1.4",68,68]
[655,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","Existing","Coal and/or lignite ","< 100 MWth",0,"Emissions to air ","Air","HF","Hydrogen fluoride (as F) (Ecological - Daily Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD; (viii) Combined techniques for NOX and SOX reduction; (ix) Replacement or removal of the gas- gas heater located downstream of the wet FGD; (x) Fuel choice","mg/Nm3",1,6,"Green","Once every three months ",0,0,0.06,"Yearly average or average of samples obtained during one year ","The higher end of the BAT-AEL range is 7 mg/Nm3 in the following cases: plants fitted with wet FGD with a downstream gas-gas heater; plants operated < 1 500 h/yr; FBC boilers. For plants operated < 500 h/yr, these levels are indicative.","LCP (2017)\n2017/1497","2.1.4",33,33]
[719,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","Existing","Solid biomass and/or peat","< 100 MWth",0,"Emissions to air ","Air","HF","Hydrogen fluoride (as F) (Ecological - Daily Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3","N/A","1.5","Green","Once every year",0,0,0.06,"Average over sampling period ","For plants operated < 500 h/yr, these levels are indicative.","LCP (2017)\n2017/1561","2.2.4",40,40]
[723,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","Existing","Solid biomass and/or peat","≥ 300 MWth",0,"Emissions to air ","Air","HF","Hydrogen fluoride (as F) (Ecological - Daily Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3","N/A","1","Green","Once every year",0,0,0.06,"Average over sampling period ","For plants operated < 500 h/yr, these levels are indicative.","LCP (2017)\n2017/1565","2.2.4",40,40]
[721,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","Existing","Solid biomass and/or peat","100-300 MWth",0,"Emissions to air ","Air","HF","Hydrogen fluoride (as F) (Ecological - Daily Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3","N/A","1","Green","Once every year",0,0,0.06,"Average over sampling period ","For plants operated < 500 h/yr, these levels are indicative.","LCP (2017)\n2017/1563","2.2.4",40,40]
[654,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","New","Coal and/or lignite ","< 100 MWth",0,"Emissions to air ","Air","HF","Hydrogen fluoride (as F) (Ecological - Daily Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD; (viii) Combined techniques for NOX and SOX reduction; (ix) Replacement or removal of the gas- gas heater located downstream of the wet FGD; (x) Fuel choice","mg/Nm3",1,3,"Green","Once every three months ",0,0,0.06,"Yearly average or average of samples obtained during one year ",0,"LCP (2017)\n2017/1496","2.1.4",33,33]
[656,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","New","Coal and/or lignite ","≥ 100 MWth",0,"Emissions to air ","Air","HF","Hydrogen fluoride (as F) (Ecological - Daily Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD; (viii) Combined techniques for NOX and SOX reduction; (ix) Replacement or removal of the gas- gas heater located downstream of the wet FGD; (x) Fuel choice","mg/Nm3",1,2,"Green","Once every three months ",0,0,0.06,"Yearly average or average of samples obtained during one year ",0,"LCP (2017)\n2017/1498","2.1.4",33,33]
[718,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","New","Solid biomass and/or peat","< 100 MWth",0,"Emissions to air ","Air","HF","Hydrogen fluoride (as F) (Ecological - Daily Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3","N/A","1","Green","Once every year",0,0,0.06,"Average over sampling period ",0,"LCP (2017)\n2017/1560","2.2.4",40,40]
[722,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","New","Solid biomass and/or peat","≥ 300 MWth",0,"Emissions to air ","Air","HF","Hydrogen fluoride (as F) (Ecological - Daily Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3","N/A","1","Green","Once every year",0,0,0.06,"Average over sampling period ",0,"LCP (2017)\n2017/1564","2.2.4",40,40]
[720,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","New","Solid biomass and/or peat","100-300 MWth",0,"Emissions to air ","Air","HF","Hydrogen fluoride (as F) (Ecological - Daily Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3","N/A","1","Green","Once every year",0,0,0.06,"Average over sampling period ",0,"LCP (2017)\n2017/1562","2.2.4",40,40]
[838,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Boilers","Existing","Process fuels from the chemical industry","< 100 MWth",0,"Emissions to air ","Air","HF","Hydrogen fluoride (as F) (Ecological - Daily Mean)","In order to reduce SOX, HCl and HF emissions to air from the combustion of process fuels from the chemical industry in boilers, BAT is to use one or a combination of the techniques given below: (i) Fuel choice; (ii) Boiler sorbent injection (in-furnace or in-bed); (iii) Duct sorbent injection (DSI); (iv) Spray dry absorber (SDA); (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD Table","mg/Nm3",1,"6","Green","Once every three months ",0,0,0.03,"Average of samples obtained during one year","For plants operated < 500 h/yr, these levels are indicative.\n\nIn the case of plants operated < 1 500 h/yr, the higher end of the BAT-AEL range is 7 mg/Nm3.","LCP (2017)\n2017/1680","5.1.4",68,68]
[842,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Boilers","Existing","Process fuels from the chemical industry","≥ 100 MWth",0,"Emissions to air ","Air","HF","Hydrogen fluoride (as F) (Ecological - Daily Mean)","In order to reduce SOX, HCl and HF emissions to air from the combustion of process fuels from the chemical industry in boilers, BAT is to use one or a combination of the techniques given below: (i) Fuel choice; (ii) Boiler sorbent injection (in-furnace or in-bed); (iii) Duct sorbent injection (DSI); (iv) Spray dry absorber (SDA); (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD Table","mg/Nm3",1,"3","Green","Once every three months ",0,0,0.03,"Average of samples obtained during one year","For plants operated < 500 h/yr, these levels are indicative.\n\nIn the case of plants operated < 1 500 h/yr, the higher end of the BAT-AEL range is 7 mg/Nm3.","LCP (2017)\n2017/1684","5.1.4",68,68]
[837,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Boilers","New","Process fuels from the chemical industry","< 100 MWth",0,"Emissions to air ","Air","HF","Hydrogen fluoride (as F) (Ecological - Daily Mean)","In order to reduce SOX, HCl and HF emissions to air from the combustion of process fuels from the chemical industry in boilers, BAT is to use one or a combination of the techniques given below: (i) Fuel choice; (ii) Boiler sorbent injection (in-furnace or in-bed); (iii) Duct sorbent injection (DSI); (iv) Spray dry absorber (SDA); (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD Table","mg/Nm3","N/A","1-3","Green","Once every three months ",0,0,0.03,"Average of samples obtained during one year",0,"LCP (2017)\n2017/1679","5.1.4",68,68]
[841,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Boilers","New","Process fuels from the chemical industry","≥ 100 MWth",0,"Emissions to air ","Air","HF","Hydrogen fluoride (as F) (Ecological - Daily Mean)","In order to reduce SOX, HCl and HF emissions to air from the combustion of process fuels from the chemical industry in boilers, BAT is to use one or a combination of the techniques given below: (i) Fuel choice; (ii) Boiler sorbent injection (in-furnace or in-bed); (iii) Duct sorbent injection (DSI); (iv) Spray dry absorber (SDA); (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD Table","mg/Nm3",1,"2","Green","Once every three months ",0,0,0.03,"Average of samples obtained during one year",0,"LCP (2017)\n2017/1683","5.1.4",68,68]
[657,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","Existing","Coal and/or lignite ","≥ 100 MWth",0,"Emissions to air ","Air","HF ","Hydrogen fluoride (as F) (Ecological - Daily Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD; (viii) Combined techniques for NOX and SOX reduction; (ix) Replacement or removal of the gas- gas heater located downstream of the wet FGD; (x) Fuel choice","mg/Nm3",1,3,"Green","Once every three months ",0,0,0.06,"Yearly average or average of samples obtained during one year ","The higher end of the BAT-AEL range is 7 mg/Nm3 in the following cases: plants fitted with wet FGD with a downstream gas-gas heater; plants operated < 1 500 h/yr; FBC boilers. For plants operated < 500 h/yr, these levels are indicative.","LCP (2017)\n2017/1499","2.1.4",33,33]
[676,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","Existing","Coal","< 300 MWth ",0,"Emissions to air ","Air","Mercury","Mercury and compounds, except mercury alkyls, (as","In order to prevent or reduce mercury emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Dry or semi-dry FGD system; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Selective catalytic reduction (SCR); (vi) Carbon sorbent (e.g. activated carbon or halogenated activated carbon) injection in the flue- gas; (vii) Use of halogenated additives in the fuel or injected in the furnace; (viii) Fuel pretreatment; (ix) Fuel choice ","ug/Nm3",1,"9","Green","Once every three months ",0,0,0.06,"Yearly average or average of samples obtained during one year ","The lower end of the BAT-AEL range can be achieved with specific mercury abatement techniques.","LCP (2017)\n2017/1518","2.1.6",35,35]
[680,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","Existing","Coal","≥ 300 MWth",0,"Emissions to air ","Air","Mercury","Mercury and compounds, except mercury alkyls, (as","In order to prevent or reduce mercury emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Dry or semi-dry FGD system; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Selective catalytic reduction (SCR); (vi) Carbon sorbent (e.g. activated carbon or halogenated activated carbon) injection in the flue- gas; (vii) Use of halogenated additives in the fuel or injected in the furnace; (viii) Fuel pretreatment; (ix) Fuel choice ","ug/Nm3",1,"4","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ","The lower end of the BAT-AEL range can be achieved with specific mercury abatement techniques.","LCP (2017)\n2017/1522","2.1.6",35,35]
[677,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","Existing","Lignite","< 300 MWth ",0,"Emissions to air ","Air","Mercury","Mercury and compounds, except mercury alkyls, (as","In order to prevent or reduce mercury emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Dry or semi-dry FGD system; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Selective catalytic reduction (SCR); (vi) Carbon sorbent (e.g. activated carbon or halogenated activated carbon) injection in the flue- gas; (vii) Use of halogenated additives in the fuel or injected in the furnace; (viii) Fuel pretreatment; (ix) Fuel choice ","ug/Nm3",1,"10","Green","Once every three months ",0,0,0.06,"Yearly average or average of samples obtained during one year ","The lower end of the BAT-AEL range can be achieved with specific mercury abatement techniques.","LCP (2017)\n2017/1519","2.1.6",35,35]
[681,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","Existing","Lignite","≥ 300 MWth",0,"Emissions to air ","Air","Mercury","Mercury and compounds, except mercury alkyls, (as","In order to prevent or reduce mercury emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Dry or semi-dry FGD system; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Selective catalytic reduction (SCR); (vi) Carbon sorbent (e.g. activated carbon or halogenated activated carbon) injection in the flue- gas; (vii) Use of halogenated additives in the fuel or injected in the furnace; (viii) Fuel pretreatment; (ix) Fuel choice ","ug/Nm3",1,"7","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ","The lower end of the BAT-AEL range can be achieved with specific mercury abatement techniques.","LCP (2017)\n2017/1523","2.1.6",35,35]
[674,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","New","Coal","< 300 MWth ",0,"Emissions to air ","Air","Mercury","Mercury and compounds, except mercury alkyls, (as","In order to prevent or reduce mercury emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Dry or semi-dry FGD system; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Selective catalytic reduction (SCR); (vi) Carbon sorbent (e.g. activated carbon or halogenated activated carbon) injection in the flue- gas; (vii) Use of halogenated additives in the fuel or injected in the furnace; (viii) Fuel pretreatment; (ix) Fuel choice ","ug/Nm3",1,"3","Green","Once every three months ",0,0,0.06,"Yearly average or average of samples obtained during one year ",0,"LCP (2017)\n2017/1516","2.1.6",35,35]
[678,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","New","Coal","≥ 300 MWth",0,"Emissions to air ","Air","Mercury","Mercury and compounds, except mercury alkyls, (as","In order to prevent or reduce mercury emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Dry or semi-dry FGD system; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Selective catalytic reduction (SCR); (vi) Carbon sorbent (e.g. activated carbon or halogenated activated carbon) injection in the flue- gas; (vii) Use of halogenated additives in the fuel or injected in the furnace; (viii) Fuel pretreatment; (ix) Fuel choice ","ug/Nm3",1,"2","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ",0,"LCP (2017)\n2017/1520","2.1.6",35,35]
[675,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","New","Lignite","< 300 MWth ",0,"Emissions to air ","Air","Mercury","Mercury and compounds, except mercury alkyls, (as","In order to prevent or reduce mercury emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Dry or semi-dry FGD system; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Selective catalytic reduction (SCR); (vi) Carbon sorbent (e.g. activated carbon or halogenated activated carbon) injection in the flue- gas; (vii) Use of halogenated additives in the fuel or injected in the furnace; (viii) Fuel pretreatment; (ix) Fuel choice ","ug/Nm3",1,"5","Green","Once every three months ",0,0,0.06,"Yearly average or average of samples obtained during one year ",0,"LCP (2017)\n2017/1517","2.1.6",35,35]
[679,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","New","Lignite","≥ 300 MWth",0,"Emissions to air ","Air","Mercury","Mercury and compounds, except mercury alkyls, (as","In order to prevent or reduce mercury emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Dry or semi-dry FGD system; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Selective catalytic reduction (SCR); (vi) Carbon sorbent (e.g. activated carbon or halogenated activated carbon) injection in the flue- gas; (vii) Use of halogenated additives in the fuel or injected in the furnace; (viii) Fuel pretreatment; (ix) Fuel choice ","ug/Nm3",1,"4","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ",0,"LCP (2017)\n2017/1521","2.1.6",35,35]
[736,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","Existing","Solid biomass and/or peat","Unspecified ",0,"Emissions to air ","Air","Mercury ","Mercury and compounds, except mercury alkyls, (as","In order to prevent or reduce mercury emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Carbon sorbent (e.g. activated carbon or halogenated activated carbon) injection in the flue- gas; (ii) Use of halogenated additives in the fuel or injected in the furnace; (iii) Fuel choice; (iv) Electrostatic precipitator (ESP); (v) Bag filter; (vi) Dry or semi-dry FGD system; (vii) Wet flue-gas desulphurisation (wet FGD)","ug/Nm3",1,"5","Green","Once every year",0,0,0.06,"Average over the sampling period",0,"LCP (2017)\n2017/1578","2.2.5",41,41]
[788,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"CCGT with a net total fuel utilisation of < 75 %","Existing","Natural gas ","50-600 MWth",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",10,"45","Green","Continuous ",0,0,0.15,"Yearly","These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines\n\nIn the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective.\n\nThese BAT-AELs do not apply to existing plants operated < 1 500 h/yr.\n\nOptimising the functioning of an existing technique to reduce NOX emissions further may lead to levels of CO emissions at the higher end of the indicative range for CO emissions given after this table.\n\nThese BAT-AELs do not apply to existing turbines for mechanical drive applications or to plants operated < 500 h/yr.\n\nFor plants with a net electrical efficiency (EE) greater than 55 %, a correction factor may be applied to the higher end of the BAT-AEL range, corresponding to [higher end] × EE/55, where EE is the net electrical efficiency of the plant determined at ISO baseload conditions.","LCP (2017)\n2017/1630","4.1.2",54,54]
[789,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"CCGT with a net total fuel utilisation of < 75 %","Existing","Natural gas ","50-600 MWth",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",35,"55","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period ","These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines\n\nIn the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective.\n\nThese BAT-AELs do not apply to existing turbines for mechanical drive applications or to plants operated < 500 h/yr.\n\nFor plants with a net electrical efficiency (EE) greater than 55 %, a correction factor may be applied to the higher end of the BAT-AEL range, corresponding to [higher end] × EE/55, where EE is the net electrical efficiency of the plant determined at ISO baseload conditions.","LCP (2017)\n2017/1631","4.1.2",54,54]
[790,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"CCGT with a net total fuel utilisation of ≥ 75 %","Existing","Natural gas ","50-600 MWth",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",25,"50","Green","Continuous ",0,0,0.15,"Yearly","These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines\n\nIn the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective.\n\nThese BAT-AELs do not apply to existing plants operated < 1 500 h/yr.\n\nOptimising the functioning of an existing technique to reduce NOX emissions further may lead to levels of CO emissions at the higher end of the indicative range for CO emissions given after this table.\n\nThese BAT-AELs do not apply to existing turbines for mechanical drive applications or to plants operated < 500 h/yr.\n\nFor plants with a net electrical efficiency (EE) greater than 55 %, a correction factor may be applied to the higher end of the BAT-AEL range, corresponding to [higher end] × EE/55, where EE is the net electrical efficiency of the plant determined at ISO baseload conditions.\n\nFor existing plants put into operation no later than 7 January 2014, the higher end of the BAT-AEL range is 55 mg/Nm3.","LCP (2017)\n2017/1632","4.1.2",54,54]
[791,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"CCGT with a net total fuel utilisation of ≥ 75 %","Existing","Natural gas ","50-600 MWth",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",35,"55","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period ","These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines\n\nIn the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective.\n\nThese BAT-AELs do not apply to existing turbines for mechanical drive applications or to plants operated < 500 h/yr.\n\nFor plants with a net electrical efficiency (EE) greater than 55 %, a correction factor may be applied to the higher end of the BAT-AEL range, corresponding to [higher end] × EE/55, where EE is the net electrical efficiency of the plant determined at ISO baseload conditions.\n\nFor existing plants put into operation no later than 7 January 2014, the higher end of the BAT-AEL range is 80 mg/Nm3.","LCP (2017)\n2017/1633","4.1.2",54,54]
[618,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","Existing","Coal and/or lignite ","< 100 MWth",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Combination of other primary techniques for NOX reduction (e.g. air staging, fuel staging, flue-gas recirculation, low- NOX burners (LNB)); (iii) Selective non- catalytic reduction (SNCR); (iv) Selective catalytic reduction (SCR); (v) Combined techniques for NOX and SOX reduction","mg/Nm3",165,330,"Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ","In the case of coal-fired PC boiler plants put into operation no later than 1 July 1987, which are operated < 1 500 h/yr and for which SCR and/or SNCR is not applicable, the higher end of the range is 340 mg/Nm3.\n\nFor plants operated < 500 h/yr, these levels are indicative.","LCP (2017)\n2017/1460","2.1.3",30,30]
[622,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","Existing","Coal and/or lignite ","100-300 MWth",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Combination of other primary techniques for NOX reduction (e.g. air staging, fuel staging, flue-gas recirculation, low- NOX burners (LNB)); (iii) Selective non- catalytic reduction (SNCR); (iv) Selective catalytic reduction (SCR); (v) Combined techniques for NOX and SOX reduction","mg/Nm3",155,210,"Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ",0,"LCP (2017)\n2017/1464","2.1.3",30,30]
[616,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","Existing","Coal and/or lignite ","< 100 MWth",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Combination of other primary techniques for NOX reduction (e.g. air staging, fuel staging, flue-gas recirculation, low- NOX burners (LNB)); (iii) Selective non- catalytic reduction (SNCR); (iv) Selective catalytic reduction (SCR); (v) Combined techniques for NOX and SOX reduction","mg/Nm3",100,270,"Green","Continuous ",0,0,0.06,"Yearly","These BAT-AELs do not apply to plants operated < 1 500 h/yr.","LCP (2017)\n2017/1458","2.1.3",30,30]
[620,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","Existing","Coal and/or lignite ","100-300 MWth",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Combination of other primary techniques for NOX reduction (e.g. air staging, fuel staging, flue-gas recirculation, low- NOX burners (LNB)); (iii) Selective non- catalytic reduction (SNCR); (iv) Selective catalytic reduction (SCR); (v) Combined techniques for NOX and SOX reduction","mg/Nm3",100,180,"Green","Continuous ",0,0,0.06,"Yearly",0,"LCP (2017)\n2017/1462","2.1.3",30,30]
[691,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","Existing","Solid biomass and/or peat","≥ 300 MWth",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Low-NOX burners (LNB); (iii) Air staging; (iv) Fuel staging, (v) Flue-gas recirculation; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR)","mg/Nm3",40,"150","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ","The higher end of the BAT-AEL range is 160 mg/Nm3 for plants put into operation no later than 7 January 2014.","LCP (2017)\n2017/1533","2.2.2",37,37]
[693,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","Existing","Solid biomass and/or peat","≥ 300 MWth",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Low-NOX burners (LNB); (iii) Air staging; (iv) Fuel staging, (v) Flue-gas recirculation; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR)","mg/Nm3",95,"165","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ","The higher end of the BAT-AEL range is 200 mg/Nm3 for plants put into operation no later than 7 January 2014.","LCP (2017)\n2017/1535","2.2.2",37,37]
[687,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","Existing","Solid biomass and/or peat","100-300 MWth",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Low-NOX burners (LNB); (iii) Air staging; (iv) Fuel staging, (v) Flue-gas recirculation; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR)","mg/Nm3",50,"180","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ",0,"LCP (2017)\n2017/1529","2.2.2",37,37]
[689,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","Existing","Solid biomass and/or peat","100-300 MWth",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Low-NOX burners (LNB); (iii) Air staging; (iv) Fuel staging, (v) Flue-gas recirculation; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR)","mg/Nm3",100,"220","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ",0,"LCP (2017)\n2017/1531","2.2.2",37,37]
[683,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","Existing","Solid biomass and/or peat","50-100 MWth",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Low-NOX burners (LNB); (iii) Air staging; (iv) Fuel staging, (v) Flue-gas recirculation; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR)","mg/Nm3",70,"225","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ","For plants burning fuels where the average potassium content is 2 000 mg/kg (dry) or higher, and/or the average sodium content is 300 mg/kg or higher, the higher end of the BAT-AEL range is 250 mg/Nm3.","LCP (2017)\n2017/1525","2.2.2",37,37]
[685,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","Existing","Solid biomass and/or peat","50-100 MWth",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Low-NOX burners (LNB); (iii) Air staging; (iv) Fuel staging, (v) Flue-gas recirculation; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR)","mg/Nm3",120,"275","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ","For plants put into operation no later than 7 January 2014 and burning fuels where the average potassium content is 2 000 mg/kg (dry) or higher, and/or the average sodium content is 300 mg/kg or higher, the higher end of the BAT-AEL range is 310 mg/Nm3.","LCP (2017)\n2017/1527","2.2.2",37,37]
[615,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","New","Coal and/or lignite ","< 100 MWth",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Combination of other primary techniques for NOX reduction (e.g. air staging, fuel staging, flue-gas recirculation, low- NOX burners (LNB)); (iii) Selective non- catalytic reduction (SNCR); (iv) Selective catalytic reduction (SCR); (v) Combined techniques for NOX and SOX reduction","mg/Nm3",100,150,"Green","Continuous ",0,0,0.06,"Yearly",0,"LCP (2017)\n2017/1457","2.1.3",30,30]
[617,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","New","Coal and/or lignite ","< 100 MWth",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Combination of other primary techniques for NOX reduction (e.g. air staging, fuel staging, flue-gas recirculation, low- NOX burners (LNB)); (iii) Selective non- catalytic reduction (SNCR); (iv) Selective catalytic reduction (SCR); (v) Combined techniques for NOX and SOX reduction","mg/Nm3",155,200,"Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ",0,"LCP (2017)\n2017/1459","2.1.3",30,30]
[619,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","New","Coal and/or lignite ","100-300 MWth",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Combination of other primary techniques for NOX reduction (e.g. air staging, fuel staging, flue-gas recirculation, low- NOX burners (LNB)); (iii) Selective non- catalytic reduction (SNCR); (iv) Selective catalytic reduction (SCR); (v) Combined techniques for NOX and SOX reduction","mg/Nm3",50,100,"Green","Continuous ",0,0,0.06,"Yearly",0,"LCP (2017)\n2017/1461","2.1.3",30,30]
[621,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","New","Coal and/or lignite ","100-300 MWth",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Combination of other primary techniques for NOX reduction (e.g. air staging, fuel staging, flue-gas recirculation, low- NOX burners (LNB)); (iii) Selective non- catalytic reduction (SNCR); (iv) Selective catalytic reduction (SCR); (v) Combined techniques for NOX and SOX reduction","mg/Nm3",80,130,"Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ",0,"LCP (2017)\n2017/1463","2.1.3",30,30]
[690,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","New","Solid biomass and/or peat","≥ 300 MWth",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Low-NOX burners (LNB); (iii) Air staging; (iv) Fuel staging, (v) Flue-gas recirculation; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR)","mg/Nm3",40,"140","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ",0,"LCP (2017)\n2017/1532","2.2.2",37,37]
[692,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","New","Solid biomass and/or peat","≥ 300 MWth",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Low-NOX burners (LNB); (iii) Air staging; (iv) Fuel staging, (v) Flue-gas recirculation; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR)","mg/Nm3",65,"150","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ",0,"LCP (2017)\n2017/1534","2.2.2",37,37]
[686,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","New","Solid biomass and/or peat","100-300 MWth",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Low-NOX burners (LNB); (iii) Air staging; (iv) Fuel staging, (v) Flue-gas recirculation; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR)","mg/Nm3",50,"140","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ",0,"LCP (2017)\n2017/1528","2.2.2",37,37]
[688,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","New","Solid biomass and/or peat","100-300 MWth",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Low-NOX burners (LNB); (iii) Air staging; (iv) Fuel staging, (v) Flue-gas recirculation; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR)","mg/Nm3",100,"200","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ",0,"LCP (2017)\n2017/1530","2.2.2",37,37]
[682,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","New","Solid biomass and/or peat","50-100 MWth",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Low-NOX burners (LNB); (iii) Air staging; (iv) Fuel staging, (v) Flue-gas recirculation; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR)","mg/Nm3",70,"150","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ","For plants burning fuels where the average potassium content is 2 000 mg/kg (dry) or higher, and/or the average sodium content is 300 mg/kg or higher, the higher end of the BAT-AEL range is 200 mg/Nm3.","LCP (2017)\n2017/1524","2.2.2",37,37]
[684,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","New","Solid biomass and/or peat","50-100 MWth",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Low-NOX burners (LNB); (iii) Air staging; (iv) Fuel staging, (v) Flue-gas recirculation; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR)","mg/Nm3",120,"200","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ","For plants burning fuels where the average potassium content is 2 000 mg/kg (dry) or higher, and/or the average sodium content is 300 mg/kg or higher, the higher end of the BAT-AEL range is 260 mg/Nm3.","LCP (2017)\n2017/1526","2.2.2",37,37]
[809,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Boilers","Existing","100% iron and steel process gases ","Unspecified ",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of iron and steel process gases in CCGTs, BAT is to use one or a combination of the techniques given below: (i) Process gas management system; (ii) Advanced control system; (iii) Water/steam addition; (iv) Dry low-NOX burners(DLN); (v) Low-NOX burners (LNB); (vi) Selective catalytic reduction (SCR)","mg/Nm3",20,"100","Green","Continuous ",0,0,0.03,"Yearly","Plants combusting a mixture of gases with an equivalent LHV of > 20 MJ/Nm3 are expected to emit at the higher end of the BAT-AEL ranges.\n\nThe lower end of the BAT-AEL range can be achieved when using SCR.\n\nFor plants operated < 1 500 h/yr, these BAT AELs do not apply.","LCP (2017)\n2017/1651","4.2.2",59,59]
[810,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Boilers","Existing","100% iron and steel process gases ","Unspecified ",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of iron and steel process gases in CCGTs, BAT is to use one or a combination of the techniques given below: (i) Process gas management system; (ii) Advanced control system; (iii) Water/steam addition; (iv) Dry low-NOX burners(DLN); (v) Low-NOX burners (LNB); (vi) Selective catalytic reduction (SCR)","mg/Nm3",22,"110","Green","Continuous ",0,0,0.03,"Daily average or average over sampling period ","Plants combusting a mixture of gases with an equivalent LHV of > 20 MJ/Nm3 are expected to emit at the higher end of the BAT-AEL ranges.\n\nThe lower end of the BAT-AEL range can be achieved when using SCR.\n\nIn the case of plants put into operation no later than 7 January 2014, the higher end of the BAT-AEL range is 160 mg/Nm3. Furthermore, the higher end of the BAT-AEL range may be exceeded when SCR cannot be used and when using a high share of COG (e.g. > 50 %) and/or when combusting COG with a relatively high level of H2. In this case, the higher end of the BAT-AEL range is 220 mg/Nm3.\n\nFor plants operated < 500 h/yr, these levels are indicative.","LCP (2017)\n2017/1652","4.2.2",59,59]
[807,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Boilers","New","100% iron and steel process gases ","Unspecified ",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of iron and steel process gases in CCGTs, BAT is to use one or a combination of the techniques given below: (i) Process gas management system; (ii) Advanced control system; (iii) Water/steam addition; (iv) Dry low-NOX burners(DLN); (v) Low-NOX burners (LNB); (vi) Selective catalytic reduction (SCR)","mg/Nm3",15,"65","Green","Continuous ",0,0,0.03,"Yearly","Plants combusting a mixture of gases with an equivalent LHV of > 20 MJ/Nm3 are expected to emit at the higher end of the BAT-AEL ranges.","LCP (2017)\n2017/1649","4.2.2",59,59]
[808,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Boilers","New","100% iron and steel process gases ","Unspecified ",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of iron and steel process gases in CCGTs, BAT is to use one or a combination of the techniques given below: (i) Process gas management system; (ii) Advanced control system; (iii) Water/steam addition; (iv) Dry low-NOX burners(DLN); (v) Low-NOX burners (LNB); (vi) Selective catalytic reduction (SCR)","mg/Nm3",22,"100","Green","Continuous ",0,0,0.03,"Daily average or average over sampling period ","Plants combusting a mixture of gases with an equivalent LHV of > 20 MJ/Nm3 are expected to emit at the higher end of the BAT-AEL ranges.","LCP (2017)\n2017/1650","4.2.2",59,59]
[830,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Boilers","Existing","Gases only ","Unspecified ",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO emissions to air from the combustion of process fuels from the chemical industry, BAT is to use one or a combination of the techniques given below: (i) Low-NOX burners (LNB); (ii) Air staging; (iii) Fuel staging; (iv) Flue-gas recirculation; (v) Water/steam addition; (vi) Fuel choice; (vii) Advanced control system; (viii) Selective non-catalytic reduction (SNCR); (ix) Selective catalytic reduction (SCR)","mg/Nm3",70,"100","Green","Continuous ",0,0,0.03,"Yearly","For plants operated < 1 500 h/yr, these BAT AELs do not apply.  \n\nFor existing plants put into operation no later than 7 January 2014, the higher end of the BAT-AEL range is 180 mg/Nm3.","LCP (2017)\n2017/1672","5.1.3",66,66]
[832,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Boilers","Existing","Gases only ","Unspecified ",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO emissions to air from the combustion of process fuels from the chemical industry, BAT is to use one or a combination of the techniques given below: (i) Low-NOX burners (LNB); (ii) Air staging; (iii) Fuel staging; (iv) Flue-gas recirculation; (v) Water/steam addition; (vi) Fuel choice; (vii) Advanced control system; (viii) Selective non-catalytic reduction (SNCR); (ix) Selective catalytic reduction (SCR)","mg/Nm3",85,"110","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ","For plants operated < 500 h/yr, these levels are indicative.\n\nFor existing plants put into operation no later than 7 January 2014, the higher end of the BAT-AEL range is 210 mg/Nm3.","LCP (2017)\n2017/1674","5.1.3",66,66]
[738,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Boilers","Existing","HFO and/or gas oil in boilers","< 100 MWth",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Air staging; (ii) Fuel staging; (iii) Flue-gas recirculation; (iv) Low-NOX burners (LNB); (v) Water/steam addition; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR); (viii) Advanced control systeml (ix) Fuel choice","mg/Nm3",150,"270","Green","Continuous ",0,0,0.03,"Yearly","These BAT-AELs do not apply to plants operated < 1 500 h/yr.","LCP (2017)\n2017/1580","3.1.2",42,42]
[740,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Boilers","Existing","HFO and/or gas oil in boilers","< 100 MWth",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Air staging; (ii) Fuel staging; (iii) Flue-gas recirculation; (iv) Low-NOX burners (LNB); (v) Water/steam addition; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR); (viii) Advanced control systeml (ix) Fuel choice","mg/Nm3",210,"330","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ","For plants operated < 500 h/yr, these levels are indicative.\n\nFor industrial boilers and district heating plants put into operation no later than 27 November 2003, which are operated < 1 500 h/yr and for which SCR and/or SNCR is not applicable, the higher end of the BAT-AEL range is 450 mg/Nm3.","LCP (2017)\n2017/1582","3.1.2",42,42]
[742,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Boilers","Existing","HFO and/or gas oil in boilers","≥ 100 MWth",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Air staging; (ii) Fuel staging; (iii) Flue-gas recirculation; (iv) Low-NOX burners (LNB); (v) Water/steam addition; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR); (viii) Advanced control systeml (ix) Fuel choice","mg/Nm3",45,"100","Green","Continuous ",0,0,0.03,"Yearly","The higher end of the BAT-AEL range is 110 mg/Nm3 for plants of 100–300 MWth and plants of ≥ 300 MWth that were put into operation no later than 7 January 2014.","LCP (2017)\n2017/1584","3.1.2",42,42]
[744,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Boilers","Existing","HFO and/or gas oil in boilers","≥ 100 MWth",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Air staging; (ii) Fuel staging; (iii) Flue-gas recirculation; (iv) Low-NOX burners (LNB); (v) Water/steam addition; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR); (viii) Advanced control systeml (ix) Fuel choice","mg/Nm3",85,"110","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ","For industrial boilers and district heating plants of > 100 MWth put into operation no later than 27 November 2003, which are operated < 1 500 h/yr and for which SCR and/or SNCR is not applicable, the higher end of the BAT-AEL range is 365 mg/Nm3.","LCP (2017)\n2017/1586","3.1.2",42,42]
[826,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Boilers","Existing","Mixture of gases and liquids","Unspecified ",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO emissions to air from the combustion of process fuels from the chemical industry, BAT is to use one or a combination of the techniques given below: (i) Low-NOX burners (LNB); (ii) Air staging; (iii) Fuel staging; (iv) Flue-gas recirculation; (v) Water/steam addition; (vi) Fuel choice; (vii) Advanced control system; (viii) Selective non-catalytic reduction (SNCR); (ix) Selective catalytic reduction (SCR)","mg/Nm3",80,"290","Green","Continuous ",0,0,0.03,"Yearly","For plants operated < 1 500 h/yr, these BAT AELs do not apply.\n\nFor existing plants of ≤ 500 MWth put into operation no later than 27 November 2003 using liquid fuels with a nitrogen content higher than 0,6 wt-%, the higher end of the BAT-AEL range is 380 mg/Nm3.","LCP (2017)\n2017/1668","5.1.3",66,66]
[828,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Boilers","Existing","Mixture of gases and liquids","Unspecified ",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO emissions to air from the combustion of process fuels from the chemical industry, BAT is to use one or a combination of the techniques given below: (i) Low-NOX burners (LNB); (ii) Air staging; (iii) Fuel staging; (iv) Flue-gas recirculation; (v) Water/steam addition; (vi) Fuel choice; (vii) Advanced control system; (viii) Selective non-catalytic reduction (SNCR); (ix) Selective catalytic reduction (SCR)","mg/Nm3",100,"330","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ","For plants operated < 500 h/yr, these levels are indicative. \n\nFor existing plants of ≤ 500 MWth put into operation no later than 27 November 2003 using liquid fuels with a nitrogen content higher than 0,6 wt-%, the higher end of the BAT-AEL range is 380 mg/Nm3.","LCP (2017)\n2017/1670","5.1.3",66,66]
[797,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Boilers","Existing","Natural gas ","Unspecified ",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",50,"100","Green","Continuous ",0,0,0.15,"Yearly","Optimising the functioning of an existing technique to reduce NOX emissions further may lead to levels of CO emissions at the higher end of the indicative range for CO emissions given after this table.\n\nThese BAT-AELs do not apply to plants operated < 1 500 h/yr.","LCP (2017)\n2017/1639","4.1.2",56,56]
[799,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Boilers","Existing","Natural gas ","Unspecified ",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",85,"110","Green","Continuous ",0,0,0.15,"Daily average or average over sampling period ","For plants operated < 500 h/yr, these levels are indicative.","LCP (2017)\n2017/1641","4.1.2",56,56]
[829,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Boilers","New","Gases only ","Unspecified ",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO emissions to air from the combustion of process fuels from the chemical industry, BAT is to use one or a combination of the techniques given below: (i) Low-NOX burners (LNB); (ii) Air staging; (iii) Fuel staging; (iv) Flue-gas recirculation; (v) Water/steam addition; (vi) Fuel choice; (vii) Advanced control system; (viii) Selective non-catalytic reduction (SNCR); (ix) Selective catalytic reduction (SCR)","mg/Nm3",20,"80","Green","Continuous ",0,0,0.03,"Yearly",0,"LCP (2017)\n2017/1671","5.1.3",66,66]
[831,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Boilers","New","Gases only ","Unspecified ",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO emissions to air from the combustion of process fuels from the chemical industry, BAT is to use one or a combination of the techniques given below: (i) Low-NOX burners (LNB); (ii) Air staging; (iii) Fuel staging; (iv) Flue-gas recirculation; (v) Water/steam addition; (vi) Fuel choice; (vii) Advanced control system; (viii) Selective non-catalytic reduction (SNCR); (ix) Selective catalytic reduction (SCR)","mg/Nm3",30,"100","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ",0,"LCP (2017)\n2017/1673","5.1.3",66,66]
[737,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Boilers","New","HFO and/or gas oil in boilers","< 100 MWth",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Air staging; (ii) Fuel staging; (iii) Flue-gas recirculation; (iv) Low-NOX burners (LNB); (v) Water/steam addition; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR); (viii) Advanced control systeml (ix) Fuel choice","mg/Nm3",75,"200","Green","Continuous ",0,0,0.03,"Yearly",0,"LCP (2017)\n2017/1579","3.1.2",42,42]
[741,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Boilers","New","HFO and/or gas oil in boilers","≥ 100 MWth",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Air staging; (ii) Fuel staging; (iii) Flue-gas recirculation; (iv) Low-NOX burners (LNB); (v) Water/steam addition; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR); (viii) Advanced control systeml (ix) Fuel choice","mg/Nm3",45,"75","Green","Continuous ",0,0,0.03,"Yearly",0,"LCP (2017)\n2017/1583","3.1.2",42,42]
[825,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Boilers","New","Mixture of gases and liquids","Unspecified ",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO emissions to air from the combustion of process fuels from the chemical industry, BAT is to use one or a combination of the techniques given below: (i) Low-NOX burners (LNB); (ii) Air staging; (iii) Fuel staging; (iv) Flue-gas recirculation; (v) Water/steam addition; (vi) Fuel choice; (vii) Advanced control system; (viii) Selective non-catalytic reduction (SNCR); (ix) Selective catalytic reduction (SCR)","mg/Nm3",30,"85","Green","Continuous ",0,0,0.03,"Yearly",0,"LCP (2017)\n2017/1667","5.1.3",66,66]
[827,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Boilers","New","Mixture of gases and liquids","Unspecified ",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO emissions to air from the combustion of process fuels from the chemical industry, BAT is to use one or a combination of the techniques given below: (i) Low-NOX burners (LNB); (ii) Air staging; (iii) Fuel staging; (iv) Flue-gas recirculation; (v) Water/steam addition; (vi) Fuel choice; (vii) Advanced control system; (viii) Selective non-catalytic reduction (SNCR); (ix) Selective catalytic reduction (SCR)","mg/Nm3",50,"110","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ",0,"LCP (2017)\n2017/1669","5.1.3",66,66]
[796,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Boilers","New","Natural gas ","Unspecified ",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",10,"60","Green","Continuous ",0,0,0.15,"Yearly","Optimising the functioning of an existing technique to reduce NOX emissions further may lead to levels of CO emissions at the higher end of the indicative range for CO emissions given after this table.","LCP (2017)\n2017/1638","4.1.2",56,56]
[798,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Boilers","New","Natural gas ","Unspecified ",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",30,"85","Green","Continuous ",0,0,0.15,"Daily average or average over sampling period ",0,"LCP (2017)\n2017/1640","4.1.2",56,56]
[739,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Boilers","New ","HFO and/or gas oil in boilers","< 100 MWth",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Air staging; (ii) Fuel staging; (iii) Flue-gas recirculation; (iv) Low-NOX burners (LNB); (v) Water/steam addition; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR); (viii) Advanced control systeml (ix) Fuel choice","mg/Nm3",100,"215","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ",0,"LCP (2017)\n2017/1581","3.1.2",42,42]
[743,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Boilers","New ","HFO and/or gas oil in boilers","≥ 100 MWth",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Air staging; (ii) Fuel staging; (iii) Flue-gas recirculation; (iv) Low-NOX burners (LNB); (v) Water/steam addition; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR); (viii) Advanced control systeml (ix) Fuel choice","mg/Nm3",85,"100","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ","The higher end of the BAT-AEL range is 145 mg/Nm3 for plants of 100–300 MWth and plants of ≥ 300 MWth that were put into operation no later than 7 January 2014.","LCP (2017)\n2017/1585","3.1.2",42,42]
[813,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"CCGT","Existing","100% iron and steel process gases ","Unspecified ",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of iron and steel process gases in CCGTs, BAT is to use one or a combination of the techniques given below: (i) Process gas management system; (ii) Advanced control system; (iii) Water/steam addition; (iv) Dry low-NOX burners(DLN); (v) Low-NOX burners (LNB); (vi) Selective catalytic reduction (SCR)","mg/Nm3",20,"50","Green","Continuous ",0,0,0.15,"Yearly","Plants combusting a mixture of gases with an equivalent LHV of > 20 MJ/Nm3 are expected to emit at the higher end of the BAT-AEL ranges.\n\nThe lower end of the BAT-AEL range can be achieved when using SCR.\n\nFor plants operated < 1 500 h/yr, these BAT AELs do not apply.","LCP (2017)\n2017/1655","4.2.2",60,60]
[814,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"CCGT","Existing","100% iron and steel process gases ","Unspecified ",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of iron and steel process gases in CCGTs, BAT is to use one or a combination of the techniques given below: (i) Process gas management system; (ii) Advanced control system; (iii) Water/steam addition; (iv) Dry low-NOX burners(DLN); (v) Low-NOX burners (LNB); (vi) Selective catalytic reduction (SCR)","mg/Nm3",30,"55","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period ","Plants combusting a mixture of gases with an equivalent LHV of > 20 MJ/Nm3 are expected to emit at the higher end of the BAT-AEL ranges.\n\nFor plants operated < 500 h/yr, these levels are indicative.\n\nIn the case of plants put into operation no later than 7 January 2014, the higher end of the BAT-AEL range is 70 mg/Nm3.","LCP (2017)\n2017/1656","4.2.2",60,60]
[811,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"CCGT","New","100% iron and steel process gases ","Unspecified ",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of iron and steel process gases in CCGTs, BAT is to use one or a combination of the techniques given below: (i) Process gas management system; (ii) Advanced control system; (iii) Water/steam addition; (iv) Dry low-NOX burners(DLN); (v) Low-NOX burners (LNB); (vi) Selective catalytic reduction (SCR)","mg/Nm3",20,"35","Green","Continuous ",0,0,0.15,"Yearly","Plants combusting a mixture of gases with an equivalent LHV of > 20 MJ/Nm3 are expected to emit at the higher end of the BAT-AEL ranges.","LCP (2017)\n2017/1653","4.2.2",60,60]
[812,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"CCGT","New","100% iron and steel process gases ","Unspecified ",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of iron and steel process gases in CCGTs, BAT is to use one or a combination of the techniques given below: (i) Process gas management system; (ii) Advanced control system; (iii) Water/steam addition; (iv) Dry low-NOX burners(DLN); (v) Low-NOX burners (LNB); (vi) Selective catalytic reduction (SCR)","mg/Nm3",30,"50","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period ","Plants combusting a mixture of gases with an equivalent LHV of > 20 MJ/Nm3 are expected to emit at the higher end of the BAT-AEL ranges.","LCP (2017)\n2017/1654","4.2.2",60,60]
[782,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"CCGT","New","Natural gas ","≥ 50 MWth",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",10,"30","Green","Continuous ",0,0,0.15,"Yearly","These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines\n\nIn the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective.\n\nThese BAT-AELs do not apply to existing plants operated < 1 500 h/yr.\n\nOptimising the functioning of an existing technique to reduce NOX emissions further may lead to levels of CO emissions at the higher end of the indicative range for CO emissions given after this table.\n\nThese BAT-AELs do not apply to existing turbines for mechanical drive applications or to plants operated < 500 h/yr.\n\nFor plants with a net electrical efficiency (EE) greater than 55 %, a correction factor may be applied to the higher end of the BAT-AEL range, corresponding to [higher end] × EE/55, where EE is the net electrical efficiency of the plant determined at ISO baseload conditions.","LCP (2017)\n2017/1624","4.1.2",54,54]
[783,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"CCGT","New","Natural gas ","≥ 50 MWth",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",15,"40","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period ","These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines\n\nIn the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective.","LCP (2017)\n2017/1625","4.1.2",54,54]
[784,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"CCGT with a net total fuel utilisation of < 75 %","Existing","Natural gas ","≥ 600 MWth",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",10,"40","Green","Continuous ",0,0,0.15,"Yearly","These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines\n\nIn the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective.\n\nThese BAT-AELs do not apply to existing plants operated < 1 500 h/yr.\n\nOptimising the functioning of an existing technique to reduce NOX emissions further may lead to levels of CO emissions at the higher end of the indicative range for CO emissions given after this table.\n\nThese BAT-AELs do not apply to existing turbines for mechanical drive applications or to plants operated < 500 h/yr.\n\nFor plants with a net electrical efficiency (EE) greater than 55 %, a correction factor may be applied to the higher end of the BAT-AEL range, corresponding to [higher end] × EE/55, where EE is the net electrical efficiency of the plant determined at ISO baseload conditions.","LCP (2017)\n2017/1626","4.1.2",54,54]
[785,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"CCGT with a net total fuel utilisation of < 75 %","Existing","Natural gas ","≥ 600 MWth",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",18,"50","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period ","These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines\n\nIn the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective.\n\nThese BAT-AELs do not apply to existing turbines for mechanical drive applications or to plants operated < 500 h/yr.\n\nFor plants with a net electrical efficiency (EE) greater than 55 %, a correction factor may be applied to the higher end of the BAT-AEL range, corresponding to [higher end] × EE/55, where EE is the net electrical efficiency of the plant determined at ISO baseload conditions.","LCP (2017)\n2017/1627","4.1.2",54,54]
[786,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"CCGT with a net total fuel utilisation of ≥ 75 %","Existing","Natural gas ","≥ 600 MWth",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",10,"50","Green","Continuous ",0,0,0.15,"Yearly","These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines\n\nIn the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective.\n\nThese BAT-AELs do not apply to existing plants operated < 1 500 h/yr.\n\nOptimising the functioning of an existing technique to reduce NOX emissions further may lead to levels of CO emissions at the higher end of the indicative range for CO emissions given after this table.\n\nThese BAT-AELs do not apply to existing turbines for mechanical drive applications or to plants operated < 500 h/yr.\n\nFor plants with a net electrical efficiency (EE) greater than 55 %, a correction factor may be applied to the higher end of the BAT-AEL range, corresponding to [higher end] × EE/55, where EE is the net electrical efficiency of the plant determined at ISO baseload conditions.","LCP (2017)\n2017/1628","4.1.2",54,54]
[787,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"CCGT with a net total fuel utilisation of ≥ 75 %","Existing","Natural gas ","≥ 600 MWth",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",18,"55","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period ","These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines\n\nIn the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective.\n\nThese BAT-AELs do not apply to existing turbines for mechanical drive applications or to plants operated < 500 h/yr.\n\nFor plants with a net electrical efficiency (EE) greater than 55 %, a correction factor may be applied to the higher end of the BAT-AEL range, corresponding to [higher end] × EE/55, where EE is the net electrical efficiency of the plant determined at ISO baseload conditions.\n\nFor existing plants put into operation no later than 7 January 2014, the higher end of the BAT-AEL range is 65 mg/Nm3.","LCP (2017)\n2017/1629","4.1.2",54,54]
[630,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Coal-fired PC boiler","Existing","Coal and/or lignite ","≥ 300 MWth",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Combination of other primary techniques for NOX reduction (e.g. air staging, fuel staging, flue-gas recirculation, low- NOX burners (LNB)); (iii) Selective non- catalytic reduction (SNCR); (iv) Selective catalytic reduction (SCR); (v) Combined techniques for NOX and SOX reduction","mg/Nm3",85,"165","Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ","In the case of plants put into operation no later than 7 January 2014, the higher end of the range is 200 mg/Nm3 for plants operated ≥ 1 500 h/yr, and 220 mg/Nm3 for plants operated < 1 500 h/yr.","LCP (2017)\n2017/1472","2.1.3",30,30]
[628,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Coal-fired PC boiler","Existing","Coal and/or lignite ","≥ 300 MWth",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Combination of other primary techniques for NOX reduction (e.g. air staging, fuel staging, flue-gas recirculation, low- NOX burners (LNB)); (iii) Selective non- catalytic reduction (SNCR); (iv) Selective catalytic reduction (SCR); (v) Combined techniques for NOX and SOX reduction","mg/Nm3",65,150,"Green","Continuous ",0,0,0.06,"Yearly",0,"LCP (2017)\n2017/1470","2.1.3",30,30]
[627,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Coal-fired PC boiler","New","Coal and/or lignite ","≥ 300 MWth",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Combination of other primary techniques for NOX reduction (e.g. air staging, fuel staging, flue-gas recirculation, low- NOX burners (LNB)); (iii) Selective non- catalytic reduction (SNCR); (iv) Selective catalytic reduction (SCR); (v) Combined techniques for NOX and SOX reduction","mg/Nm3",65,85,"Green","Continuous ",0,0,0.06,"Yearly",0,"LCP (2017)\n2017/1469","2.1.3",30,30]
[629,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Coal-fired PC boiler","New","Coal and/or lignite ","≥ 300 MWth",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Combination of other primary techniques for NOX reduction (e.g. air staging, fuel staging, flue-gas recirculation, low- NOX burners (LNB)); (iii) Selective non- catalytic reduction (SNCR); (iv) Selective catalytic reduction (SCR); (v) Combined techniques for NOX and SOX reduction","mg/Nm3",80,125,"Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ",0,"LCP (2017)\n2017/1471","2.1.3",30,30]
[773,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Dual fuel gas turbines ","Unspecified ","Gas oil ","Unspecified ",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of gas oil in gas turbines, BAT is to use one or a combination of the techniques given below: (i) Water/steam addition; (ii) Low-NOX burners (LNB); (iii) Selective catalytic reduction (SCR)","mg/Nm3",145,"250","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period.","The emission level for NOX emissions to air from the combustion of gas oil in dual fuel gas turbines for emergency use operated < 500 h/yr","LCP (2017)\n2017/1615","3.3.2",50,50]
[801,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Engine","Existing","Natural gas ","Unspecified ",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",20,"100","Green","Continuous ",0,0,0.15,"Yearly","Optimising the functioning of an existing technique to reduce NOX emissions further may lead to levels of CO emissions at the higher end of the indicative range for CO emissions given after this table.\n\nThese BAT-AELs do not apply to plants operated < 1 500 h/yr.","LCP (2017)\n2017/1643","4.1.2",56,56]
[803,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Engine","Existing","Natural gas ","Unspecified ",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",55,"110","Green","Continuous ",0,0,0.15,"Daily average or average over sampling period ","For plants operated < 500 h/yr, these levels are indicative.\n\nIn the case of engines for emergency use operated < 500 h/yr that could not apply the lean-burn concept or use SCR, the higher end of the indicative range is 175 mg/Nm3.","LCP (2017)\n2017/1645","4.1.2",56,56]
[800,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Engine","New","Natural gas ","Unspecified ",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",20,"75","Green","Continuous ",0,0,0.15,"Yearly","Optimising the functioning of an existing technique to reduce NOX emissions further may lead to levels of CO emissions at the higher end of the indicative range for CO emissions given after this table.","LCP (2017)\n2017/1642","4.1.2",56,56]
[802,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Engine","New","Natural gas ","Unspecified ",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",55,"85","Green","Continuous ",0,0,0.15,"Daily average or average over sampling period ",0,"LCP (2017)\n2017/1644","4.1.2",56,56]
[626,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"FBC boiler combusting coal and/or lignite and lignite-fired PC boiler","Existing","Coal and/or lignite ","≥ 300 MWth",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Combination of other primary techniques for NOX reduction (e.g. air staging, fuel staging, flue-gas recirculation, low- NOX burners (LNB)); (iii) Selective non- catalytic reduction (SNCR); (iv) Selective catalytic reduction (SCR); (v) Combined techniques for NOX and SOX reduction","mg/Nm3",140,165,"Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ","The higher end of the range is 220 mg/Nm3 for FBC boilers put into operation no later than 7 January 2014 and for lignite-fired PC boilers.","LCP (2017)\n2017/1468","2.1.3",30,30]
[624,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"FBC boiler combusting coal and/or lignite and lignite-fired PC boiler","Existing","Coal and/or lignite ","≥ 300 MWth",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Combination of other primary techniques for NOX reduction (e.g. air staging, fuel staging, flue-gas recirculation, low- NOX burners (LNB)); (iii) Selective non- catalytic reduction (SNCR); (iv) Selective catalytic reduction (SCR); (v) Combined techniques for NOX and SOX reduction","mg/Nm3",85,"150","Green","Continuous ",0,0,0.06,"Yearly","The lower end of the range is considered achievable when using SCR.\n\nThe higher end of the range is 175 mg/Nm3 for FBC boilers put into operation no later than 7 January 2014 and for lignite-fired PC boilers.","LCP (2017)\n2017/1466","2.1.3",30,30]
[623,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"FBC boiler combusting coal and/or lignite and lignite-fired PC boiler","New","Coal and/or lignite ","≥ 300 MWth",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Combination of other primary techniques for NOX reduction (e.g. air staging, fuel staging, flue-gas recirculation, low- NOX burners (LNB)); (iii) Selective non- catalytic reduction (SNCR); (iv) Selective catalytic reduction (SCR); (v) Combined techniques for NOX and SOX reduction","mg/Nm3",50,85,"Green","Continuous ",0,0,0.06,"Yearly",0,"LCP (2017)\n2017/1465","2.1.3",30,30]
[625,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"FBC boiler combusting coal and/or lignite and lignite-fired PC boiler","New","Coal and/or lignite ","≥ 300 MWth",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Combination of other primary techniques for NOX reduction (e.g. air staging, fuel staging, flue-gas recirculation, low- NOX burners (LNB)); (iii) Selective non- catalytic reduction (SNCR); (iv) Selective catalytic reduction (SCR); (v) Combined techniques for NOX and SOX reduction","mg/Nm3",80,125,"Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ",0,"LCP (2017)\n2017/1467","2.1.3",30,30]
[762,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Fired engines ","Existing","HFO and/or gas oil in reciprocating engines","≥ 50 MWth",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of HFO and/or gas oil in reciprocating engines, BAT is to use one or a combination of the techniques given below: (i) Low-NOX combustion concept in diesel engines; (ii) Exhaust-gas recirculation (EGR); (iii) Water/steam addition; (iv) Selective catalytic reduction (SCR)","mg/Nm3",152,"625","Green","Continuous ",0,0,0.15,"Yearly","These BAT-AELs do not apply to plants operated < 1 500 h/yr or to plants that cannot be fitted with secondary abatement techniques.","LCP (2017)\n2017/1604","3.2.2",47,47]
[764,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Fired engines ","Existing","HFO and/or gas oil in reciprocating engines","≥ 50 MWth",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of HFO and/or gas oil in reciprocating engines, BAT is to use one or a combination of the techniques given below: (i) Low-NOX combustion concept in diesel engines; (ii) Exhaust-gas recirculation (EGR); (iii) Water/steam addition; (iv) Selective catalytic reduction (SCR)","mg/Nm3",150,"750","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period ","The BAT-AEL range is 1 150–1 900 mg/Nm3 for plants operated < 1 500 h/yr and for plants that cannot be fitted with secondary abatement techniques.\n\nFor plants operated < 500 h/yr, these levels are indicative.","LCP (2017)\n2017/1606","3.2.2",47,47]
[761,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Fired engines ","New","HFO and/or gas oil in reciprocating engines","≥ 50 MWth",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of HFO and/or gas oil in reciprocating engines, BAT is to use one or a combination of the techniques given below: (i) Low-NOX combustion concept in diesel engines; (ii) Exhaust-gas recirculation (EGR); (iii) Water/steam addition; (iv) Selective catalytic reduction (SCR)","mg/Nm3",115,"190","Green","Continuous ",0,0,0.15,"Yearly","For plants including units of < 20 MWth combusting HFO, the higher end of the BAT-AEL range applying to those units is 225 mg/Nm3.","LCP (2017)\n2017/1603","3.2.2",47,47]
[763,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Fired engines ","New","HFO and/or gas oil in reciprocating engines","≥ 50 MWth",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of HFO and/or gas oil in reciprocating engines, BAT is to use one or a combination of the techniques given below: (i) Low-NOX combustion concept in diesel engines; (ii) Exhaust-gas recirculation (EGR); (iii) Water/steam addition; (iv) Selective catalytic reduction (SCR)","mg/Nm3",145,"300","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period ",0,"LCP (2017)\n2017/1605","3.2.2",47,47]
[795,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Gas turbine for mechanical drive applications — All but plants operated < 500 h/yr","Existing","Natural gas ","≥ 50 MWth",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",25,"55","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period ","These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines\n\nIn the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective.\n\nFor existing plants put into operation no later than 7 January 2014, the higher end of the BAT-AEL range is 65 mg/Nm3.\n\nFor existing plants put into operation no later than 7 January 2014, the higher end of the BAT-AEL range is 65 mg/Nm3.","LCP (2017)\n2017/1637","4.1.2",54,54]
[794,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Gas turbine for mechanical drive applications — All but plants operated < 500 h/yr","Existing","Natural gas ","≥ 50 MWth",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",15,"50","Green","Continuous ",0,0,0.15,"Yearly","These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines\n\nIn the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective.\n\nThese BAT-AELs do not apply to existing plants operated < 1 500 h/yr.\n\nOptimising the functioning of an existing technique to reduce NOX emissions further may lead to levels of CO emissions at the higher end of the indicative range for CO emissions given after this table.\n\nFor existing plants put into operation no later than 7 January 2014, the higher end of the BAT-AEL range is 60 mg/Nm3.\n","LCP (2017)\n2017/1636","4.1.2",54,54]
[792,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Gas turbine put into operation no later than 27 November 2003, or existing gas turbine for emergency use and operated < 500 h/yr","Existing","Natural gas ","≥ 50 MWth",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3","N/A","N/A","Green","Continuous ",0,0,0.15,"Yearly","These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines\n\nIn the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective.\n\nThese BAT-AELs do not apply to existing plants operated < 1 500 h/yr.\n\nOptimising the functioning of an existing technique to reduce NOX emissions further may lead to levels of CO emissions at the higher end of the indicative range for CO emissions given after this table.","LCP (2017)\n2017/1634","4.1.2",54,54]
[793,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Gas turbine put into operation no later than 27 November 2003, or existing gas turbine for emergency use and operated < 500 h/yr","Existing","Natural gas ","≥ 50 MWth",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",60,"140","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period ","These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines\n\nIn the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective.\n\nThe lower end of the BAT-AEL range for NOX can be achieved with DLN burners.\n\nThese levels are indicative.","LCP (2017)\n2017/1635","4.1.2",54,54]
[863,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"IGCC","Existing","Unspecified","≥ 100 MWth",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent and/or reduce NOX emissions to air while limiting CO emissions to air from IGCC plants, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Water/steam addition; (iii) Dry low-NOX burners (DLN); (iv) Syngas dilution with waste nitrogen from the air supply unit (ASU); (v) Selective catalytic reduction (SCR)","mg/Nm3",12,"45","Green","Continuous",0,0,0.15,"Yearly","As an indication, the yearly average CO emission levels for existing plants operated ≥ 1 500 h/yr and for new plants will generally be < 5–30 mg/Nm3.","LCP (2017)\n2017/1705","7.1.2",75,75]
[865,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"IGCC","Existing","Unspecified","≥ 100 MWth",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent and/or reduce NOX emissions to air while limiting CO emissions to air from IGCC plants, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Water/steam addition; (iii) Dry low-NOX burners (DLN); (iv) Syngas dilution with waste nitrogen from the air supply unit (ASU); (v) Selective catalytic reduction (SCR)","mg/Nm3",1,"60","Green","Continuous",0,0,0.15,"Daily average or average over the sampling period ","As an indication, the yearly average CO emission levels for existing plants operated ≥ 1 500 h/yr and for new plants will generally be < 5–30 mg/Nm3.","LCP (2017)\n2017/1707","7.1.2",75,75]
[862,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"IGCC","New","Unspecified","≥ 100 MWth",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent and/or reduce NOX emissions to air while limiting CO emissions to air from IGCC plants, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Water/steam addition; (iii) Dry low-NOX burners (DLN); (iv) Syngas dilution with waste nitrogen from the air supply unit (ASU); (v) Selective catalytic reduction (SCR)","mg/Nm3",10,"25","Green","Continuous",0,0,0.15,"Yearly","As an indication, the yearly average CO emission levels for existing plants operated ≥ 1 500 h/yr and for new plants will generally be < 5–30 mg/Nm3.","LCP (2017)\n2017/1704","7.1.2",75,75]
[864,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"IGCC","New","Unspecified","≥ 100 MWth",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent and/or reduce NOX emissions to air while limiting CO emissions to air from IGCC plants, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Water/steam addition; (iii) Dry low-NOX burners (DLN); (iv) Syngas dilution with waste nitrogen from the air supply unit (ASU); (v) Selective catalytic reduction (SCR)","mg/Nm3",1,"35","Green","Continuous",0,0,0.15,"Daily average or average over the sampling period ","As an indication, the yearly average CO emission levels for existing plants operated ≥ 1 500 h/yr and for new plants will generally be < 5–30 mg/Nm3.","LCP (2017)\n2017/1706","7.1.2",75,75]
[778,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"OCGT","New","Natural gas ","≥ 50 MWth",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",15,"35","Green","Continuous ",0,0,0.15,"Yearly","These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines\n\nIn the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective.\n\nThese BAT-AELs do not apply to existing plants operated < 1 500 h/yr.\n\nOptimising the functioning of an existing technique to reduce NOX emissions further may lead to levels of CO emissions at the higher end of the indicative range for CO emissions given after this table.\n\nThese BAT-AELs do not apply to existing turbines for mechanical drive applications or to plants operated < 500 h/yr.\n\nFor plants with a net electrical efficiency (EE) greater than 39 %, a correction factor may be applied to the higher end of the range, corresponding to [higher end] × EE/39, where EE is the net electrical energy efficiency or net mechanical energy efficiency of the plant determined at ISO baseload conditions.","LCP (2017)\n2017/1620","4.1.2",54,54]
[779,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"OCGT","New","Natural gas ","≥ 50 MWth",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",25,"50","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period ","These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines\n\nIn the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective.\n\nThese BAT-AELs do not apply to existing turbines for mechanical drive applications or to plants operated < 500 h/yr.\n\nFor plants with a net electrical efficiency (EE) greater than 39 %, a correction factor may be applied to the higher end of the range, corresponding to [higher end] × EE/39, where EE is the net electrical energy efficiency or net mechanical energy efficiency of the plant determined at ISO baseload conditions.","LCP (2017)\n2017/1621","4.1.2",54,54]
[780,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"OCGT (excluding turbines for mechanical drive applications) — All but plants operated < 500 h/yr","Existing","Natural gas ","≥ 50 MWth",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",15,"50","Green","Continuous ",0,0,0.15,"Yearly","These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines\n\nIn the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective.\n\nThese BAT-AELs do not apply to existing plants operated < 1 500 h/yr.\n\nOptimising the functioning of an existing technique to reduce NOX emissions further may lead to levels of CO emissions at the higher end of the indicative range for CO emissions given after this table.\n\nThese BAT-AELs do not apply to existing turbines for mechanical drive applications or to plants operated < 500 h/yr.\n\nFor plants with a net electrical efficiency (EE) greater than 39 %, a correction factor may be applied to the higher end of the range, corresponding to [higher end] × EE/39, where EE is the net electrical energy efficiency or net mechanical energy efficiency of the plant determined at ISO baseload conditions.","LCP (2017)\n2017/1622","4.1.2",54,54]
[781,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"OCGT (excluding turbines for mechanical drive applications) — All but plants operated < 500 h/yr","Existing","Natural gas ","≥ 50 MWth",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",25,"55","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period ","These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines\n\nIn the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective.\n\nThe higher end of the range is 80 mg/Nm3 in the case of plants which were put into operation no later than 27 November 2003 and are operated between 500 h/yr and 1 500 h/yr.\n\n\nThese BAT-AELs do not apply to existing turbines for mechanical drive applications or to plants operated < 500 h/yr.\n\nFor plants with a net electrical efficiency (EE) greater than 39 %, a correction factor may be applied to the higher end of the range, corresponding to [higher end] × EE/39, where EE is the net electrical energy efficiency or net mechanical e","LCP (2017)\n2017/1623","4.1.2",54,54]
[824,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Open-cycle gas turbines on offshore platforms","Existing","Gaseous fuels ","Unspecified ",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of gaseous and/or liquid fuels on offshore platforms, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Dry low-NOX burners (DLN); (iii) Lean-burn concept; (iv) Low-NOX burners (LNB)","mg/Nm3",50,"350","Green","Continuous ",0,0,0.03,"Average over the sampling period","These BAT-AELs are based on > 70 % of baseload power available on the day.\n\nThis includes single fuel and dual fuel gas turbines.\n\nThe lower end of the BAT-AEL range can be achieved with DLN burners.","LCP (2017)\n2017/1666",4.3,64,64]
[823,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Open-cycle gas turbines on offshore platforms","New","Gaseous fuels ","Unspecified ",0,"Emissions to air ","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of gaseous and/or liquid fuels on offshore platforms, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Dry low-NOX burners (DLN); (iii) Lean-burn concept; (iv) Low-NOX burners (LNB)","mg/Nm3",15,"50","Green","Continuous ",0,0,0.03,"Average over the sampling period","These BAT-AELs are based on > 70 % of baseload power available on the day. \n\nThis includes single fuel and dual fuel gas turbines.\n\nThe higher end of the BAT-AEL range is 250 mg/Nm3 if DLN burners are not applicable.","LCP (2017)\n2017/1665",4.3,64,64]
[859,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Biomass-, peat-, coal- and/or lignite-fired combustion plant","Unspecified ","Co-incineration of waste with biomass, peat, coal and/or lignite","Unspecified ",0,"Emissions to air ","Air","PCDD/F","PCDD/F","In order to reduce emissions of volatile organic compounds and polychlorinated dibenzo-dioxins and -furans to air from the co-incineration of waste with biomass, peat, coal and/or lignite, BAT is to use a combination of the techniques given in BAT 6, BAT 26 and below: (i) Activated carbon injection; (ii) Rapid quenching using wet scrubbing/flue-gas condenser; (iii) Selective catalytic reduction (SCR)","ng I-TEQ/Nm3",0.01,"0.03","Green","Once every 6 months ",0,0,0.06,"Average over the sampling period",0,"LCP (2017)\n2017/1701","6.1.7",73,73]
[851,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Boilers","Unspecified ","100 % process fuels from the chemical industry","Unspecified ",0,"Emissions to air ","Air","PCDD/F","PCDD/F","In order to reduce emissions to air of volatile organic compounds and polychlorinated dibenzo- dioxins and -furans from the combustion of process fuels from the chemical industry in boilers, BAT is to use one or a combination of the techniques given in BAT 6 and below: (i) Activated carbon injection; (ii) Rapid quenching using wet scrubbing/flue-gas condenser; (iii) Selective catalytic reduction (SCR)","ng I-TEQ/Nm3",1.2E-2,"0.036","Green","Once every 6 months",0,0,0.03,"Average over the sampling period","These BAT-AELs only apply to plants using fuels derived from chemical processes involving chlorinated substances.","LCP (2017)\n2017/1693","5.1.6",69,69]
[857,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Unspecified","Unspecified ","Co-incineration of waste with biomass and/or peat","Unspecified ",0,"Emissions to air ","Air","Sb + As + Pb + Cr + Co + Cu + Mn + Ni + V","Sb + As + Pb + Cr + Co + Cu + Mn + Ni + V","In order to reduce dust and particulate-bound metal emissions to air from the co-incineration of waste with biomass and/or peat, BAT is to use one or a combination of the techniques given in BAT 26.","mg/Nm3",7.4999999999999997E-2,"0.3","Amber",0,0,0,0.06,"Average of samples obtained during one year",0,"LCP (2017)\n2017/1699","6.1.5",72,72]
[853,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Unspecified","Unspecified ","Co-incineration of waste with coal and/or lignite","< 300 MWth ",0,"Emissions to air ","Air","Sb + As + Pb + Cr + Co + Cu + Mn + Ni + V","Sb + As + Pb + Cr + Co + Cu + Mn + Ni + V","In order to reduce dust and particulate-bound metal emissions to air from the co-incineration of waste with coal and/or lignite, BAT is to use one or a combination of the techniques given in BAT 22.","mg/Nm3",5.0000000000000001E-3,"0.5","Green","Once every 6 months",0,0,0.06,"Average over the sampling period",0,"LCP (2017)\n2017/1695","6.1.5",72,72]
[855,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Unspecified","Unspecified ","Co-incineration of waste with coal and/or lignite","≥ 300 MWth",0,"Emissions to air ","Air","Sb + As + Pb + Cr + Co + Cu + Mn + Ni + V","Sb + As + Pb + Cr + Co + Cu + Mn + Ni + V","In order to reduce dust and particulate-bound metal emissions to air from the co-incineration of waste with coal and/or lignite, BAT is to use one or a combination of the techniques given in BAT 22.","mg/Nm3",5.0000000000000001E-3,"0.2","Green","Once every 3 months ",0,0,0.06,"Average of samples obtained during one year",0,"LCP (2017)\n2017/1697","6.1.5",72,72]
[635,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","Existing","Coal and/or lignite ","< 100 MWth",0,"Emissions to air ","Air","SO2","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD; (viii) Combined techniques for NOX and SOX reduction; (ix) Replacement or removal of the gas- gas heater located downstream of the wet FGD; (x) Fuel choice","mg/Nm3",150,360,"Green","Continuous ",0,0,0.06,"Yearly",0,"LCP (2017)\n2017/1477","2.1.4",32,32]
[639,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","Existing","Coal and/or lignite ","100-300 MWth",0,"Emissions to air ","Air","SO2","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD; (viii) Combined techniques for NOX and SOX reduction; (ix) Replacement or removal of the gas- gas heater located downstream of the wet FGD; (x) Fuel choice","mg/Nm3",95,200,"Green","Continuous ",0,0,0.06,"Yearly",0,"LCP (2017)\n2017/1481","2.1.4",32,32]
[695,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","Existing","Solid biomass and/or peat","< 100 MWth",0,"Emissions to air ","Air","SO2","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3",15,"100","Green","Continuous ",0,0,0.06,"Yearly ","These BAT-AELs do not apply to plants operated < 1 500 h/yr.","LCP (2017)\n2017/1537","2.2.2",38,38]
[697,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","Existing","Solid biomass and/or peat","< 100 MWth",0,"Emissions to air ","Air","SO2","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3",30,"215","Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ","For plants operated < 500 h/yr, these levels are indicative.","LCP (2017)\n2017/1539","2.2.2",38,38]
[703,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","Existing","Solid biomass and/or peat","≥ 300 MWth",0,"Emissions to air ","Air","SO2","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3",10,"50","Green","Continuous ",0,0,0.06,"Yearly ","For existing plants burning fuels where the average sulphur content is 0,1 wt-% (dry) or higher, the higher end of the BAT-AEL range is 100 mg/Nm3.","LCP (2017)\n2017/1545","2.2.2",38,38]
[705,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","Existing","Solid biomass and/or peat","≥ 300 MWth",0,"Emissions to air ","Air","SO2","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3",20,"85","Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ","For existing plants burning fuels where the average sulphur content is 0,1 wt-% (dry) or higher, the higher end of the BAT-AEL range is 165 mg/Nm3, or 215 mg/Nm3 if those plants have been put into operation no later than 7 January 2014 and/or are FBC boilers combusting peat.","LCP (2017)\n2017/1547","2.2.2",38,38]
[699,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","Existing","Solid biomass and/or peat","100-300 MWth",0,"Emissions to air ","Air","SO2","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3",10,"70","Green","Continuous ",0,0,0.06,"Yearly ","For existing plants burning fuels where the average sulphur content is 0,1 wt-% (dry) or higher, the higher end of the BAT-AEL range is 100 mg/Nm3.","LCP (2017)\n2017/1541","2.2.2",38,38]
[701,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","Existing","Solid biomass and/or peat","100-300 MWth",0,"Emissions to air ","Air","SO2","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3",20,"175","Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ","For existing plants burning fuels where the average sulphur content is 0,1 wt-% (dry) or higher, the higher end of the BAT-AEL range is 215 mg/Nm3.","LCP (2017)\n2017/1543","2.2.2",38,38]
[637,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","Existing","Coal and/or lignite ","< 100 MWth",0,"Emissions to air ","Air","SO2","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD; (viii) Combined techniques for NOX and SOX reduction; (ix) Replacement or removal of the gas- gas heater located downstream of the wet FGD; (x) Fuel choice","mg/Nm3",170,400,"Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ","For plants operated < 500 h/yr, these levels are indicative.","LCP (2017)\n2017/1479","2.1.4",32,32]
[641,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","Existing","Coal and/or lignite ","100-300 MWth",0,"Emissions to air ","Air","SO2","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD; (viii) Combined techniques for NOX and SOX reduction; (ix) Replacement or removal of the gas- gas heater located downstream of the wet FGD; (x) Fuel choice","mg/Nm3",135,220,"Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ","In the case of plants put into operation no later than 7 January 2014, the upper end of the BAT-AEL range is 250 mg/Nm3.","LCP (2017)\n2017/1483","2.1.4",32,32]
[634,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","New","Coal and/or lignite ","< 100 MWth",0,"Emissions to air ","Air","SO2","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD; (viii) Combined techniques for NOX and SOX reduction; (ix) Replacement or removal of the gas- gas heater located downstream of the wet FGD; (x) Fuel choice","mg/Nm3",150,200,"Green","Continuous ",0,0,0.06,"Yearly",0,"LCP (2017)\n2017/1476","2.1.4",32,32]
[636,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","New","Coal and/or lignite ","< 100 MWth",0,"Emissions to air ","Air","SO2","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD; (viii) Combined techniques for NOX and SOX reduction; (ix) Replacement or removal of the gas- gas heater located downstream of the wet FGD; (x) Fuel choice","mg/Nm3",170,220,"Green","Continuous ",0,0,0.06,"Daily",0,"LCP (2017)\n2017/1478","2.1.4",32,32]
[638,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","New","Coal and/or lignite ","100-300 MWth",0,"Emissions to air ","Air","SO2","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD; (viii) Combined techniques for NOX and SOX reduction; (ix) Replacement or removal of the gas- gas heater located downstream of the wet FGD; (x) Fuel choice","mg/Nm3",80,150,"Green","Continuous ",0,0,0.06,"Yearly",0,"LCP (2017)\n2017/1480","2.1.4",32,32]
[640,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","New","Coal and/or lignite ","100-300 MWth",0,"Emissions to air ","Air","SO2","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD; (viii) Combined techniques for NOX and SOX reduction; (ix) Replacement or removal of the gas- gas heater located downstream of the wet FGD; (x) Fuel choice","mg/Nm3",135,200,"Green","Continuous ",0,0,0.06,"Daily",0,"LCP (2017)\n2017/1482","2.1.4",32,32]
[694,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","New","Solid biomass and/or peat","< 100 MWth",0,"Emissions to air ","Air","SO2","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3",15,"70","Green","Continuous ",0,0,0.06,"Yearly ",0,"LCP (2017)\n2017/1536","2.2.2",38,38]
[696,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","New","Solid biomass and/or peat","< 100 MWth",0,"Emissions to air ","Air","SO2","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3",30,"175","Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ",0,"LCP (2017)\n2017/1538","2.2.2",38,38]
[702,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","New","Solid biomass and/or peat","≥ 300 MWth",0,"Emissions to air ","Air","SO2","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3",10,"35","Green","Continuous ",0,0,0.06,"Yearly ",0,"LCP (2017)\n2017/1544","2.2.2",38,38]
[704,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","New","Solid biomass and/or peat","≥ 300 MWth",0,"Emissions to air ","Air","SO2","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3",20,"70","Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ",0,"LCP (2017)\n2017/1546","2.2.2",38,38]
[698,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","New","Solid biomass and/or peat","100-300 MWth",0,"Emissions to air ","Air","SO2","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3",10,"50","Green","Continuous ",0,0,0.06,"Yearly ",0,"LCP (2017)\n2017/1540","2.2.2",38,38]
[700,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"All","New","Solid biomass and/or peat","100-300 MWth",0,"Emissions to air ","Air","SO2","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3",20,"85","Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ",0,"LCP (2017)\n2017/1542","2.2.2",38,38]
[815,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Boilers","Unspecified","100% iron and steel process gases ","Unspecified ",0,"Emissions to air ","Air","SO2","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX emissions to air from the combustion of iron and steel process gases, BAT is to use a combination of the techniques given below: (i) Process gas management system and auxiliary fuel choice; (ii) Coke oven gas pretreatment at the iron- and steel-works","mg/Nm3",25,"150","Green","Continuous ",0,0,0.03,"Yearly","For existing plants operated < 1 500 h/yr, these BAT AELs do not apply.","LCP (2017)\n2017/1657","4.2.3",61,61]
[816,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Boilers","Unspecified","100% iron and steel process gases ","Unspecified ",0,"Emissions to air ","Air","SO2","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX emissions to air from the combustion of iron and steel process gases, BAT is to use a combination of the techniques given below: (i) Process gas management system and auxiliary fuel choice; (ii) Coke oven gas pretreatment at the iron- and steel-works","mg/Nm3",50,"200","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ","For existing plants operated < 500 h/yr, these levels are indicative.","LCP (2017)\n2017/1658","4.2.3",61,61]
[834,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Boilers","Existing","100 % process fuels from the chemical industry","Unspecified ",0,"Emissions to air ","Air","SO2","Sulphur Dioxide (24 Hour Mean)","In order to reduce SOX, HCl and HF emissions to air from the combustion of process fuels from the chemical industry in boilers, BAT is to use one or a combination of the techniques given below: (i) Fuel choice; (ii) Boiler sorbent injection (in-furnace or in-bed); (iii) Duct sorbent injection (DSI); (iv) Spray dry absorber (SDA); (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD","mg/Nm3",90,"200","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ","For existing plants operated < 500 h/yr, these levels are indicative.","LCP (2017)\n2017/1676","5.1.4",67,67]
[746,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Boilers","Existing","HFO and/or gas oil in boilers","< 300 MWth ",0,"Emissions to air ","Air","SO2","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Duct sorbent injection (DSI); (ii) Spray dry absorber (SDA); (iii) Flue-gas condenser; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Seawater FGD; (vi) Fuel choice","mg/Nm3",50,"175","Green","Continuous ",0,0,0.03,"Yearly","These BAT-AELs do not apply to plants operated < 1 500 h/yr.","LCP (2017)\n2017/1588",3.13,44,44]
[748,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Boilers","Existing","HFO and/or gas oil in boilers","< 300 MWth ",0,"Emissions to air ","Air","SO2","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Duct sorbent injection (DSI); (ii) Spray dry absorber (SDA); (iii) Flue-gas condenser; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Seawater FGD; (vi) Fuel choice","mg/Nm3",150,"200","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ","For plants operated < 500 h/yr, these levels are indicative.\n\nFor industrial boilers and district heating plants put into operation no later than 27 November 2003 and operated < 1 500 h/yr, the higher end of the BAT-AEL range is 400 mg/Nm3.","LCP (2017)\n2017/1590",3.13,44,44]
[750,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Boilers","Existing","HFO and/or gas oil in boilers","≥ 300 MWth",0,"Emissions to air ","Air","SO2","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Duct sorbent injection (DSI); (ii) Spray dry absorber (SDA); (iii) Flue-gas condenser; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Seawater FGD; (vi) Fuel choice","mg/Nm3",50,"110","Green","Continuous ",0,0,0.03,"Yearly","These BAT-AELs do not apply to plants operated < 1 500 h/yr.","LCP (2017)\n2017/1592",3.13,44,44]
[752,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Boilers","Existing","HFO and/or gas oil in boilers","≥ 300 MWth",0,"Emissions to air ","Air","SO2","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Duct sorbent injection (DSI); (ii) Spray dry absorber (SDA); (iii) Flue-gas condenser; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Seawater FGD; (vi) Fuel choice","mg/Nm3",150,"165","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ","For plants operated < 500 h/yr, these levels are indicative.\n\nFor industrial boilers and district heating plants put into operation no later than 27 November 2003 and operated < 1 500 h/yr, the higher end of the BAT-AEL range is 400 mg/Nm3.","LCP (2017)\n2017/1594",3.13,44,44]
[833,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Boilers","New","100 % process fuels from the chemical industry","Unspecified ",0,"Emissions to air ","Air","SO2","Sulphur Dioxide (24 Hour Mean)","In order to reduce SOX, HCl and HF emissions to air from the combustion of process fuels from the chemical industry in boilers, BAT is to use one or a combination of the techniques given below: (i) Fuel choice; (ii) Boiler sorbent injection (in-furnace or in-bed); (iii) Duct sorbent injection (DSI); (iv) Spray dry absorber (SDA); (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD","mg/Nm3",10,"110","Green","Continuous ",0,0,0.03,"Yearly","For existing plants operated < 1 500 h/yr, these BAT-AELs do not apply.","LCP (2017)\n2017/1675","5.1.4",67,67]
[745,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Boilers","New","HFO and/or gas oil in boilers","< 300 MWth ",0,"Emissions to air ","Air","SO2","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Duct sorbent injection (DSI); (ii) Spray dry absorber (SDA); (iii) Flue-gas condenser; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Seawater FGD; (vi) Fuel choice","mg/Nm3",50,"175","Green","Continuous ",0,0,0.03,"Yearly",0,"LCP (2017)\n2017/1587",3.13,44,44]
[747,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Boilers","New","HFO and/or gas oil in boilers","< 300 MWth ",0,"Emissions to air ","Air","SO2","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Duct sorbent injection (DSI); (ii) Spray dry absorber (SDA); (iii) Flue-gas condenser; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Seawater FGD; (vi) Fuel choice","mg/Nm3",150,"200","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ",0,"LCP (2017)\n2017/1589",3.13,44,44]
[749,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Boilers","New","HFO and/or gas oil in boilers","≥ 300 MWth",0,"Emissions to air ","Air","SO2","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Duct sorbent injection (DSI); (ii) Spray dry absorber (SDA); (iii) Flue-gas condenser; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Seawater FGD; (vi) Fuel choice","mg/Nm3",35,"50","Green","Continuous ",0,0,0.03,"Yearly",0,"LCP (2017)\n2017/1591",3.13,44,44]
[751,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Boilers","New","HFO and/or gas oil in boilers","≥ 300 MWth",0,"Emissions to air ","Air","SO2","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Duct sorbent injection (DSI); (ii) Spray dry absorber (SDA); (iii) Flue-gas condenser; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Seawater FGD; (vi) Fuel choice","mg/Nm3",50,"120","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ",0,"LCP (2017)\n2017/1593",3.13,44,44]
[817,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"CCGT","Unspecified","100% iron and steel process gases ","Unspecified ",0,"Emissions to air ","Air","SO2","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX emissions to air from the combustion of iron and steel process gases, BAT is to use a combination of the techniques given below: (i) Process gas management system and auxiliary fuel choice; (ii) Coke oven gas pretreatment at the iron- and steel-works","mg/Nm3",10,"45","Green","Continuous ",0,0,0.15,"Yearly","For existing plants operated < 1 500 h/yr, these BAT AELs do not apply.","LCP (2017)\n2017/1659","4.2.3",61,61]
[818,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"CCGT","Unspecified","100% iron and steel process gases ","Unspecified ",0,"Emissions to air ","Air","SO2","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX emissions to air from the combustion of iron and steel process gases, BAT is to use a combination of the techniques given below: (i) Process gas management system and auxiliary fuel choice; (ii) Coke oven gas pretreatment at the iron- and steel-works","mg/Nm3",20,"70","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period ","For existing plants operated < 500 h/yr, these levels are indicative.","LCP (2017)\n2017/1660","4.2.3",61,61]
[766,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Fired engines ","Existing","HFO and/or gas oil in reciprocating engines","All sizes",0,"Emissions to air ","Air","SO2","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of HFO and/or gas oil in reciprocating engines, BAT is to use one or a combination of the techniques given below: (i) Fuel choice; (ii) Duct sorbent injection (DSI); (iii) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",100,"200","Green","Continuous ",0,0,0.15,"Yearly","These BAT-AELs do not apply to plants operated < 1 500 h/yr.\n\nThe higher end of the BAT-AEL range is 280 mg/Nm3 if no secondary abatement technique can be applied. This corresponds to a sulphur content of the fuel of 0,5 wt-% (dry).","LCP (2017)\n2017/1608","3.2.3",48,48]
[768,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Fired engines ","Existing","HFO and/or gas oil in reciprocating engines","All sizes",0,"Emissions to air ","Air","SO2","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of HFO and/or gas oil in reciprocating engines, BAT is to use one or a combination of the techniques given below: (i) Fuel choice; (ii) Duct sorbent injection (DSI); (iii) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",105,"235","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period ","For plants operated < 500 h/yr, these levels are indicative.\n\nThe higher end of the BAT-AEL range is 280 mg/Nm3 if no secondary abatement technique can be applied. This corresponds to a sulphur content of the fuel of 0,5 wt-% (dry).","LCP (2017)\n2017/1610","3.2.3",48,48]
[765,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Fired engines ","New","HFO and/or gas oil in reciprocating engines","All sizes",0,"Emissions to air ","Air","SO2","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of HFO and/or gas oil in reciprocating engines, BAT is to use one or a combination of the techniques given below: (i) Fuel choice; (ii) Duct sorbent injection (DSI); (iii) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",45,"100","Green","Continuous ",0,0,0.15,"Yearly",0,"LCP (2017)\n2017/1607","3.2.3",48,48]
[767,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Fired engines ","New","HFO and/or gas oil in reciprocating engines","All sizes",0,"Emissions to air ","Air","SO2","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of HFO and/or gas oil in reciprocating engines, BAT is to use one or a combination of the techniques given below: (i) Fuel choice; (ii) Duct sorbent injection (DSI); (iii) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",60,"110","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period ",0,"LCP (2017)\n2017/1609","3.2.3",48,48]
[647,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Fluidised bed boiler","Existing","Coal and/or lignite ","≥ 300 MWth",0,"Emissions to air ","Air","SO2","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD; (viii) Combined techniques for NOX and SOX reduction; (ix) Replacement or removal of the gas- gas heater located downstream of the wet FGD; (x) Fuel choice","mg/Nm3",20,180,"Green","Continuous ",0,0,0.06,"Yearly","For circulating fluidised bed boilers, the lower end of the range can be achieved by using high-efficiency wet FGD. The higher end of the range can be achieved by using boiler in-bed sorbent injection.","LCP (2017)\n2017/1489","2.1.4",32,32]
[649,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Fluidised bed boiler","Existing ","Coal and/or lignite ","≥ 300 MWth",0,"Emissions to air ","Air","SO2","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD; (viii) Combined techniques for NOX and SOX reduction; (ix) Replacement or removal of the gas- gas heater located downstream of the wet FGD; (x) Fuel choice","mg/Nm3",50,220,"Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ","For circulating fluidised bed boilers, the lower end of the range can be achieved by using high-efficiency wet FGD. The higher end of the range can be achieved by using boiler in-bed sorbent injection.","LCP (2017)\n2017/1491","2.1.4",32,32]
[646,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Fluidised bed boiler","New","Coal and/or lignite ","≥ 300 MWth",0,"Emissions to air ","Air","SO2","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD; (viii) Combined techniques for NOX and SOX reduction; (ix) Replacement or removal of the gas- gas heater located downstream of the wet FGD; (x) Fuel choice","mg/Nm3",20,75,"Green","Continuous ",0,0,0.06,"Yearly","For circulating fluidised bed boilers, the lower end of the range can be achieved by using high-efficiency wet FGD. The higher end of the range can be achieved by using boiler in-bed sorbent injection.","LCP (2017)\n2017/1488","2.1.4",32,32]
[648,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Fluidised bed boiler","New","Coal and/or lignite ","≥ 300 MWth",0,"Emissions to air ","Air","SO2","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD; (viii) Combined techniques for NOX and SOX reduction; (ix) Replacement or removal of the gas- gas heater located downstream of the wet FGD; (x) Fuel choice","mg/Nm3",25,110,"Green","Continuous ",0,0,0.06,"Daily","For circulating fluidised bed boilers, the lower end of the range can be achieved by using high-efficiency wet FGD. The higher end of the range can be achieved by using boiler in-bed sorbent injection.","LCP (2017)\n2017/1490","2.1.4",32,32]
[774,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Gas turbines (including dual fuel turbines) ","New and existing ","Gas oil ","Unspecified ",0,"Emissions to air ","Air","SO2","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX and dust emissions to air from the combustion of gas oil in gas turbines, BAT is to use the technique given below: Fuel choice","mg/Nm3",35,"60","Green","Continuous ",0,0,0.15,"Yearly","These BAT-AELs do not apply to existing plants operated < 1 500 h/yr.","LCP (2017)\n2017/1616","3.3.3",50,50]
[775,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Gas turbines (including dual fuel turbines) ","New and existing ","Gas oil ","Unspecified ",0,"Emissions to air ","Air","SO2","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX and dust emissions to air from the combustion of gas oil in gas turbines, BAT is to use the technique given below: Fuel choice","mg/Nm3",50,"66","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period ","For existing plants operated < 500 h/yr, these levels are indicative.","LCP (2017)\n2017/1617","3.3.3",50,50]
[776,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Gas turbines (including dual fuel turbines) ","New and existing ","Gas oil ","Unspecified ",0,"Emissions to air ","Air","SO2","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX and dust emissions to air from the combustion of gas oil in gas turbines, BAT is to use the technique given below: Fuel choice","mg/Nm3",2,"5","Green","Continuous ",0,0,0.15,"Yearly","These BAT-AELs do not apply to existing plants operated < 1 500 h/yr.","LCP (2017)\n2017/1618","3.3.3",50,50]
[777,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Gas turbines (including dual fuel turbines) ","New and existing ","Gas oil ","Unspecified ",0,"Emissions to air ","Air","SO2","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX and dust emissions to air from the combustion of gas oil in gas turbines, BAT is to use the technique given below: Fuel choice","mg/Nm3",2,"10","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period ","For existing plants operated < 500 h/yr, these levels are indicative.","LCP (2017)\n2017/1619","3.3.3",50,50]
[866,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"IGCC","Unspecified ","Unspecified","≥ 100 MWth",0,"Emissions to air ","Air","SO2","Sulphur Dioxide (24 Hour Mean)","In order to reduce SOX emissions to air from IGCC plants, BAT is to use the technique given below: Acid gas removal","mg/Nm3",3,"16","Green","Continuous",0,0,0.15,"Yearly",0,"LCP (2017)\n2017/1708","7.1.2",75,75]
[643,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"PC boiler ","Existing","Coal and/or lignite ","≥ 300 MWth",0,"Emissions to air ","Air","SO2","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD; (viii) Combined techniques for NOX and SOX reduction; (ix) Replacement or removal of the gas- gas heater located downstream of the wet FGD; (x) Fuel choice","mg/Nm3",10,130,"Green","Continuous ",0,0,0.06,"Yearly","The lower end of the range can be achieved with the use of low-sulphur fuels in combination with the most advanced wet abatement system designs.","LCP (2017)\n2017/1485","2.1.4",32,32]
[645,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"PC boiler ","Existing ","Coal and/or lignite ","≥ 300 MWth",0,"Emissions to air ","Air","SO2","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD; (viii) Combined techniques for NOX and SOX reduction; (ix) Replacement or removal of the gas- gas heater located downstream of the wet FGD; (x) Fuel choice","mg/Nm3",25,165,"Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ","The higher end of the BAT-AEL range is 220 mg/Nm3 in the case of plants put into operation no later than 7 January 2014 and operated < 1 500 h/yr. For other existing plants put into operation no later than 7 January 2014, the higher end of the BAT-AEL range is 205 mg/Nm3.","LCP (2017)\n2017/1487","2.1.4",32,32]
[642,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"PC boiler ","New","Coal and/or lignite ","≥ 300 MWth",0,"Emissions to air ","Air","SO2","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD; (viii) Combined techniques for NOX and SOX reduction; (ix) Replacement or removal of the gas- gas heater located downstream of the wet FGD; (x) Fuel choice","mg/Nm3",10,75,"Green","Continuous ",0,0,0.06,"Yearly",0,"LCP (2017)\n2017/1484","2.1.4",32,32]
[644,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"PC boiler ","New","Coal and/or lignite ","≥ 300 MWth",0,"Emissions to air ","Air","SO2","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD; (viii) Combined techniques for NOX and SOX reduction; (ix) Replacement or removal of the gas- gas heater located downstream of the wet FGD; (x) Fuel choice","mg/Nm3",25,110,"Green","Continuous ",0,0,0.06,"Daily",0,"LCP (2017)\n2017/1486","2.1.4",32,32]
[860,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Biomass-, peat-, coal- and/or lignite-fired combustion plant","Unspecified ","Co-incineration of waste with biomass, peat, coal and/or lignite","Unspecified ",0,"Emissions to air ","Air","TVOC","VOC","In order to reduce emissions of volatile organic compounds and polychlorinated dibenzo-dioxins and -furans to air from the co-incineration of waste with biomass, peat, coal and/or lignite, BAT is to use a combination of the techniques given in BAT 6, BAT 26 and below: (i) Activated carbon injection; (ii) Rapid quenching using wet scrubbing/flue-gas condenser; (iii) Selective catalytic reduction (SCR)","mg/Nm3",0.1,"5","Green","Continuous",0,0,0.06,"Yearly",0,"LCP (2017)\n2017/1702","6.1.7",73,73]
[861,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Biomass-, peat-, coal- and/or lignite-fired combustion plant","Unspecified ","Co-incineration of waste with biomass, peat, coal and/or lignite","Unspecified ",0,"Emissions to air ","Air","TVOC","VOC","In order to reduce emissions of volatile organic compounds and polychlorinated dibenzo-dioxins and -furans to air from the co-incineration of waste with biomass, peat, coal and/or lignite, BAT is to use a combination of the techniques given in BAT 6, BAT 26 and below: (i) Activated carbon injection; (ii) Rapid quenching using wet scrubbing/flue-gas condenser; (iii) Selective catalytic reduction (SCR)","mg/Nm3",0.5,"10","Green","Continuous",0,0,0.06,"Daily",0,"LCP (2017)\n2017/1703","6.1.7",73,73]
[852,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Boilers","Unspecified ","100 % process fuels from the chemical industry","Unspecified ",0,"Emissions to air ","Air","TVOC","VOC","In order to reduce emissions to air of volatile organic compounds and polychlorinated dibenzo- dioxins and -furans from the combustion of process fuels from the chemical industry in boilers, BAT is to use one or a combination of the techniques given in BAT 6 and below: (i) Activated carbon injection; (ii) Rapid quenching using wet scrubbing/flue-gas condenser; (iii) Selective catalytic reduction (SCR)","mg/Nm3",0.6,"12","Green","Once every 6 months",0,0,0.03,"Average over the sampling period",0,"LCP (2017)\n2017/1694","5.1.6",69,69]
[607,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Unspecified","Unspecified","Unspecified","Unspecified",0,"Direct discharges from flue-gas treatment  to receiving water body","Water","As","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water from flue-gas treatment, BAT is to use an appropriate combination of the techniques given below, and to use secondary techniques as close as possible to the source in order to avoid dilution: (i) Optimised combustion (see BAT 6) and flue-gas treatment systems (e.g. SCR/SNCR, see BAT 7); (ii) Adsorption on activated carbon; (iii) Aerobic biological treatment; (iv) Anoxic/anaerobic biological treatment; (v) Coagulation and flocculation; (vi) Crystallisation; (vii) Filtration (e.g. sand filtration, microfiltration, ultrafiltration); (viii) Flotation; (ix) Ion exchange; (x) Neutralisation; (xi) Oxidation; (xii) Precipitation; (xiii) Sedimentation; (xiv) Stripping","ug/l",10,50,"Green","Once every month",0,0,"Unspecified ","Daily ",0,"LCP (2017)\n2017/1449",1.5,25,25]
[608,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Unspecified","Unspecified","Unspecified","Unspecified",0,"Direct discharges from flue-gas treatment  to receiving water body","Water","Cd","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water from flue-gas treatment, BAT is to use an appropriate combination of the techniques given below, and to use secondary techniques as close as possible to the source in order to avoid dilution: (i) Optimised combustion (see BAT 6) and flue-gas treatment systems (e.g. SCR/SNCR, see BAT 7); (ii) Adsorption on activated carbon; (iii) Aerobic biological treatment; (iv) Anoxic/anaerobic biological treatment; (v) Coagulation and flocculation; (vi) Crystallisation; (vii) Filtration (e.g. sand filtration, microfiltration, ultrafiltration); (viii) Flotation; (ix) Ion exchange; (x) Neutralisation; (xi) Oxidation; (xii) Precipitation; (xiii) Sedimentation; (xiv) Stripping","ug/l",2,5,"Green","Once every month",0,0,"Unspecified ","Daily ",0,"LCP (2017)\n2017/1450",1.5,25,25]
[601,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Unspecified","Unspecified","Unspecified","Unspecified",0,"Direct discharges from flue-gas treatment  to receiving water body","Water","Chemical oxygen demand (COD)","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water from flue-gas treatment, BAT is to use an appropriate combination of the techniques given below, and to use secondary techniques as close as possible to the source in order to avoid dilution: (i) Optimised combustion (see BAT 6) and flue-gas treatment systems (e.g. SCR/SNCR, see BAT 7); (ii) Adsorption on activated carbon; (iii) Aerobic biological treatment; (iv) Anoxic/anaerobic biological treatment; (v) Coagulation and flocculation; (vi) Crystallisation; (vii) Filtration (e.g. sand filtration, microfiltration, ultrafiltration); (viii) Flotation; (ix) Ion exchange; (x) Neutralisation; (xi) Oxidation; (xii) Precipitation; (xiii) Sedimentation; (xiv) Stripping","mg/l",60,150,"Green","Once every month",0,0,"Unspecified ","Daily ","Either the BAT-AEL for TOC or the BAT-AEL for COD applies. TOC is the preferred option because its monitoring does not rely on the use of very toxic compounds.\n\nThis BAT-AEL applies after subtraction of the intake load.\n\nThis BAT-AEL only applies to waste water from the use of wet FGD.","LCP (2017)\n2017/1443",1.5,24,24]
[609,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Unspecified","Unspecified","Unspecified","Unspecified",0,"Direct discharges from flue-gas treatment  to receiving water body","Water","Cr","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water from flue-gas treatment, BAT is to use an appropriate combination of the techniques given below, and to use secondary techniques as close as possible to the source in order to avoid dilution: (i) Optimised combustion (see BAT 6) and flue-gas treatment systems (e.g. SCR/SNCR, see BAT 7); (ii) Adsorption on activated carbon; (iii) Aerobic biological treatment; (iv) Anoxic/anaerobic biological treatment; (v) Coagulation and flocculation; (vi) Crystallisation; (vii) Filtration (e.g. sand filtration, microfiltration, ultrafiltration); (viii) Flotation; (ix) Ion exchange; (x) Neutralisation; (xi) Oxidation; (xii) Precipitation; (xiii) Sedimentation; (xiv) Stripping","ug/l",10,50,"Green","Once every month",0,0,"Unspecified ","Daily ",0,"LCP (2017)\n2017/1451",1.5,25,25]
[610,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Unspecified","Unspecified","Unspecified","Unspecified",0,"Direct discharges from flue-gas treatment  to receiving water body","Water","Cu","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water from flue-gas treatment, BAT is to use an appropriate combination of the techniques given below, and to use secondary techniques as close as possible to the source in order to avoid dilution: (i) Optimised combustion (see BAT 6) and flue-gas treatment systems (e.g. SCR/SNCR, see BAT 7); (ii) Adsorption on activated carbon; (iii) Aerobic biological treatment; (iv) Anoxic/anaerobic biological treatment; (v) Coagulation and flocculation; (vi) Crystallisation; (vii) Filtration (e.g. sand filtration, microfiltration, ultrafiltration); (viii) Flotation; (ix) Ion exchange; (x) Neutralisation; (xi) Oxidation; (xii) Precipitation; (xiii) Sedimentation; (xiv) Stripping","ug/l",10,50,"Green","Once every month",0,0,"Unspecified ","Daily ",0,"LCP (2017)\n2017/1452",1.5,25,25]
[603,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Unspecified","Unspecified","Unspecified","Unspecified",0,"Direct discharges from flue-gas treatment  to receiving water body","Water","Flouride","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water from flue-gas treatment, BAT is to use an appropriate combination of the techniques given below, and to use secondary techniques as close as possible to the source in order to avoid dilution: (i) Optimised combustion (see BAT 6) and flue-gas treatment systems (e.g. SCR/SNCR, see BAT 7); (ii) Adsorption on activated carbon; (iii) Aerobic biological treatment; (iv) Anoxic/anaerobic biological treatment; (v) Coagulation and flocculation; (vi) Crystallisation; (vii) Filtration (e.g. sand filtration, microfiltration, ultrafiltration); (viii) Flotation; (ix) Ion exchange; (x) Neutralisation; (xi) Oxidation; (xii) Precipitation; (xiii) Sedimentation; (xiv) Stripping","mg/l",10,25,"Green","Once every month",0,0,"Unspecified ","Daily ","This BAT-AEL only applies to waste water from the use of wet FGD.","LCP (2017)\n2017/1445",1.5,24,24]
[611,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Unspecified","Unspecified","Unspecified","Unspecified",0,"Direct discharges from flue-gas treatment  to receiving water body","Water","Hg","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water from flue-gas treatment, BAT is to use an appropriate combination of the techniques given below, and to use secondary techniques as close as possible to the source in order to avoid dilution: (i) Optimised combustion (see BAT 6) and flue-gas treatment systems (e.g. SCR/SNCR, see BAT 7); (ii) Adsorption on activated carbon; (iii) Aerobic biological treatment; (iv) Anoxic/anaerobic biological treatment; (v) Coagulation and flocculation; (vi) Crystallisation; (vii) Filtration (e.g. sand filtration, microfiltration, ultrafiltration); (viii) Flotation; (ix) Ion exchange; (x) Neutralisation; (xi) Oxidation; (xii) Precipitation; (xiii) Sedimentation; (xiv) Stripping","ug/l",0.2,3,"Green","Once every month",0,0,"Unspecified ","Daily ",0,"LCP (2017)\n2017/1453",1.5,25,25]
[612,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Unspecified","Unspecified","Unspecified","Unspecified",0,"Direct discharges from flue-gas treatment  to receiving water body","Water","Ni","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water from flue-gas treatment, BAT is to use an appropriate combination of the techniques given below, and to use secondary techniques as close as possible to the source in order to avoid dilution: (i) Optimised combustion (see BAT 6) and flue-gas treatment systems (e.g. SCR/SNCR, see BAT 7); (ii) Adsorption on activated carbon; (iii) Aerobic biological treatment; (iv) Anoxic/anaerobic biological treatment; (v) Coagulation and flocculation; (vi) Crystallisation; (vii) Filtration (e.g. sand filtration, microfiltration, ultrafiltration); (viii) Flotation; (ix) Ion exchange; (x) Neutralisation; (xi) Oxidation; (xii) Precipitation; (xiii) Sedimentation; (xiv) Stripping","ug/l",10,50,"Green","Once every month",0,0,"Unspecified ","Daily ",0,"LCP (2017)\n2017/1454",1.5,25,25]
[613,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Unspecified","Unspecified","Unspecified","Unspecified",0,"Direct discharges from flue-gas treatment  to receiving water body","Water","Pb","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water from flue-gas treatment, BAT is to use an appropriate combination of the techniques given below, and to use secondary techniques as close as possible to the source in order to avoid dilution: (i) Optimised combustion (see BAT 6) and flue-gas treatment systems (e.g. SCR/SNCR, see BAT 7); (ii) Adsorption on activated carbon; (iii) Aerobic biological treatment; (iv) Anoxic/anaerobic biological treatment; (v) Coagulation and flocculation; (vi) Crystallisation; (vii) Filtration (e.g. sand filtration, microfiltration, ultrafiltration); (viii) Flotation; (ix) Ion exchange; (x) Neutralisation; (xi) Oxidation; (xii) Precipitation; (xiii) Sedimentation; (xiv) Stripping","ug/l",10,20,"Green","Once every month",0,0,"Unspecified ","Daily ",0,"LCP (2017)\n2017/1455",1.5,25,25]
[604,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Unspecified","Unspecified","Unspecified","Unspecified",0,"Direct discharges from flue-gas treatment  to receiving water body","Water","Sulphate","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water from flue-gas treatment, BAT is to use an appropriate combination of the techniques given below, and to use secondary techniques as close as possible to the source in order to avoid dilution: (i) Optimised combustion (see BAT 6) and flue-gas treatment systems (e.g. SCR/SNCR, see BAT 7); (ii) Adsorption on activated carbon; (iii) Aerobic biological treatment; (iv) Anoxic/anaerobic biological treatment; (v) Coagulation and flocculation; (vi) Crystallisation; (vii) Filtration (e.g. sand filtration, microfiltration, ultrafiltration); (viii) Flotation; (ix) Ion exchange; (x) Neutralisation; (xi) Oxidation; (xii) Precipitation; (xiii) Sedimentation; (xiv) Stripping","mg/l",1.3,2,"Green","Once every month",0,0,"Unspecified ","Daily ","This BAT-AEL only applies to waste water from the use of wet FGD.\n\nThis BAT-AEL only applies to combustion plants using calcium compounds in flue-gas treatment. \n\nThe higher end of the BAT-AEL range may not apply in the case of highly saline waste water (e.g. chloride concentrations ≥ 5 g/l) due to the increased solubility of calcium sulphate.\n\nThis BAT-AEL does not apply to discharges to the sea or to brackish water bodies.","LCP (2017)\n2017/1446",1.5,24,24]
[605,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Unspecified","Unspecified","Unspecified","Unspecified",0,"Direct discharges from flue-gas treatment  to receiving water body","Water","Sulphides, easily released","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water from flue-gas treatment, BAT is to use an appropriate combination of the techniques given below, and to use secondary techniques as close as possible to the source in order to avoid dilution: (i) Optimised combustion (see BAT 6) and flue-gas treatment systems (e.g. SCR/SNCR, see BAT 7); (ii) Adsorption on activated carbon; (iii) Aerobic biological treatment; (iv) Anoxic/anaerobic biological treatment; (v) Coagulation and flocculation; (vi) Crystallisation; (vii) Filtration (e.g. sand filtration, microfiltration, ultrafiltration); (viii) Flotation; (ix) Ion exchange; (x) Neutralisation; (xi) Oxidation; (xii) Precipitation; (xiii) Sedimentation; (xiv) Stripping","mg/l",0.1,0.2,"Green","Once every month",0,0,"Unspecified ","Daily ","This BAT-AEL only applies to waste water from the use of wet FGD.","LCP (2017)\n2017/1447",1.5,24,24]
[606,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Unspecified","Unspecified","Unspecified","Unspecified",0,"Direct discharges from flue-gas treatment  to receiving water body","Water","Sulphite ","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water from flue-gas treatment, BAT is to use an appropriate combination of the techniques given below, and to use secondary techniques as close as possible to the source in order to avoid dilution: (i) Optimised combustion (see BAT 6) and flue-gas treatment systems (e.g. SCR/SNCR, see BAT 7); (ii) Adsorption on activated carbon; (iii) Aerobic biological treatment; (iv) Anoxic/anaerobic biological treatment; (v) Coagulation and flocculation; (vi) Crystallisation; (vii) Filtration (e.g. sand filtration, microfiltration, ultrafiltration); (viii) Flotation; (ix) Ion exchange; (x) Neutralisation; (xi) Oxidation; (xii) Precipitation; (xiii) Sedimentation; (xiv) Stripping","mg/l",1,20,"Green","Once every month",0,0,"Unspecified ","Daily ","This BAT-AEL only applies to waste water from the use of wet FGD.","LCP (2017)\n2017/1448",1.5,24,24]
[600,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Unspecified","Unspecified","Unspecified","Unspecified",0,"Direct discharges from flue-gas treatment  to receiving water body","Water","Total organic carbon (TOC) ","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water from flue-gas treatment, BAT is to use an appropriate combination of the techniques given below, and to use secondary techniques as close as possible to the source in order to avoid dilution: (i) Optimised combustion (see BAT 6) and flue-gas treatment systems (e.g. SCR/SNCR, see BAT 7); (ii) Adsorption on activated carbon; (iii) Aerobic biological treatment; (iv) Anoxic/anaerobic biological treatment; (v) Coagulation and flocculation; (vi) Crystallisation; (vii) Filtration (e.g. sand filtration, microfiltration, ultrafiltration); (viii) Flotation; (ix) Ion exchange; (x) Neutralisation; (xi) Oxidation; (xii) Precipitation; (xiii) Sedimentation; (xiv) Stripping","mg/l",20,50,"Green","Once every month",0,0,"Unspecified ","Daily ","Either the BAT-AEL for TOC or the BAT-AEL for COD applies. TOC is the preferred option because its monitoring does not rely on the use of very toxic compounds.\n\nThis BAT-AEL applies after subtraction of the intake load.\n\nThis BAT-AEL only applies to waste water from the use of wet FGD.","LCP (2017)\n2017/1442 ",1.5,24,24]
[602,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Unspecified","Unspecified","Unspecified","Unspecified",0,"Direct discharges from flue-gas treatment  to receiving water body","Water","Total Suspended Solids (TSS) ","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water from flue-gas treatment, BAT is to use an appropriate combination of the techniques given below, and to use secondary techniques as close as possible to the source in order to avoid dilution: (i) Optimised combustion (see BAT 6) and flue-gas treatment systems (e.g. SCR/SNCR, see BAT 7); (ii) Adsorption on activated carbon; (iii) Aerobic biological treatment; (iv) Anoxic/anaerobic biological treatment; (v) Coagulation and flocculation; (vi) Crystallisation; (vii) Filtration (e.g. sand filtration, microfiltration, ultrafiltration); (viii) Flotation; (ix) Ion exchange; (x) Neutralisation; (xi) Oxidation; (xii) Precipitation; (xiii) Sedimentation; (xiv) Stripping","mg/l",10,30,"Green","Once every month",0,0,"Unspecified ","Daily ",0,"LCP (2017)\n2017/1444",1.5,24,24]
[614,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Unspecified","Unspecified","Unspecified","Unspecified",0,"Direct discharges from flue-gas treatment  to receiving water body","Water","Zn","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water from flue-gas treatment, BAT is to use an appropriate combination of the techniques given below, and to use secondary techniques as close as possible to the source in order to avoid dilution: (i) Optimised combustion (see BAT 6) and flue-gas treatment systems (e.g. SCR/SNCR, see BAT 7); (ii) Adsorption on activated carbon; (iii) Aerobic biological treatment; (iv) Anoxic/anaerobic biological treatment; (v) Coagulation and flocculation; (vi) Crystallisation; (vii) Filtration (e.g. sand filtration, microfiltration, ultrafiltration); (viii) Flotation; (ix) Ion exchange; (x) Neutralisation; (xi) Oxidation; (xii) Precipitation; (xiii) Sedimentation; (xiv) Stripping","ug/l",50,200,"Green","Once every month",0,0,"Unspecified ","Daily ",0,"LCP (2017)\n2017/1456",1.5,25,25]
[1368,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Alumina and Anode production","Anode production","Unspecified ","Unspecified","Unspecified","Unspecified","Baking plant in a stand-alone anode production plant","Emissions to air ","Air","BaP","Benzo-a-pyrene","In order to reduce dust, PAH and fluoride emissions to air from a baking plant in a stand-alone anode production plant, BAT is to use a pre-filtration unit and a regenerative thermal oxidiser followed by a dry scrubber (e.g. lime bed)","mg/Nm3",1E-3,0.01,"Green","Once per year ",0,0,0,"Average over sampling period",0,"NFM (2016) 2016/1032 \n","1.3.2.1.2",64,33]
[1364,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Alumina and Anode production","Anode production","Unspecified ","Unspecified","Unspecified","Unspecified","Baking plant with a primary aluminium smelter ","Emissions to air ","Air","BaP","Benzo-a-pyrene","In order to reduce dust, sulphur dioxide, PAH and fluoride emissions to air from a baking plant in an anode production plant integrated with a primary aluminium smelter, BAT is to use one or a combination of the techniques given below: (i) Use of raw materials and fuels containing a\nlow amount of sulphur; (ii) Dry scrubber using alumina as the adsorbent\nagent followed by a bag filter; (iii) Wet scrubber; (iv) Regenerative thermal oxidiser in combination\nwith a dust abatement system","mg/Nm3",1E-3,0.01,"Green","Once per year ",0,0,0,"Average over the sampling period",0,"NFM (2016) 2016/1032 \n","1.3.2.1.2",63,32]
[1362,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Alumina and Anode production","Anode production","Unspecified ","Unspecified","Unspecified","Unspecified","Paste plant (hot pitch storage, paste\nmixing, cooling and forming)","Emissions to air ","Air","BaP","Benzo-a-pyrene","In order to reduce dust and PAH emissions to air from a paste plant (hot pitch storage, paste mixing, cooling and forming), BAT is to use one or a combination of the techniques given below: (i) Dry scrubber using coke as the adsorbent agent, with or without precooling, followed by a bag filter; (ii) Regenerative thermal oxidiser; (iii) Catalytic thermal oxidiser","mg/Nm3",1E-3,0.01,"Green","Once per year ",0,0,0,"Average over the sampling period ",0,"NFM (2016) 2016/1032 \n","1.3.2.1.1",63,32]
[1438,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Carbon and/or Graphite Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Baking","Emissions to air ","Air","BaP","Benzo-a-pyrene","In order to reduce dust and PAH emissions to air from baking, BAT is to use one or a combination of the techniques given below: (i) ESP, in combination with a thermal oxidation step (e.g.\nregenerative thermal oxidiser) when highly volatile\ncompounds are expected; (ii) Regenerative thermal oxidiser, in combination with a\npretreatment (e.g. ESP) in cases of a high dust content\nin the exhaust gas; (iii) Thermal oxidiser","mg/Nm3",5.0000000000000001E-3,1.4999999999999999E-2,"Green","Once per year",0,0,0,"Average over the sampling period","The lower end of the range is associated with the use of a thermal oxidiser. The upper end of the range is associated with the use of a combination of an ESP and a regenerative thermal oxidiser.\n\nFor cathode production, the upper end of the range is 0,05 mg/Nm3.","NFM (2016) 2016/1032 \n","1.9.1.2",101,70]
[1440,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Carbon and/or Graphite Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Impregnation","Emissions to air ","Air","BaP","Benzo-a-pyrene","In order to reduce dust and PAH emissions to air from impregnation, BAT is to use one or a combination of the techniques given below: (i) Dry scrubber followed by a bag filter; (ii) Coke filter; (iii) Thermal oxidiser","mg/Nm3",1E-3,0.01,"Green","Once per year",0,0,0,"Average over the sampling period",0,"NFM (2016) 2016/1032 \n","1.9.1.2",102,71]
[1436,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Carbon and/or Graphite Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Production of green paste and green shapes","Emissions to air ","Air","BaP","Benzo-a-pyrene","In order to reduce dust and PAH emissions to air from the production of green paste and green shapes, BAT is to use one or a combination of the techniques given below: (i) Dry scrubber using coke as the adsorbent agent and with or without precooling, followed by a bag\nfilter; (ii) Coke filter; (iii) Regenerative thermal oxidiser; (iv) Thermal oxidiser","mg/Nm3",1E-3,0.01,"Green","Once per year",0,0,0,"Average over the sampling period",0,"NFM (2016) 2016/1032 \n","1.9.1.2",101,70]
[1434,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Carbon and/or Graphite Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Storage, handling and transportation of coke and pitch, and mechanical processes (such as grinding) and graphitising and machining","Emissions to air ","Air","BaP","Benzo-a-pyrene","In order to reduce dust emissions to air from the storage, handling and transportation of coke and pitch, and mechanical processes (such as grinding) and graphitising and machining, BAT is to use a bag filter.","mg/Nm3","N/A",0.01,"Green","Once per year",0,0,0,"Average over the sampling period","BaP particles are only expected if processing solid pitch","NFM (2016) 2016/1032 \n","1.9.1.2",100,69]
[1415,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Zinc and/or Cadmium Production","Cadmium Production","Unspecified","Unspecified","Unspecified","Unspecified","Pyrometallurgical cadmium production and the melting, alloying and casting of cadmium ingots","Emissions to air ","Air","Cd","Cadmium and its compounds (as Cd)","In order to reduce dust and metal emissions to air from pyrometallurgical cadmium production and the melting, alloying and casting of cadmium ingots, BAT is to use one or a combination of the techniques given below: (i) Bag filter; (ii) ESP; (iii) Wet scrubber ","mg/Nm3","N/A",0.1,"Green","Once per year",0,0,0,"Average over the sampling period",0,"NFM (2016) 2016/1032 \n","1.5.4.1.2",87,56]
[1386,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Alumina and Anode production","Secondary aluminium production ","Unspecified","Unspecified","Unspecified","Unspecified","Thermal treatment of contaminated secondary raw materials (e.g. swarf), the melting furnace, and remelting and molten metal treatment","Emissions to air ","Air","Cl2","Chlorine","In order to reduce emissions to air of HCl, Cl2 and HF from the thermal treatment of contaminated secondary raw materials (e.g. swarf), the melting furnace, and remelting and molten metal treatment, BAT is to use one or a combination of the techniques given below: (i) Select and feed the raw materials according to the furnace and the abatement techniques used; (ii) Ca(OH)2 or sodium bicarbonate injection in combination with a bag filter; (iii) Control of the refining process, adapting the quantity of refining gas used to remove the contaminants\npresent into the molten metals; (iv) Use of dilute chlorine with inert gas in the refining process","mg/Nm3","N/A",1,"Green","Once per year",0,0,0,"Average over the sampling period","Only applicable to emissions from refining processes carried out with chemicals containing chlorine.","NFM (2016) 2016/1032 \n","1.3.4.3.4",72,41]
[1421,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Metals Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Hydrometallurgical operation, including the associated incineration, calcining and drying operations","Emissions to air ","Air","Cl2","Chlorine","In order to reduce HCl and Cl2 emissions to air from a hydrometallurgical operation, including the associated incineration, calcining and drying operations, BAT is to use an alkaline scrubber.","mg/Nm3",0.5,2,"Green","Once per year",0,0,0,"Average over the sampling period ",0,"NFM (2016) 2016/1032 \n","1.6.1.5",91,60]
[1431,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Nickel and/or Cobalt Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Atmospheric or pressure leaching processes","Emissions to air ","Air","Cl2","Chlorine","In order to reduce nickel and chlorine emissions to air from the atmospheric or pressure leaching processes, BAT is to use a wet scrubber.","mg/Nm3","N/A",1,"Green","Once per year",0,0,0,"Average over the sampling period",0,"NFM (2016) 2016/1032 \n","1.8.2.3",98,67]
[1367,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Alumina and Anode production","Anode production","Unspecified ","Unspecified","Unspecified","Unspecified","Baking plant in a stand-alone anode production plant","Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","In order to reduce dust, PAH and fluoride emissions to air from a baking plant in a stand-alone anode production plant, BAT is to use a pre-filtration unit and a regenerative thermal oxidiser followed by a dry scrubber (e.g. lime bed)","mg/Nm3",2,5,"Green","Continuous",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.3.2.1.2",64,33]
[1363,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Alumina and Anode production","Anode production","Unspecified ","Unspecified","Unspecified","Unspecified","Baking plant with a primary aluminium smelter ","Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","In order to reduce dust, sulphur dioxide, PAH and fluoride emissions to air from a baking plant in an anode production plant integrated with a primary aluminium smelter, BAT is to use one or a combination of the techniques given below: (i) Use of raw materials and fuels containing a\nlow amount of sulphur; (ii) Dry scrubber using alumina as the adsorbent\nagent followed by a bag filter; (iii) Wet scrubber; (iv) Regenerative thermal oxidiser in combination\nwith a dust abatement system","mg/Nm3",2,5,"Green","Continuous",0,0,0,"Daily average or as an average over the sampling period",0,"NFM (2016) 2016/1032 \n","1.3.2.1.2",63,32]
[1361,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Alumina and Anode production","Anode production","Unspecified ","Unspecified","Unspecified","Unspecified","Paste plant (hot pitch storage, paste\nmixing, cooling and forming)","Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","In order to reduce dust and PAH emissions to air from a paste plant (hot pitch storage, paste mixing, cooling and forming), BAT is to use one or a combination of the techniques given below: (i) Dry scrubber using coke as the adsorbent agent, with or without precooling, followed by a bag filter; (ii) Regenerative thermal oxidiser; (iii) Catalytic thermal oxidiser","mg/Nm3",2,5,"Green","Continuous or\nonce per year",0,0,0,"Daily average or as an average over the sampling period",0,"NFM (2016) 2016/1032 \n","1.3.2.1.1",63,32]
[1370,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Alumina and Anode production","Primary aluminium production","Unspecified ","Existing","Unspecified","Unspecified","Electrolysis house (collected from the electrolytic cells and roof vents) ","Emissions to air ","Air","Dust","Particulates (PM10) (Annual Mean)","In order to prevent or collect diffuse emissions from electrolytic cells in primary aluminium production using the Søderberg technology, BAT is to use a combination of the techniques given below: (i) Use of paste with a pitch content between 25 % and 28 % (dry paste); (ii) Upgrade the manifold design to allow closed point feeding operations and improved off-gas collection\nefficiency; (iii) Alumina point feeding\n\nIn order to prevent or collect diffuse emissions from electrolytic cells in primary aluminium\nproduction using prebaked anodes, BAT is to use a combination of the techniques given below: (i) Automatic multiple point feeding of alumina; (ii) Complete hood coverage of the cell and adequate off-gas extraction rates (to lead the off-gas to the\ntreatment in BAT 67) taking into account fluoride generation from bath and carbon anode\nconsumption; (iii) Boosted suction system connected to the abatement techniques listed in BAT 67; (iv) Minimisation of the time for changing anodes and other activities that require cell hoods to be\nremoved; (v) Efficient process control system avoiding process deviations that might otherwise lead to increased cell\nevolution and emissions; (vi) Use of a programmed system for cell operations and maintenance; (vii) Use of established efficient cleaning methods in the rodding plant to recover fluorides and carbonl (viii) Storage of removed anodes in a compartment near the cell, connected to the treatment in BAT 67, or\nstorage of the butts in confined boxes\n\nIn order to reduce dust, metal and fluoride emissions to air from electrolytic cells, BAT is to use\none of the techniques given below: (i) Dry scrubber using alumina as the adsorbent agent\nfollowed by a bag filter; (ii) Dry scrubber using alumina as the adsorbent agent\nfollowed by a bag filter and a wet scrubber\n\n","kg/t Al","N/A",1.2,"Green","Continuous or\nonce per year",0,0,0,"As mass of pollutant emitted during a year from the electrolysis house divided by the mass of liquid aluminium produced in the same year.","\n\n These BAT-AELs are not applicable to plants that due to their configuration cannot measure roof emissions.","NFM (2016) 2016/1032 \n","1.3.3.1.2",66,35]
[1371,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Alumina and Anode production","Primary aluminium production","Unspecified ","New","Unspecified","Unspecified","Electrolysis house (collected from the electrolytic cells and roof vents) ","Emissions to air ","Air","Dust","Particulates (PM10) (Annual Mean)","In order to prevent or collect diffuse emissions from electrolytic cells in primary aluminium production using the Søderberg technology, BAT is to use a combination of the techniques given below: (i) Use of paste with a pitch content between 25 % and 28 % (dry paste); (ii) Upgrade the manifold design to allow closed point feeding operations and improved off-gas collection\nefficiency; (iii) Alumina point feeding\n\nIn order to prevent or collect diffuse emissions from electrolytic cells in primary aluminium\nproduction using prebaked anodes, BAT is to use a combination of the techniques given below: (i) Automatic multiple point feeding of alumina; (ii) Complete hood coverage of the cell and adequate off-gas extraction rates (to lead the off-gas to the\ntreatment in BAT 67) taking into account fluoride generation from bath and carbon anode\nconsumption; (iii) Boosted suction system connected to the abatement techniques listed in BAT 67; (iv) Minimisation of the time for changing anodes and other activities that require cell hoods to be\nremoved; (v) Efficient process control system avoiding process deviations that might otherwise lead to increased cell\nevolution and emissions; (vi) Use of a programmed system for cell operations and maintenance; (vii) Use of established efficient cleaning methods in the rodding plant to recover fluorides and carbonl (viii) Storage of removed anodes in a compartment near the cell, connected to the treatment in BAT 67, or\nstorage of the butts in confined boxes\n\nIn order to reduce dust, metal and fluoride emissions to air from electrolytic cells, BAT is to use\none of the techniques given below: (i) Dry scrubber using alumina as the adsorbent agent\nfollowed by a bag filter; (ii) Dry scrubber using alumina as the adsorbent agent\nfollowed by a bag filter and a wet scrubber\n\n","kg/t Al","N/A",0.6,"Green","Continuous or\nonce per year",0,0,0,"As mass of pollutant emitted during a year from the electrolysis house divided by the mass of liquid aluminium produced in the same year.",0,"NFM (2016) 2016/1032 \n","1.3.3.1.2",66,35]
[1375,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Alumina and Anode production","Primary aluminium production","Unspecified","Unspecified","Unspecified","Unspecified","Electrolytic cells","Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","In order to reduce dust, metal and fluoride emissions to air from electrolytic cells, BAT is to use one of the techniques given below: (i) Dry scrubber using alumina as the adsorbent agent\nfollowed by a bag filter; (ii) Dry scrubber using alumina as the adsorbent agent\nfollowed by a bag filter and a wet scrubber","mg/Nm3",2,5,"Green","Continuous or\nonce per year",0,0,0,"Daily average or average over the sampling period",0,"NFM (2016) 2016/1032 \n","1.3.3.1.1",66,35]
[1378,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Alumina and Anode production","Primary aluminium production","Unspecified","Unspecified","Unspecified","Unspecified","Melting and molten metal treatment and casting","Emissions to air ","Air","Dust","Particulates (PM10) (Annual Mean)","In order to prevent or reduce dust and metal emissions to air from melting and molten metal\ntreatment and casting in primary aluminium production, BAT is to use one or both of the techniques given\nbelow","mg/Nm3",2,25,"Green","Once per year",0,0,0,"Average of the samples obtained over a year","The lower end of the range is associated with the use of a bag filter","NFM (2016) 2016/1032 \n","1.3.3.1.2",67,36]
[1374,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Alumina and Anode production","Primary aluminium production","Unspecified","Unspecified","Unspecified","Unspecified","Storage, handling and transport of raw materials","Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","In order to reduce dust emissions from the storage, handling and transport of raw materials, BAT is to use a bag filter.","mg/Nm3",5,10,"Green","Oncer per year ",0,0,0,"Average over sampling period",0,"NFM (2016) 2016/1032 \n","1.3.3.1.1",65,34]
[1381,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Alumina and Anode production","Secondary aluminium production ","Unspecified","Unspecified","Unspecified","Unspecified","Furnace processes such as charging, melting, tapping and molten metal treatment","Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air from furnace processes such as charging, melting, tapping and molten metal treatment in secondary aluminium production, BAT is to use a bag filter","mg/Nm3",2,5,"Green","Oncer per year ",0,0,0,"Daily average or average over the sampling period",0,"NFM (2016) 2016/1032 \n","1.3.4.3.2",70,39]
[1382,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Alumina and Anode production","Secondary aluminium production ","Unspecified","Unspecified","Unspecified","Unspecified","Remelting","Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air from remelting in secondary aluminium production, BAT is to use one or a combination of the techniques given below: (i) Use of uncontaminated aluminium material i.e. solid material free of substances such as paint, plastic\nor oil (e.g. billets); (ii) Optimise combustion conditions to reduce the emissions of dust; (iii) Bag filter","mg/Nm3",2,5,"Green","Once per year",0,0,0,"Average over the sampling period","For furnaces designed to use and using only uncontaminated raw material, for which dust emissions are below 1 kg/h, the upper end of the range is 25 mg/Nm3 as an average of the samples obtained over a year.","NFM (2016) 2016/1032 \n","1.3.4.3.2",71,40]
[1380,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Alumina and Anode production","Secondary aluminium production ","Unspecified","Unspecified","Unspecified","Unspecified","Swarf drying and the removal of oil and organic compounds from the swarf, from the crushing, milling and dry separation of non-metallic constituents and metals other than aluminium, and from the storage, handling and transport","Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions from the swarf drying and the removal of oil and organic compounds from the swarf, from the crushing, milling and dry separation of non-metallic constituents and metals other than aluminium, and from the storage, handling and transport in secondary aluminium production, BAT is to use a bag filter.","mg/Nm3","N/A",5,"Green","Oncer per year ",0,0,0,"Average over the sampling period",0,"NFM (2016) 2016/1032 \n","1.3.4.3.2",70,39]
[1388,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Aluminium Production","Salt slag recycling process","Unspecified","Unspecified","Unspecified","Unspecified","Crushing and dry milling associated with the salt slag recovery process","Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air from crushing and dry milling associated with the salt slag recovery process, BAT is to use a bag filter.","mg/Nm3",2,5,"Green","Continuous",0,0,0,"Daily average or average over sampling period",0,"NFM (2016) 2016/1032 \n","1.3.5.2",73,42]
[1437,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Carbon and/or Graphite Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Baking","Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","In order to reduce dust and PAH emissions to air from baking, BAT is to use one or a combination of the techniques given below: (i) ESP, in combination with a thermal oxidation step (e.g.\nregenerative thermal oxidiser) when highly volatile\ncompounds are expected; (ii) Regenerative thermal oxidiser, in combination with a\npretreatment (e.g. ESP) in cases of a high dust content\nin the exhaust gas; (iii) Thermal oxidiser","mg/Nm3",2,10,"Green","Once per year",0,0,0,"Average over the sampling period","The lower end of the range is associated with the use of a combination of an ESP and a regenerative thermal oxidiser. The higher end of the range is associated with the use of a thermal oxidiser.","NFM (2016) 2016/1032 \n","1.9.1.2",101,70]
[1439,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Carbon and/or Graphite Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Impregnation","Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","In order to reduce dust and PAH emissions to air from impregnation, BAT is to use one or a combination of the techniques given below: (i) Dry scrubber followed by a bag filter; (ii) Coke filter; (iii) Thermal oxidiser","mg/Nm3",2,10,"Green","Once per year",0,0,0,"Average over the sampling period",0,"NFM (2016) 2016/1032 \n","1.9.1.2",102,71]
[1435,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Carbon and/or Graphite Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Production of green paste and green shapes","Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","In order to reduce dust and PAH emissions to air from the production of green paste and green shapes, BAT is to use one or a combination of the techniques given below: (i) Dry scrubber using coke as the adsorbent agent and with or without precooling, followed by a bag\nfilter; (ii) Coke filter; (iii) Regenerative thermal oxidiser; (iv) Thermal oxidiser","mg/Nm3",2,10,"Green","Once per year",0,0,0,"Average over the sampling period",0,"NFM (2016) 2016/1032 \n","1.9.1.2",101,70]
[1433,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Carbon and/or Graphite Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Storage, handling and transportation of coke and pitch, and mechanical processes (such as grinding) and graphitising and machining","Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","In order to reduce dust emissions to air from the storage, handling and transportation of coke and pitch, and mechanical processes (such as grinding) and graphitising and machining, BAT is to use a bag filter.","mg/Nm3",2,5,"Green","Once per year",0,0,0,"Average over the sampling period",0,"NFM (2016) 2016/1032 \n","1.9.1.2",100,69]
[1355,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Copper production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Anode casting (in primary and secondary copper production)","Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air from anode casting in primary and secondary copper production, BAT is to use a bag filter or, in the case of off-gases with a water content close to the dew point, a wet scrubber or a demister.","mg/Nm3",5,15,"Green","Once per year ",0,0,0,"Daily average or average over sampling period","The lower end of the range is associated with the use of a bag filter.","NFM (2016) 2016/1032 \n","1.2.3.9",57,26]
[1354,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Copper production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Anode furnace (in primary and secondary copper production)","Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air from the anode furnace in primary and secondary copper production, BAT is to use a bag filter or a scrubber in combination with an ESP.","mg/Nm3",2,5,"Green","Once per year ",0,0,0,"Daily average or average over sampling period","Dust emissions are expected to be towards the lower end of the range when emissions of heavy metals are above the following levels: 1 mg/Nm3 for lead, 1 mg/Nm3 for copper, 0,05 mg/Nm3 for arsenic, 0,05 mg/Nm3 for cadmium","NFM (2016) 2016/1032 \n","1.2.3.8",57,26]
[1349,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Copper production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Concentrate drying in primary copper production","Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air from concentrate drying in primary copper production, BAT is to use a bag filter.","mg/Nm3",3,5,"Green","Once per year ",0,0,0,"Daily average or average over the sampling period","Dust emissions are expected to be towards the lower end of the range when emissions of heavy metals are above the\nfollowing levels: 1 mg/Nm3 for lead, 1 mg/Nm3 for copper, 0,05 mg/Nm3 for arsenic, 0,05 mg/Nm3 for cadmium. ","NFM (2016) 2016/1032 \n","1.2.3.3",56,25]
[1356,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Copper production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Copper melting furnace","Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air from a copper melting furnace, BAT is to select and feed the raw materials according to the furnace type and the abatement system used and to use a bag filter.","mg/Nm3",2,5,"Green","Once per year ",0,0,0,"Daily average or average over sampling period","Dust emissions are expected to be towards the lower end of the range when emissions of copper are above 1 mg/Nm3","NFM (2016) 2016/1032 \n","1.2.3.10",57,26]
[1353,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Copper production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Copper-rich slag furnace processing","Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air from copper-rich slag furnace processing, BAT is to use a bag filter or a scrubber in combination with an ESP.","mg/Nm3",2,5,"Green","Once per year ",0,0,0,"Average over sampling period","Dust emissions are expected to be towards the lower end of the range when emissions of lead are above 1 mg/Nm3","NFM (2016) 2016/1032 \n","1.2.3.7",57,26]
[1350,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Copper production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Primary copper smelter and converter (emissions other than those that are routed to the sulphuric acid or liquid SO2 plant or power plant)","Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air (other than those that are routed to the sulphuric acid or liquid SO2 plant or power plant) from the primary copper smelter and converter, BAT is to use a bag filter and/or a wet scrubber.","mg/Nm3",2,5,"Green","Once per year ",0,0,0,"Daily average","Dust emissions are expected to be towards the lower end of the range when emissions of heavy metals are above the following levels: 1 mg/Nm3 for lead, 1 mg/Nm3 for copper, 0,05 mg/Nm3 for arsenic, 0,05 mg/Nm3 for cadmium.\n\n When the concentrates used have a high organic carbon content (e.g. around 10 wt-%), emissions of up to 10 mg/Nm3\ncan be expected. ","NFM (2016) 2016/1032 \n","1.2.3.4",56,25]
[1348,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Copper production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Reception,           storage,           handling,           transport,           metering,           mixing,           \nblending,  crushing,  drying,  cutting  and  screening  of  raw  \nmaterials,  and  the  pyrolytic  treatment  of  copper  turnings  \nin  primary  and  secondary  copper  production","Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air from the reception, storage, handling, transport, metering, mixing, blending, crushing, drying, cutting and screening of raw materials, and the pyrolytic treatment of copper turnings in primary and secondary copper production, BAT is to use a bag filter.","mg/Nm3",2,5,"Green","Once per year ",0,0,0,"Average over sampling period",0,"NFM (2016) 2016/1032 \n","1.2.3.2",56,25]
[1352,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Copper production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Secondary copper holding furnace","Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air from the secondary copper holding furnace, BAT is to use a bag filter","mg/Nm3","N/A",5,"Green","Once per year ",0,0,0,"Average over sampling period","Dust emissions are expected to be towards the lower end of the range when emissions of heavy metals are above the following levels: 1 mg/Nm3 for lead, 1 mg/Nm3 for copper, 0,05 mg/Nm3 for arsenic, 0,05 mg/Nm3 for cadmium","NFM (2016) 2016/1032 \n","1.2.3.6",57,26]
[1351,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Copper production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Secondary copper smelter and converter and processing of secondary copper intermediates (emissions other than those that are routed to the sulphuric acid plant)","Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air (other than those that are routed to the sulphuric acid plant) from the secondary copper smelter and converter and from the processing of secondary copper intermediates, BAT is to use a bag filter.","mg/Nm3",2,4,"Green","Once per year ",0,0,0,"Daily average or average over the sampling period","Dust emissions are expected to be towards the lower end of the range when emissions of heavy metals are above the following levels: 1 mg/Nm3 for lead, 1 mg/Nm3 for copper, 0,05 mg/Nm3 for arsenic, 0,05 mg/Nm3 for cadmium","NFM (2016) 2016/1032 \n","1.2.3.5",57,26]
[1427,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Ferro-alloys Production","All","Unspecified","Unspecified","Unspecified","Unspecified","— Closed submerged arc furnace or closed plasma\ndust process\n— Refractory-lined crucible for the production of\nferro-molybdenum and ferro-vanadium","Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air from a closed submerged arc furnace or a closed plasma dust process, BAT is to use one of the techniques given below: (i) Wet scrubber in combination with an ESP; (ii) Bag filter \n\nIn order to reduce dust and metal emissions to air from a refractory-lined crucible for the\nproduction of ferro-molybdenum and ferro-vanadium, BAT is to use a bag filter.","mg/Nm3",2,5,"Green","Continuous",0,0,0,"As a daily average or as an average over the sampling period.",0,"NFM (2016) 2016/1032 \n","1.7.2.2",95,64]
[1424,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Ferro-alloys Production","All","Unspecified","Unspecified","Unspecified","Unspecified","— Storage, handling and transport of solid materials — Pretreatment operations such as metering, mixing, blending and degreasing — Tapping, casting and packaging","Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air from the storage, handling and transport of solid materials, and from pretreatment operations such as metering, mixing, blending and degreasing, and from tapping, casting and packaging, BAT is to use a bag filter.","mg/Nm3",2,5,"Green","Continuous",0,0,0,"As an average over the sampling period.",0,"NFM (2016) 2016/1032 \n","1.7.2.2",95,64]
[1425,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Ferro-alloys Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Crushing, briquetting, pelletising and sintering","Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air from crushing, briquetting, pelletising and sintering, BAT is to use a bag filter or a bag filter in combination with other techniques.","mg/Nm3",2,5,"Green","Continuous",0,0,0,"As a daily average or as an average over the sampling period.","\n\nThe upper end of the range can be up to 10 mg/Nm3 for cases where a bag filter cannot be used. ","NFM (2016) 2016/1032 \n","1.7.2.2",95,64]
[1426,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Ferro-alloys Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Open or semi-closed submerged arc furnace","Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air from an open or a semi-closed submerged arc furnace, BAT is to use a bag filter.","mg/Nm3",2,5,"Green","Continuous",0,0,0,"As a daily average or as an average over the sampling period.","\nThe upper end of the range may be up to 15 mg/Nm3 for the production of FeMn, SiMn, CaSi due to the sticky nature\nof the dust (caused e.g. by its hygroscopic capacity or chemical characteristics) affecting the efficiency of the bag filter. \n\nDust emissions are expected to be towards the lower end of the range when emissions of metals are above the\nfollowing levels: 1 mg/Nm3 for lead, 0,05 mg/Nm3 for cadmium, 0,05 mg/Nm3 for chromiumVI, 0,05 mg/Nm3 for\nthallium.\n","NFM (2016) 2016/1032 \n","1.7.2.2",95,64]
[1393,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Lead and/or Tin Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Battery preparation (crushing, screning and classifying) ","Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air from battery preparation (crushing, screening and classifying), BAT is to use a bag filter or a wet scrubber.","mg/Nm3","N/A",5,"Green","Once per year",0,0,0,"Average over the sampling period ",0,"NFM (2016) 2016/1032 \n","1.4.1.2",76,45]
[1394,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Lead and/or Tin Production","Primary and secondary ","Unspecified","Unspecified","Unspecified","Unspecified","Charging, smelting and tapping","Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air (other than those that are routed to the sulphuric acid or liquid SO2 plant) from charging, smelting and tapping in primary and secondary lead and/or tin production, BAT is to use a bag filter.","mg/Nm3",2,4,"Green","Continuous",0,0,0,"Daily average or  average over the sampling period ","Dust emissions are expected to be towards the lower end of the range when emissions are above the following levels: 1 mg/Nm3 for copper, 0,05 mg/Nm3 for arsenic, 0,05 mg/Nm3 for cadmium.","NFM (2016) 2016/1032 \n","1.4.1.2",76,45]
[1392,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Lead and/or Tin Production","Primary and secondary ","Unspecified","Unspecified","Unspecified","Unspecified","Raw material preparation","Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air from raw material preparation (such as reception, handling, storage, metering, mixing, blending, drying, crushing, cutting and screening) in primary and secondary lead/or and tin production, BAT is to use a bag filter.","mg/Nm3","N/A",5,"Green","Continuous",0,0,0,"Daily average or average over the sampling period",0,"NFM (2016) 2016/1032 \n","1.4.1.2",76,45]
[1396,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Lead and/or Tin Production","Primary and secondary ","Unspecified","Unspecified","Unspecified","Unspecified","Remelting, refining and casting","Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air from remelting, refining and casting in primary and secondary lead and/or tin production, BAT is to use the techniques given below: (i) For pyrometallurgical processes: maintain the temperature of the melt bath at the lowest possible level\naccording to the process stage in combination with a bag filter; (ii) For hydrometallurgical processes: use a wet scrubber","mg/Nm3",2,4,"Green","Continous",0,0,0,"Daily average or  average over the sampling period ","Dust emissions are expected to be towards the lower end of the range when emissions are above the following levels: 1 mg/Nm3 for copper, 1 mg/Nm3 for antimony, 0,05 mg/Nm3 for arsenic, 0,05 mg/Nm3 for cadmium.","NFM (2016) 2016/1032 \n","1.4.1.2",77,46]
[1416,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Metals Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Crushing, sieving, mixing, melting, smelting, incineration, calcining, drying and refining","Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air from all dusty operations, such as crushing, sieving, mixing, melting, smelting, incineration, calcining, drying and refining, BAT is to use one of the techniques given below: (i) Bag filter; (ii) Wet scrubber in combination with an ESP, allowing\nthe recovery of selenium","mg/Nm3",2,5,"Green","Continuous",0,0,0,"Daily average or average over the sampling period",0,"NFM (2016) 2016/1032 \n","1.6.1.2",90,59]
[1429,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Nickel and/or Cobalt Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Handling and storage of raw materials, material pretreatment processes (such as ore preparation and ore/concentrate drying), furnace charging, smelting, converting, thermal refining and nickel powder and briquette production","Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","When processing sulphidic ores, in order to reduce dust and metal emissions to air from the\nhandling and storage of raw materials, material pretreatment processes (such as ore preparation and ore/concentrate\ndrying), furnace charging, smelting, converting, thermal refining and nickel powder and briquette\nproduction, BAT is to use a bag filter or a combination of an ESP and a bag filter.","mg/Nm3",2,5,"Green","Continuous",0,0,0,"Daily average or average over the sampling period",0,"NFM (2016) 2016/1032 \n","1.8.2.2",98,67]
[1414,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Zinc and/or Cadmium Production","Cadmium Production","Unspecified","Unspecified","Unspecified","Unspecified","Pyrometallurgical cadmium production and the melting, alloying and casting of cadmium ingots","Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air from pyrometallurgical cadmium production and the melting, alloying and casting of cadmium ingots, BAT is to use one or a combination of the techniques given below: (i) Bag filter; (ii) ESP; (iii) Wet scrubber ","mg/Nm3",2,3,"Green","Once per year",0,0,0,"Average over the sampling period",0,"NFM (2016) 2016/1032 \n","1.5.4.1.2",87,56]
[1401,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Zinc and/or Cadmium Production","Hydrometallurgical zinc production","Unspecified","Unspecified","Unspecified","Unspecified","Handling and storage of raw materials, dry roaster feed preparation, dry roaster feeding and calcine processing","Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air from the handling and storage of raw materials, dry roaster feed preparation, dry roaster feeding and calcine processing, BAT is to use a bag filter.","mg/Nm3","N/A",5,"Green","Once per year",0,0,0,"Average over the sampling period",0,"NFM (2016) 2016/1032 \n","1.5.1.1.2.2",81,50]
[1413,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Zinc and/or Cadmium Production","Melting, alloying and casting of zinc ingots and zinc power production","Unspecified","Unspecified","Unspecified","Unspecified","Melting, alloying and casting of zinc ingots and zinc powder production","Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air from the melting, alloying and casting of zinc ingots and zinc powder production, BAT is to use a bag filter.","mg/Nm3","N/A",5,"Green","Once per year",0,0,0,"Average over the sampling period",0,"NFM (2016) 2016/1032 \n","1.5.3.1.2",86,55]
[1405,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Zinc and/or Cadmium Production","Pyrometallurgical zinc production","Unspecified","Unspecified","Unspecified","Unspecified","Pyrometallurgical zinc production","Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air (other than those that are routed to the sulphuric acid plant) from pyrometallurgical zinc production, BAT is to use a bag filter.","mg/Nm3",2,5,"Green","Continuous",0,0,0,"Daily average or average over the sampling period","When a bag filter is not applicable, the upper end of the range is 10 mg/Nm3","NFM (2016) 2016/1032 \n","1.5.1.2.1.1",84,53]
[1408,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Zinc and/or Cadmium Production","Secondary ","Unspecified","Unspecified","Unspecified","Unspecified","Melting of metallic and mixed metallic/oxidic streams, and from the slag fuming furnace and the Waelz kiln","Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air from the melting of metallic and mixed metallic/oxidic streams, and from the slag fuming furnace and the Waelz kiln, BAT is to use a bag filter.","mg/Nm3",2,5,"Green","Once per year",0,0,0,"Daily average or average over the sampling period","A bag filter may not be applicable for a clinker operation (where chlorides need to be abated instead of metal oxides).\n\nWhen a bag filter is not applicable, the upper end of the range may be higher, up to 15 mg/Nm3. \n\n Dust emissions are expected to be towards the lower end of the range when emissions of arsenic or cadmium are\nabove 0,05 mg/Nm3.","NFM (2016) 2016/1032 \n","1.5.2.1.1",85,54]
[1407,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Zinc and/or Cadmium Production","Secondary ","Unspecified","Unspecified","Unspecified","Unspecified","Pelletising and slag processing","Emissions to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air from pelletising and slag processing, BAT is to use a bag filter.","mg/Nm3","N/A",5,"Green","Once per year",0,0,0,"Average over the sampling period ",0,"NFM (2016) 2016/1032 \n","1.5.2.1.1",84,53]
[1391,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Aluminium Production","Salt slag recycling process","Unspecified","Unspecified","Unspecified","Unspecified","Wet milling and leaching from the salt slag recovery process","Emissions to air ","Air","H2S","Hydrogen sulphide","In order to reduce gaseous emissions to air from wet milling and leaching from the salt slag recovery process, BAT is to use one or a combination of the techniques given below: (i) Activated carbon injection; (ii) Afterburner; (iii) Wet scrubber with H2SO4 solution","mg/Nm3","N/A",2,"Green","Once per year",0,0,0,"Average over the sampling period ",0,"NFM (2016) 2016/1032 \n","1.3.5.3",74,43]
[1403,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Zinc and/or Cadmium Production","Hydrometallurgical zinc production","Unspecified","Unspecified","Unspecified","Unspecified","Leaching, purification and electrolysis, and to reduce arsane and stibane emissions from purification","Emissions to air ","Air","H2SO4","Sulphuric acid","In order to reduce zinc and sulphuric acid emissions to air from leaching, purification and electrolysis, and to reduce arsane and stibane emissions from purification, BAT is to use one or a combination of the techniques given below: (i) Wet scrubber; (ii) Demister; (iii) Centrifugal system","mg/Nm3","N/A",10,"Green","Once per year",0,0,0,"Average over the sampling period",0,"NFM (2016) 2016/1032 \n","1.5.1.1.2.2",82,51]
[1385,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Alumina and Anode production","Secondary aluminium production ","Unspecified","Unspecified","Unspecified","Unspecified","Thermal treatment of contaminated secondary raw materials (e.g. swarf), the melting furnace, and remelting and molten metal treatment","Emissions to air ","Air","Hydrogen chloride, expressed as HCl","Hydrogen chloride","In order to reduce emissions to air of HCl, Cl2 and HF from the thermal treatment of contaminated secondary raw materials (e.g. swarf), the melting furnace, and remelting and molten metal treatment, BAT is to use one or a combination of the techniques given below: (i) Select and feed the raw materials according to the furnace and the abatement techniques used; (ii) Ca(OH)2 or sodium bicarbonate injection in combination with a bag filter; (iii) Control of the refining process, adapting the quantity of refining gas used to remove the contaminants\npresent into the molten metals; (iv) Use of dilute chlorine with inert gas in the refining process","mg/Nm3",5,10,"Green","Continuous or\nonce per year",0,0,0,"Daily average or  an average over the sampling period","For refining carried out with chemicals containing chlorine, the BAT-AEL refers to the average concentration during chlorination.","NFM (2016) 2016/1032 \n","1.3.4.3.4",72,41]
[1420,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Metals Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Hydrometallurgical operation, including the associated incineration, calcining and drying operations","Emissions to air ","Air","Hydrogen chloride, expressed as HCl","Hydrogen chloride","In order to reduce HCl and Cl2 emissions to air from a hydrometallurgical operation, including the associated incineration, calcining and drying operations, BAT is to use an alkaline scrubber.","mg/Nm3",5,10,"Green","Once per year",0,0,0,"Average over the sampling period ",0,"NFM (2016) 2016/1032 \n","1.6.1.5",91,60]
[1411,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Zinc and/or Cadmium Production","Secondary ","Unspecified","Unspecified","Unspecified","Unspecified","Melting of metallic and mixed metallic/oxidic streams, and from the slag fuming furnace and the Waelz kiln","Emissions to air ","Air","Hydrogen chloride, expressed as HCl","Hydrogen chloride","In order to reduce emissions of HCl and HF to air from the melting of metallic and mixed metallic/oxidic streams, and from the slag fuming furnace and the Waelz kiln, BAT is to use one of the techniques given below: (i) Injection of adsorbent followed by a bag filter; (ii) Wet scrubber ","mg/Nm3","N/A",1.5,"Green","Once per year",0,0,0,"Average over the sampling period",0,"NFM (2016) 2016/1032 \n","1.5.2.1.3",86,55]
[1369,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Alumina and Anode production","Anode production","Unspecified ","Unspecified","Unspecified","Unspecified","Baking plant in a stand-alone anode production plant","Emissions to air ","Air","HF","Hydrogen fluoride (as F) (Ecological - Daily Mean)","In order to reduce dust, PAH and fluoride emissions to air from a baking plant in a stand-alone anode production plant, BAT is to use a pre-filtration unit and a regenerative thermal oxidiser followed by a dry scrubber (e.g. lime bed)","mg/Nm3","N/A",3,"Green","Continuous",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.3.2.1.2",64,33]
[1365,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Alumina and Anode production","Anode production","Unspecified ","Unspecified","Unspecified","Unspecified","Baking plant with a primary aluminium smelter ","Emissions to air ","Air","HF","Hydrogen fluoride (as F) (Ecological - Daily Mean)","In order to reduce dust, sulphur dioxide, PAH and fluoride emissions to air from a baking plant in an anode production plant integrated with a primary aluminium smelter, BAT is to use one or a combination of the techniques given below: (i) Use of raw materials and fuels containing a\nlow amount of sulphur; (ii) Dry scrubber using alumina as the adsorbent\nagent followed by a bag filter; (iii) Wet scrubber; (iv) Regenerative thermal oxidiser in combination\nwith a dust abatement system","mg/Nm3",0.3,0.5,"Green","Continuous",0,0,0,"Daily average or as an average over the sampling period",0,"NFM (2016) 2016/1032 \n","1.3.2.1.2",63,32]
[1376,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Alumina and Anode production","Primary aluminium production","Unspecified","Unspecified","Unspecified","Unspecified","Electrolytic cells","Emissions to air ","Air","HF","Hydrogen fluoride (as F) (Ecological - Daily Mean)","In order to reduce dust, metal and fluoride emissions to air from electrolytic cells, BAT is to use one of the techniques given below: (i) Dry scrubber using alumina as the adsorbent agent\nfollowed by a bag filter; (ii) Dry scrubber using alumina as the adsorbent agent\nfollowed by a bag filter and a wet scrubber","mg/Nm3","N/A",1,"Green","Continuous or\nonce per year",0,0,0,"Daily average or average over the sampling period",0,"NFM (2016) 2016/1032 \n","1.3.3.1.1",66,35]
[1387,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Alumina and Anode production","Secondary aluminium production ","Unspecified","Unspecified","Unspecified","Unspecified","Thermal treatment of contaminated secondary raw materials (e.g. swarf), the melting furnace, and remelting and molten metal treatment","Emissions to air ","Air","HF","Hydrogen fluoride (as F) (Ecological - Daily Mean)","In order to reduce emissions to air of HCl, Cl2 and HF from the thermal treatment of contaminated secondary raw materials (e.g. swarf), the melting furnace, and remelting and molten metal treatment, BAT is to use one or a combination of the techniques given below: (i) Select and feed the raw materials according to the furnace and the abatement techniques used; (ii) Ca(OH)2 or sodium bicarbonate injection in combination with a bag filter; (iii) Control of the refining process, adapting the quantity of refining gas used to remove the contaminants\npresent into the molten metals; (iv) Use of dilute chlorine with inert gas in the refining process","mg/Nm3","N/A",1,"Green","Once per year",0,0,0,"Average over the sampling period",0,"NFM (2016) 2016/1032 \n","1.3.4.3.4",72,41]
[1412,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Zinc and/or Cadmium Production","Secondary ","Unspecified","Unspecified","Unspecified","Unspecified","Melting of metallic and mixed metallic/oxidic streams, and from the slag fuming furnace and the Waelz kiln","Emissions to air ","Air","HF","Hydrogen fluoride (as F) (Ecological - Daily Mean)","In order to reduce emissions of HCl and HF to air from the melting of metallic and mixed metallic/oxidic streams, and from the slag fuming furnace and the Waelz kiln, BAT is to use one of the techniques given below: (i) Injection of adsorbent followed by a bag filter; (ii) Wet scrubber ","mg/Nm3","N/A",0.3,"Green","Once per year",0,0,0,"Average over the sampling period",0,"NFM (2016) 2016/1032 \n","1.5.2.1.3",86,55]
[1300,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","All","All","Unspecified ","Unspecified","Unspecified","Unspecified","Pyrometallurgical process","Emissions to air","Air","Mercury and its compounds, expressed as Hg","Mercury and compounds, except mercury alkyls, (as","In order to reduce mercury emissions to air (other than those that are routed to the sulphuric acid plant) from a pyrometallurgical process, BAT is to use one or both of the techniques given below: (i) Use raw materials with a low mercury content, including by cooperating with providers in order to\nremove mercury from secondary materials; (ii) Use adsorbents (e.g. activated carbon, selenium) in combination with dust filtration","mg/Nm3",0.01,0.05,"Green","Continuous or\nonce per year",0,0,0,"Daily average or average over the sampling period","As a daily average or as an average over the sampling period.\n\nThe lower end of the range is associated with the use of adsorbents (e.g. activated carbon, selenium) in combination\nwith dust filtration, except for processes using Waelz kilns.","NFM (2016) 2016/1032 \n","1.1.6",46,15]
[1389,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Aluminium Production","Salt slag recycling process","Unspecified","Unspecified","Unspecified","Unspecified","Wet milling and leaching from the salt slag recovery process","Emissions to air ","Air","NH3","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce gaseous emissions to air from wet milling and leaching from the salt slag recovery process, BAT is to use one or a combination of the techniques given below: (i) Activated carbon injection; (ii) Afterburner; (iii) Wet scrubber with H2SO4 solution","mg/Nm3","N/A",10,"Green","Once per year",0,0,0,"Average over the sampling period ",0,"NFM (2016) 2016/1032 \n","1.3.5.3",74,43]
[1422,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Metals Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Hydrometallurgical operation using ammonia or ammonium chloride","Emissions to air ","Air","NH3","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce NH3 emissions to air from a hydrometallurgical operation using ammonia or ammonium chloride, BAT is to use a wet scrubber with sulphuric acid.","mg/Nm3",1,3,"Green","Once per year",0,0,0,"Average over the sampling period ",0,"NFM (2016) 2016/1032 \n","1.6.1.6",92,61]
[1430,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Nickel and/or Cobalt Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Atmospheric or pressure leaching processes","Emissions to air ","Air","Ni","Nickel (total Ni compounds in the PM10 fraction)","In order to reduce nickel and chlorine emissions to air from the atmospheric or pressure leaching processes, BAT is to use a wet scrubber.","mg/Nm3","N/A",1,"Green","Once per year",0,0,0,"Average over the sampling period",0,"NFM (2016) 2016/1032 \n","1.8.2.3",98,67]
[1432,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Nickel and/or Cobalt Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Nickel matte refining process using ferric\nchloride with chlorine","Emissions to air ","Air","Ni","Nickel (total Ni compounds in the PM10 fraction)","In order to reduce nickel emissions to air from the nickel matte refining process using ferric chloride with chlorine, BAT is to use a bag filter.","mg/Nm3","N/A",1,"Green","Once per year",0,0,0,"Average over the sampling period",0,"NFM (2016) 2016/1032 \n","1.8.2.3",99,68]
[1417,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Metals Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Hydrometallurgical operation involving dissolving/leaching with nitric acid","Emissions to air ","Air","NOx","Nitrogen dioxide","In order to reduce NOX emissions to air from a hydrometallurgical operation involving dissolving/leaching with nitric acid, BAT is to use one or both of the techniques given below: (i)Alkaline scrubber with caustic soda; (ii) Scrubber with oxidation agents (e.g. oxygen, hydrogen peroxide) and reducing agents (e.g. nitric acid,\nurea) for those vessels in hydrometallurgical operations with the potential to generate high concentrations\nof NOX. It is often applied in combination with (i) \n","mg/Nm3",70,150,"Green","Continuous or once per year",0,0,0,"Hourly average or average over the sampling period ",0,"NFM (2016) 2016/1032 \n","1.6.1.3",90,59]
[1395,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Lead and/or Tin Production","Primary and secondary ","Unspecified","Unspecified","Unspecified","Unspecified","Charging, smelting and tapping","Emissions to air ","Air","Pb","Lead","In order to reduce dust and metal emissions to air (other than those that are routed to the sulphuric acid or liquid SO2 plant) from charging, smelting and tapping in primary and secondary lead and/or tin production, BAT is to use a bag filter.","mg/Nm3","N/A",1,"Green","Once per year",0,0,0,"Average over the sampling period ",0,"NFM (2016) 2016/1032 \n","1.4.1.2",76,45]
[1397,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Lead and/or Tin Production","Primary and secondary ","Unspecified","Unspecified","Unspecified","Unspecified","Remelting, refining and casting","Emissions to air ","Air","Pb","Lead","In order to reduce dust and metal emissions to air from remelting, refining and casting in primary and secondary lead and/or tin production, BAT is to use the techniques given below: (i) For pyrometallurgical processes: maintain the temperature of the melt bath at the lowest possible level\naccording to the process stage in combination with a bag filter; (ii) For hydrometallurgical processes: use a wet scrubber","mg/Nm3","N/A",1,"Green","Once per year",0,0,0,"Average over the sampling period ",0,"NFM (2016) 2016/1032 \n","1.4.1.2",77,46]
[1384,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Alumina and Anode production","Secondary aluminium production ","Unspecified","Unspecified","Unspecified","Unspecified","Thermal treatment of contaminated secondary raw materials (e.g. swarf) and from the melting furnace","Emissions to air ","Air","PCDD/F","PCDD/F","In order to reduce emissions to air of organic compounds and PCDD/F from the thermal treatment of contaminated secondary raw materials (e.g. swarf) and from the melting furnace, BAT is to use a bag filter in combination with at least one of the techniques given below: (i) Select and feed the raw materials according to the furnace and the abatement techniques used; (ii) Internal burner system for melting furnaces; (iii) Afterburner; (iv) Rapid quenching; (v) Activated carbon injection","ng I-TEQ/Nm3","N/A",0.1,"Green","Once per year",0,0,0,"Average over sampling period of atleast 6 hours"," ","NFM (2016) 2016/1032 \n","1.3.4.3.2",71,40]
[1358,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Copper production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Pyrolytic treatment of copper turnings, smelting, melting, fire refining and converting operations in secondary copper production","Emissions to air ","Air","PCDD/F","PCDD/F","In order to reduce PCDD/F emissions to air from the pyrolytic treatment of copper turnings, smelting, melting, fire refining and converting operations in secondary copper production, BAT is to use one or a combination of the techniques given below: (i) Select and feed the raw materials according to the furnace and the abatement techniques used; (ii) Optimise combustion conditions to reduce the emissions of organic compounds; (iii) Use charging systems, for a semi-closed furnace, to give small additions of raw material; (iv) Thermal destruction of PCDD/F in the furnace at high temperatures (> 850 °C); (v) Use oxygen injection in the upper zone of the furnace; (vi) Internal burner system; (vi) Post-combustion chamber or afterburner or regenerative thermal oxidiser; (vii) Avoid exhaust systems with a high dust build-up for temperatures > 250 °C; (viii) Rapid quenching; (ix) Injection of adsorption agent in combination with an efficient dust collection system\n\n","ng I-TEQ/Nm3","N/A",0.1,"Green","Once per year ",0,0,0,"Average over a sampling period of at least six hours",0,"NFM (2016) 2016/1032 \n","1.2.3.3",58,27]
[1428,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Ferro-alloys Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Furnace producing ferro-alloys","Emissions to air ","Air","PCDD/F","PCDD/F","In order to reduce PCDD/F emissions to air from a furnace producing ferro-alloys, BAT is to inject adsorbents and to use an ESP and/or a bag filter.","ng I-TEQ/Nm3","N/A",0.05,"Green","Once per year",0,0,0,"As an average over the sampling period.",0,"NFM (2016) 2016/1032 \n","1.7.2.3",96,65]
[1399,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Lead and/or Tin Production","Secondary ","Unspecified","Unspecified","Unspecified","Unspecified","Smelting of raw materials","Emissions to air ","Air","PCDD/F","PCDD/F","In order to reduce PCDD/F emissions to air from the smelting of secondary lead and/or tin raw materials, BAT is to use one or a combination of the techniques given below: (i) Select and feed the raw materials according to the furnace and the abatement techniques used; (ii) Use charging systems, for a semi-closed furnace, to give small additions of raw material; (iii) Internal burner system for melting furnaces; (iv) Afterburner or regenerative thermal oxidiser; (v) Avoid exhaust systems with a high dust build-up at temperatures > 250 °C; (vi) Rapid quenching; (vii) Injection of adsorption agent in combination with efficient dust collection system; (viii) Use of efficient dust collection system; (ix) Use of oxygen injection in the upper zone of the furnace; (x) Optimise combustion conditions to reduce the emissions of organic compounds","ng I-TEQ/Nm3","N/A",0.1,"Green","Once per year",0,0,0,"Average over a sampling period of at least six hours",0,"NFM (2016) 2016/1032 \n","1.4.1.3",78,47]
[1423,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Metals Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Drying operation where the raw materials contain organic compounds, halogens or other PCDD/F precursors, from an incineration operation, and from a calcining operation","Emissions to air ","Air","PCDD/F","PCDD/F","In order to reduce PCDD/F emissions to air from a drying operation where the raw materials contain organic compounds, halogens or other PCDD/F precursors, from an incineration operation, and from a calcining operation, BAT is to use one or a combination of the techniques given below: (i) Afterburner or regenerative thermal oxidiser; (ii) Injection of adsorption agent in combination with an efficient dust collection system; (iii) Optimise combustion or process conditions for the abatement of emissions of organic compounds; (iv) Avoid exhaust systems with a high dust build-up for temperatures > 250 °C; (v) Rapid quenching; (vi) Thermal destruction of PCDD/F in the furnace at high temperatures (> 850 °C); (vii) Use of oxygen injection in the upper zone of the furnace; (viii) Internal burner system","ng I-TEQ/Nm3","N/A",0.1,"Green","Once per year",0,0,0,"Average over a sampling period of at least six hours",0,"NFM (2016) 2016/1032 \n","1.6.1.7",92,61]
[1410,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Zinc and/or Cadmium Production","Secondary ","Unspecified","Unspecified","Unspecified","Unspecified","Melting of metallic and mixed metallic/oxidic streams, and from the slag fuming furnace and the Waelz kiln","Emissions to air ","Air","PCDD/F","PCDD/F","Melting of metallic and mixed metallic/oxidic streams, and from the slag fuming furnace and the Waelz kiln: (i) Injection of adsorbent (activated carbon or lignite coke)\nfollowed by a bag filter and/or ESP; (ii) Thermal oxidiser; (iii) Regenerative thermal oxidiser ","ng I-TEQ/Nm3","N/A",0.1,"Green","Once per year",0,0,0,"Average over sampling period of atleast 6 hours",0,"NFM (2016) 2016/1032 \n","1.5.2.1.2",85,54]
[1390,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Aluminium Production","Salt slag recycling process","Unspecified","Unspecified","Unspecified","Unspecified","Wet milling and leaching from the salt slag recovery process","Emissions to air ","Air","PH3","Phosphine","In order to reduce gaseous emissions to air from wet milling and leaching from the salt slag recovery process, BAT is to use one or a combination of the techniques given below: (i) Activated carbon injection; (ii) Afterburner; (iii) Wet scrubber with H2SO4 solution","mg/Nm3","N/A",0.5,"Green","Once per year",0,0,0,"Average over the sampling period ",0,"NFM (2016) 2016/1032 \n","1.3.5.3",74,43]
[1379,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Alumina and Anode production","Primary aluminium production","Unspecified","Unspecified","Unspecified","Unspecified","Electrolytic cells","Emissions to air ","Air","SO2","Sulphur Dioxide (24 Hour Mean)","In order to reduce emissions to air from electrolytic cells, BAT is to use one or both of the techniques given below: (i) Use of low-sulphur anodes; (ii) Wet scrubber","kg/t Al",2.5,15,"Green","Continuous or\nonce per year",0,0,0,"As mass of pollutant emitted during a year divided by the mass of liquid aluminium produced in the same year.","Anodes containing less than 1,5 % sulphur as a yearly average can be produced by an appropriate\ncombination of the raw materials used. A minimum sulphur content of 0,9 % as a yearly average is required\nfor the viability of the electrolysis process.\n\n The lower end of the range is associated with the use of a wet scrubber. The higher end of the range is associated with\nthe use of low-sulphur anodes.","NFM (2016) 2016/1032 \n","1.3.3.1.3",67,36]
[1359,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Copper production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Primary copper production ","Emissions to air ","Air","SO2","Sulphur Dioxide (24 Hour Mean)","In order to reduce SO2 emissions (other than those that are routed to the sulphuric acid or liquid SO2 plant or power plant) from primary and secondary copper production, BAT is to use one or a combination of the techniques given below: (i) Dry or semi-dry scrubber; (ii) Wet scrubber ; (iii) Polyether-based absorption/desorption system ","mg/Nm3",50,500,"Green","Continuous or\nonce per year",0,0,0,"Daily average or as an average over the sampling period","In the case of using a wet scrubber or a concentrate with a low sulphur content, the BAT-AEL can be up to 350 mg/Nm3","NFM (2016) 2016/1032 \n","1.2.3.4",59,28]
[1360,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Copper production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Secondary copper production ","Emissions to air ","Air","SO2","Sulphur Dioxide (24 Hour Mean)","In order to reduce SO2 emissions (other than those that are routed to the sulphuric acid or liquid SO2 plant or power plant) from primary and secondary copper production, BAT is to use one or a combination of the techniques given below: (i) Dry or semi-dry scrubber; (ii) Wet scrubber ; (iii) Polyether-based absorption/desorption system ","mg/Nm3",50,300,"Green","Continuous or\nonce per year",0,0,0,"Daily average or as an average over the sampling period",0,"NFM (2016) 2016/1032 \n","1.2.3.4",59,28]
[1400,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Lead and/or Tin Production","Primary and secondary ","Unspecified","Unspecified","Unspecified","Unspecified","Charging, smelting and tapping","Emissions to air ","Air","SO2","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SO2 emissions to air (other than those that are routed to the sulphuric acid or liquid SO2 plant) from charging, smelting and tapping in primary and secondary lead and/or tin production, BAT is to use one or a combination of the techniques given below: (i) Alkaline leaching of raw materials that contain sulphur\nin the form of sulphate; (ii) Dry or semi-dry scrubber; (iii) Wet scrubber; (iv) Fixation of sulphur in the smelt phase ","mg/Nm3",50,350,"Green","Continuous or once per year",0,0,0,"Daily average or average over the sampling period","When wet scrubbers are not applicable, the upper end of the range is 500 mg/Nm3.\n\nAn alkali salt solution is used to remove sulphates from secondary materials prior to smelting.\n\nThe fixation of sulphur in the smelt phase is achieved by adding iron and soda (Na2CO3) in the\nsmelters which react with the sulphur contained in the raw materials to form Na2S-FeS slag","NFM (2016) 2016/1032 \n","1.4.1.4",79,48]
[1419,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Metals Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Hydrometallurgical operation, including the associated incineration, calcining and drying operations","Emissions to air ","Air","SO2","Sulphur Dioxide (24 Hour Mean)","In order to reduce SO2 emissions to air from a hydrometallurgical operation, including the associated incineration, calcining and drying operations, BAT is to use a wet scrubber.","mg/Nm3",50,100,"Green","Continuous or once per year",0,0,0,"Daily average or average over the sampling period",0,"NFM (2016) 2016/1032 \n","1.6.1.4",91,60]
[1418,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Metals Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Melting and smelting operation for the production of Doré metal, including the associated incineration, calcining and drying operations","Emissions to air ","Air","SO2","Sulphur Dioxide (24 Hour Mean)","In order to reduce SO2 emissions to air (other than those that are routed to the sulphuric acid plant) from a melting and smelting operation for the production of Doré metal, including the associated incineration, calcining and drying operations, BAT is to use one or a combination of the techniques given below: (i) Lime injection in combination with a bag filter; (ii) Wet scrubber","mg/Nm3",50,480,"Green","Continuous or once per year",0,0,0,"Daily average or average over the sampling period",0,"NFM (2016) 2016/1032 \n","1.6.1.4",91,60]
[1406,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Zinc and/or Cadmium Production","Pyrometallurgical zinc production","Unspecified","Unspecified","Unspecified","Unspecified","Pyrometallurgical zinc production","Emissions to air ","Air","SO2","Sulphur Dioxide (24 Hour Mean)","In order to reduce SO2 emissions to air (other than those that are routed to the sulphuric acid plant) from pyrometallurgical zinc production, BAT is to use a wet desulphurisation technique.","mg/Nm3","N/A",500,"Green","Continuous",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.5.1.2.1.1",84,53]
[1404,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Zinc and/or Cadmium Production","Hydrometallurgical zinc production","Unspecified","Unspecified","Unspecified","Unspecified","Leaching, purification and electrolysis, and to reduce arsane and stibane emissions from purification","Emissions to air ","Air","Sum of AsH3 and SbH3","Sum of AsH3 and SbH3","In order to reduce zinc and sulphuric acid emissions to air from leaching, purification and electrolysis, and to reduce arsane and stibane emissions from purification, BAT is to use one or a combination of the techniques given below: (i) Wet scrubber; (ii) Demister; (iii) Centrifugal system","mg/Nm3","N/A",0.5,"Green","Once per year",0,0,0,"Average over the sampling period",0,"NFM (2016) 2016/1032 \n","1.5.1.1.2.2",82,51]
[1366,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Alumina and Anode production","Anode production","Unspecified ","Unspecified","Unspecified","Unspecified","Baking plant with in an anode production plant with a primary aluminium smelter ","Emissions to air ","Air","Total fluorides","Total fluorides","In order to reduce dust, sulphur dioxide, PAH and fluoride emissions to air from a baking plant in an anode production plant integrated with a primary aluminium smelter, BAT is to use one or a combination of the techniques given below: (i) Use of raw materials and fuels containing a\nlow amount of sulphur; (ii) Dry scrubber using alumina as the adsorbent\nagent followed by a bag filter; (iii) Wet scrubber; (iv) Regenerative thermal oxidiser in combination\nwith a dust abatement system","mg/Nm3","N/A",0.8,"Green","Once per year",0,0,0,"Average over the sampling period",0,"NFM (2016) 2016/1032 \n","1.3.2.1.2",63,32]
[1372,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Alumina and Anode production","Primary aluminium production","Unspecified","Existing","Unspecified","Unspecified","Electrolysis house (collected from the electrolytic cells and roof vents) ","Emissions to air ","Air","Total fluorides","Total fluorides","In order to prevent or collect diffuse emissions from electrolytic cells in primary aluminium production using the Søderberg technology, BAT is to use a combination of the techniques given below: (i) Use of paste with a pitch content between 25 % and 28 % (dry paste); (ii) Upgrade the manifold design to allow closed point feeding operations and improved off-gas collection\nefficiency; (iii) Alumina point feeding\n\nIn order to prevent or collect diffuse emissions from electrolytic cells in primary aluminium\nproduction using prebaked anodes, BAT is to use a combination of the techniques given below: (i) Automatic multiple point feeding of alumina; (ii) Complete hood coverage of the cell and adequate off-gas extraction rates (to lead the off-gas to the\ntreatment in BAT 67) taking into account fluoride generation from bath and carbon anode\nconsumption; (iii) Boosted suction system connected to the abatement techniques listed in BAT 67; (iv) Minimisation of the time for changing anodes and other activities that require cell hoods to be\nremoved; (v) Efficient process control system avoiding process deviations that might otherwise lead to increased cell\nevolution and emissions; (vi) Use of a programmed system for cell operations and maintenance; (vii) Use of established efficient cleaning methods in the rodding plant to recover fluorides and carbonl (viii) Storage of removed anodes in a compartment near the cell, connected to the treatment in BAT 67, or\nstorage of the butts in confined boxes\n\nIn order to reduce dust, metal and fluoride emissions to air from electrolytic cells, BAT is to use\none of the techniques given below: (i) Dry scrubber using alumina as the adsorbent agent\nfollowed by a bag filter; (ii) Dry scrubber using alumina as the adsorbent agent\nfollowed by a bag filter and a wet scrubber\n\n","kg/t Al","N/A",0.6,"Green","Continuous or\nonce per year",0,0,0,"As mass of pollutant emitted during a year from the electrolysis house divided by the mass of liquid aluminium produced in the same year.","\n\n These BAT-AELs are not applicable to plants that due to their configuration cannot measure roof emissions.","NFM (2016) 2016/1032 \n","1.3.3.1.2",66,35]
[1373,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Alumina and Anode production","Primary aluminium production","Unspecified","New","Unspecified","Unspecified","Electrolysis house (collected from the electrolytic cells and roof vents) ","Emissions to air ","Air","Total fluorides","Total fluorides","In order to prevent or collect diffuse emissions from electrolytic cells in primary aluminium production using the Søderberg technology, BAT is to use a combination of the techniques given below: (i) Use of paste with a pitch content between 25 % and 28 % (dry paste); (ii) Upgrade the manifold design to allow closed point feeding operations and improved off-gas collection\nefficiency; (iii) Alumina point feeding\n\nIn order to prevent or collect diffuse emissions from electrolytic cells in primary aluminium\nproduction using prebaked anodes, BAT is to use a combination of the techniques given below: (i) Automatic multiple point feeding of alumina; (ii) Complete hood coverage of the cell and adequate off-gas extraction rates (to lead the off-gas to the\ntreatment in BAT 67) taking into account fluoride generation from bath and carbon anode\nconsumption; (iii) Boosted suction system connected to the abatement techniques listed in BAT 67; (iv) Minimisation of the time for changing anodes and other activities that require cell hoods to be\nremoved; (v) Efficient process control system avoiding process deviations that might otherwise lead to increased cell\nevolution and emissions; (vi) Use of a programmed system for cell operations and maintenance; (vii) Use of established efficient cleaning methods in the rodding plant to recover fluorides and carbonl (viii) Storage of removed anodes in a compartment near the cell, connected to the treatment in BAT 67, or\nstorage of the butts in confined boxes\n\nIn order to reduce dust, metal and fluoride emissions to air from electrolytic cells, BAT is to use\none of the techniques given below: (i) Dry scrubber using alumina as the adsorbent agent\nfollowed by a bag filter; (ii) Dry scrubber using alumina as the adsorbent agent\nfollowed by a bag filter and a wet scrubber\n\n","kg/t Al","N/A",0.35,"Green","Continuous or\nonce per year",0,0,0,"As mass of pollutant emitted during a year from the electrolysis house divided by the mass of liquid aluminium produced in the same year.",0,"NFM (2016) 2016/1032 \n","1.3.3.1.2",66,35]
[1377,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Alumina and Anode production","Primary aluminium production","Unspecified","Unspecified","Unspecified","Unspecified","Electrolytic cells","Emissions to air ","Air","Total fluorides","Total fluorides","In order to reduce dust, metal and fluoride emissions to air from electrolytic cells, BAT is to use one of the techniques given below: (i) Dry scrubber using alumina as the adsorbent agent\nfollowed by a bag filter; (ii) Dry scrubber using alumina as the adsorbent agent\nfollowed by a bag filter and a wet scrubber","mg/Nm3","N/A",1.5,"Green","Continuous or\nonce per year",0,0,0,"Average over the sampling period",0,"NFM (2016) 2016/1032 \n","1.3.3.1.1",66,35]
[1383,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Alumina and Anode production","Secondary aluminium production ","Unspecified","Unspecified","Unspecified","Unspecified","Thermal treatment of contaminated secondary raw materials (e.g. swarf) and from the melting furnace","Emissions to air ","Air","TVOC","VOC","In order to reduce emissions to air of organic compounds and PCDD/F from the thermal treatment of contaminated secondary raw materials (e.g. swarf) and from the melting furnace, BAT is to use a bag filter in combination with at least one of the techniques given below: (i) Select and feed the raw materials according to the furnace and the abatement techniques used; (ii) Internal burner system for melting furnaces; (iii) Afterburner; (iv) Rapid quenching; (v) Activated carbon injection","mg/Nm3",10,30,"Green","Continuous or\nonce per year",0,0,0,"Daily average or average over the sampling period",0,"NFM (2016) 2016/1032 \n","1.3.4.3.2",71,40]
[1441,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Carbon and/or Graphite Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Impregnation stage where special impregnation agents such as resins and biodegradable solvents are used","Emissions to air ","Air","TVOC","VOC","In order to reduce emissions of organic compounds to air, including phenol and the formaldehyde from the impregnation stage where special impregnation agents such as resins and biodegradable solvents are used, BAT is to use one of the techniques given below: (i) Regenerative thermal oxidiser in combination with an ESP for the mixing, baking and impregnation\nstages; (ii) Biofilter and/or bioscrubber for the impregnation stage where special impregnation agents such as\nresins and biodegradable solvents are used","mg/Nm3",10,40,"Green","Once per year",0,0,0,"Average over the sampling period","The lower end of the range is associated with the use of an ESP in combination with a regenerative thermal oxidiser. The upper end of the range is associated with the use of a biofilter and/or a bioscrubber.","NFM (2016) 2016/1032 \n","1.9.1.4",102,71]
[1357,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Copper production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Pyrolytic treatment of copper turnings, and the drying, smelting and melting of secondary raw materials","Emissions to air ","Air","TVOC","VOC","In  order  to  reduce  organic  compound  emissions  to  air  from  the  pyrolytic  treatment  of  copper  \nturnings,   and   the   drying,   smelting   and   melting   of   secondary   raw   materials,   BAT   is   to   use   one   of   the   \ntechniques  given  below: (i) Afterburner or post-combustion chamber or\nregenerative thermal oxidiser; (ii) Injection of adsorbent in combination with a bag\nfilter; (iii) Design of furnace and the abatement techniques\naccording to the raw materials available; (iv) Select and feed the raw materials according to the\nfurnace and the abatement techniques used; (v) Thermal destruction of TVOC at high\ntemperatures in the furnace","mg/Nm3",3,30,"Green","Continuous or\nonce per year",0,0,0,"Daily average or average over sampling period","The lower end of the range is associated with the use of a regenerative thermal oxidiser.","NFM (2016) 2016/1032 \n","1.2.3.3",58,27]
[1398,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Lead and/or Tin Production","Secondary ","Unspecified","Unspecified","Unspecified","Unspecified","Raw material drying and smelting process","Emissions to air ","Air","TVOC","VOC","In order to reduce emissions of organic compounds to air from the raw material drying and smelting process in secondary lead and/or tin production, BAT is to use one or a combination of the techniques given below: (i) Select and feed the raw materials according to the\nfurnace and the abatement techniques used; (ii) Optimise combustion conditions to reduce the\nemissions of organic compounds; (iii) Afterburner or regenerative thermal oxidiser ","mg/Nm3",10,40,"Green","Continuous or\nonce per year",0,0,0,"Daily average or  average over the sampling period ",0,"NFM (2016) 2016/1032 \n","1.4.1.3",77,46]
[1409,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Zinc and/or Cadmium Production","Secondary ","Unspecified","Unspecified","Unspecified","Unspecified","Melting of metallic and mixed metallic/oxidic streams, and from the slag fuming furnace and the Waelz kiln","Emissions to air ","Air","TVOC","VOC","In order to reduce emissions of organic compounds to air from the melting of metallic and\nmixed metallic/oxidic streams, and from the slag fuming furnace and the Waelz kiln, BAT is to use one or a\ncombination of the techniques given below: (i) Injection of adsorbent (activated carbon or lignite coke)\nfollowed by a bag filter and/or ESP\n (ii) Thermal oxidiser; (iii) Regenerative thermal oxidiser ","mg/Nm3",2,20,"Green","Continuous or once per year",0,0,0,"Daily average or average over the sampling period",0,"NFM (2016) 2016/1032 \n","1.5.2.1.2",85,54]
[1402,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Zinc and/or Cadmium Production","Hydrometallurgical zinc production","Unspecified","Unspecified","Unspecified","Unspecified","Leaching, purification and electrolysis, and to reduce arsane and stibane emissions from purification","Emissions to air ","Air","Zn","Zinc","In order to reduce zinc and sulphuric acid emissions to air from leaching, purification and electrolysis, and to reduce arsane and stibane emissions from purification, BAT is to use one or a combination of the techniques given below: (i) Wet scrubber; (ii) Demister; (iii) Centrifugal system","mg/Nm3","N/A",1,"Green","Once per year",0,0,0,"Average over the sampling period",0,"NFM (2016) 2016/1032 \n","1.5.1.1.2.2",82,51]
[1302,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Copper","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Emissions to water","Water","Arsenic (As)","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.1,"Green","Once per month",0,0,0,"Daily average","In the case of a high arsenic content in the total input of the plant, the BAT-AEL may be up to 0,2 mg/l.","NFM (2016) 2016/1032 \n","1.1.9",49,18]
[1307,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Ferro-alloys Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Emissions to water","Water","Arsenic (As)","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.1,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[1303,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Lead and/or Tin Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Emissions to water","Water","Arsenic (As)","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.1,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[1306,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Nickel and/or Cobalt Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Emissions to water","Water","Arsenic (As)","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.3,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[1305,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Precious metals","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Emissions to water","Water","Arsenic (As)","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.1,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[1304,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Zinc and/or Cadmium Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Emissions to water","Water","Arsenic (As)","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.1,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[1308,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Copper","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Emissions to water","Water","Cadmium (Cd)","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l",0.02,0.1,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[1313,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Ferro-alloys Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates",0,"Water","Cadmium (Cd)","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.05,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[1309,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Lead and/or Tin Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Emissions to water","Water","Cadmium (Cd)","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.1,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[1312,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Nickel and/or Cobalt Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates",0,"Water","Cadmium (Cd)","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.1,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[1311,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Precious metals","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates",0,"Water","Cadmium (Cd)","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.05,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[1310,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Zinc and/or Cadmium Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Emissions to water","Water","Cadmium (Cd)","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.1,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[1316,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Ferro-alloys Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates",0,"Water","Chromium total (Cr)","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.2,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[1317,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Ferro-alloys Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates",0,"Water","Chromium total (VI)  (Cr(VI))","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.05,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[1314,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Lead and/or Tin Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates",0,"Water","Cobalt (Co)","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.1,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[1315,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Nickel and/or Cobalt Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates",0,"Water","Cobalt (Co)","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l",0.1,0.5,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[1318,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Copper","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates",0,"Water","Copper (Cu)","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l",0.05,0.5,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[1323,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Ferro-alloys Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates",0,"Water","Copper (Cu)","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.5,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[1319,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Lead and/or Tin Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates",0,"Water","Copper (Cu)","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.2,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[1322,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Nickel and/or Cobalt Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates",0,"Water","Copper (Cu)","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.5,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[1321,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Precious metals","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates",0,"Water","Copper (Cu)","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.3,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[1320,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Zinc and/or Cadmium Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates",0,"Water","Copper (Cu)","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.1,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[1336,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Copper","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates",0,"Water","Lead (Pb)","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.5,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[1341,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Ferro-alloys Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates",0,"Water","Lead (Pb)","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.2,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[1337,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Lead and/or Tin Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates",0,"Water","Lead (Pb)","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.5,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[1340,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Nickel and/or Cobalt Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates",0,"Water","Lead (Pb)","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.5,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[1339,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Precious metals","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates",0,"Water","Lead (Pb)","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.5,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[1338,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Zinc and/or Cadmium Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates",0,"Water","Lead (Pb)","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.2,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[1324,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Copper","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates",0,"Water","Mercury (Hg)","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l",5.0000000000000001E-3,0.02,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[1329,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Ferro-alloys Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates",0,"Water","Mercury (Hg)","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.05,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[1325,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Lead and/or Tin Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates",0,"Water","Mercury (Hg)","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.05,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[1328,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Nickel and/or Cobalt Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates",0,"Water","Mercury (Hg)","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.05,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[1327,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Precious metals","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates",0,"Water","Mercury (Hg)","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.05,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[1326,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Zinc and/or Cadmium Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates",0,"Water","Mercury (Hg)","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.05,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[1330,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Copper","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates",0,"Water","Nickel (Ni)","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.5,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[1335,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Ferro-alloys Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates",0,"Water","Nickel (Ni)","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",2,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[1331,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Lead and/or Tin Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates",0,"Water","Nickel (Ni)","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.5,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[1334,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Nickel and/or Cobalt Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates",0,"Water","Nickel (Ni)","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",2,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[1333,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Precious metals","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates",0,"Water","Nickel (Ni)","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.5,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[1332,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Zinc and/or Cadmium Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates",0,"Water","Nickel (Ni)","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.1,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[1301,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Precious metals","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Emissions to water","Water","Silver (Ag)","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.6,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[1342,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Copper","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates",0,"Water","Zinc (Zn) ","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",1,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[1347,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Ferro-alloys Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates",0,"Water","Zinc (Zn) ","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",1,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[1343,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Lead and/or Tin Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates",0,"Water","Zinc (Zn) ","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",1,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[1346,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Nickel and/or Cobalt Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates",0,"Water","Zinc (Zn) ","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",1,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[1345,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Precious metals","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates",0,"Water","Zinc (Zn) ","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.4,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[1344,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Zinc and/or Cadmium Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates",0,"Water","Zinc (Zn) ","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",1,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[538,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Lime kilns","Emissions to air","Air","Dust","Particulates (PM10) (Annual Mean)","Existing","mg/Nm3",10,30,"Green","Continuous",0,0,0.06,"Yearly","For an existing lime kiln equipped with an ESP approaching the end of its operational life, emission levels may increase over time up to 50 mg/Nm3 (corresponding to 0,05 kg/ADt).","PP (2014)\n2014/687/EU","1.2.2.3",26,26]
[539,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Lime kilns","Emissions to air","Air","Dust","Particulates (PM10) (Annual Mean)","Existing","kg dust/ADt",5.0000000000000001E-3,0.03,"Green","Continuous",0,0,"Unspecified","Yearly","For an existing lime kiln equipped with an ESP approaching the end of its operational life, emission levels may increase over time up to 50 mg/Nm3 (corresponding to 0,05 kg/ADt).","PP (2014)\n2014/687/EU","1.2.2.3",26,26]
[536,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Lime kilns","Emissions to air","Air","Dust","Particulates (PM10) (Annual Mean)","New or major refurbishment","mg/Nm3",10,25,"Green","Continuous",0,0,0.06,"Yearly",0,"PP (2014)\n2014/687/EU","1.2.2.3",26,26]
[537,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Lime kilns","Emissions to air","Air","Dust","Particulates (PM10) (Annual Mean)","New or major refurbishment","kg dust/ADt",5.0000000000000001E-3,0.02,"Green","Continuous",0,0,"Unspecified","Yearly",0,"PP (2014)\n2014/687/EU","1.2.2.3",26,26]
[525,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Recovery boiler","Emissions to air","Air","Dust","Particulates (PM10) (Annual Mean)","Existing","mg/Nm3",10,40,"Green","Continuous",0,0,0.06,"Yearly","For an existing recovery boiler equipped with an ESP approaching the end of its operational life, emission levels may increase over time up to 50 mg/Nm3 (corresponding to 0,4 kg/ADt).","PP (2014)\n2014/687/EU","1.2.2.2",24,24]
[526,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Recovery boiler","Emissions to air","Air","Dust","Particulates (PM10) (Annual Mean)","Existing","kg dust/ADt",0.02,0.3,"Green","Continuous",0,0,"Unspecified","Yearly","For an existing recovery boiler equipped with an ESP approaching the end of its operational life, emission levels may increase over time up to 50 mg/Nm3 (corresponding to 0,4 kg/ADt).","PP (2014)\n2014/687/EU","1.2.2.2",24,24]
[561,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Recovery boiler","Emissions to air","Air","Dust","Particulates (PM10) (24 hr Mean)","In order to reduce dust and SO2 emissions from a recovery boiler, BAT is to use one of the techniques given below and to limit ‘acid operation’ of the scrubbers to the minimum required to ensure their proper functioning: (i) ESP or multicyclones with multistage venturi scrubbers; (ii) ESP or multicyclones with multistage double inlet downstream scrubbers","mg/Nm3",5,20,"Green","Periodic ",0,0," ","Average over the sampling period","For recovery boilers operated in mills using more than 25 % of hardwood (potassium-rich) in raw materials, higher dust emissions up to 30 mg/Nm3 may occur.\n\nThe BAT-AEL for dust does not apply for ammonium-based mills.","PP (2014)\n2014/687/EU","1.2.2.4",32,32]
[523,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Recovery boiler","Emissions to air","Air","Dust","Particulates (PM10) (Annual Mean)","New or major refurbishment","mg/Nm3",10,25,"Green","Continuous",0,0,0.06,"Yearly",0,"PP (2014)\n2014/687/EU","1.2.2.2",24,24]
[524,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Recovery boiler","Emissions to air","Air","Dust","Particulates (PM10) (Annual Mean)","New or major refurbishment","kg dust/ADt",0.02,0.2,"Green","Continuous",0,0,"Unspecified","Yearly",0,"PP (2014)\n2014/687/EU","1.2.2.2",24,24]
[516,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Recovery boiler","Emissions to air","Air","Gaseous S (TRS- S + SO2-S) DS 75- 83%","Gaseous S (TRS- S + SO2-S) DS 75- 83%","In order to reduce SO2 and TRS emissions from a recovery boiler, BAT is to use a combination of the techniques given below: (i) Increasing the dry solids (DS) content of black liquor; (ii) Optimised firing; (iii) Wet scrubber","kg S/ADt",0.03,0.13,"Green","Continuous",0,0,"Unspecified","Yearly","Increasing the DS content of the black liquor results in lower SO2 emissions and higher NOx emissions. Due to this, a recovery boiler with low emission levels for SO2, may be on the higher end of the range for NOx and vice versa. \n\nIf a recovery boiler were to burn black liquor with a DS > 83 %, then SO2 and gaseous S emission levels should be reconsidered on a case-by-case basis.","PP (2014)\n2014/687/EU","1.2.2.2",22,22]
[515,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Recovery boiler","Emissions to air","Air","Gaseous S (TRS- S + SO2-S) DS< 75%","Gaseous S (TRS- S + SO2-S) DS< 75%","In order to reduce SO2 and TRS emissions from a recovery boiler, BAT is to use a combination of the techniques given below: (i) Increasing the dry solids (DS) content of black liquor; (ii) Optimised firing; (iii) Wet scrubber","kg S/ADt",0.03,0.17,"Green","Continuous",0,0,"Unspecified","Yearly","Increasing the DS content of the black liquor results in lower SO2 emissions and higher NOx emissions. Due to this, a recovery boiler with low emission levels for SO2, may be on the higher end of the range for NOx and vice versa. ","PP (2014)\n2014/687/EU","1.2.2.2",22,22]
[542,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","TRS burner for strong odorous gases ","Emissions to air","Air","Gaseous S (TRS-S + SO2-S)","Gaseous S (TRS-S + SO2-S)","In order to reduce SO2 emissions from the incineration of strong odorous gases in a dedicated TRS burner, BAT is to use an alkaline SO2 scrubber.","kg S/Adt",2E-3,0.05,"Green","Continuous",0,0,"Unspecified","Yearly","This BAT-AEL is based on a gas flow in the range of 100-200 Nm3/ADt.","PP (2014)\n2014/687/EU","1.2.2.4",27,27]
[530,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Lime kilns","Emissions to air","Air","Gaseous S (TRS-S + SO2-S) when strong gases are burnt in the lime kiln","Gaseous S (TRS-S + SO2-S) when strong gases are burnt in the lime kiln","In order to reduce SO2 emissions from a lime kiln, BAT is to apply one or a combination of the techniques given below: (i) Fuel selection/low sulphur fuel; (ii) Limit incineration of sulphur-containing odorous strong gases in the lime kiln; (iii) Control of Na2S content in lime mud feed; (iv) Alkaline scrubber\n","kg S/ADt",5.5E-2,0.12,"Green","Continuous",0,0,"Unspecified","Yearly","‘strong gases’ includes methanol and turpentine","PP (2014)\n2014/687/EU","1.2.2.3",25,25]
[529,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Lime kilns","Emissions to air","Air","Gaseous S (TRS-S + SO2-S) when strong gases are not burnt in the lime kiln","Gaseous S (TRS-S + SO2-S) when strong gases are not burnt in the lime kiln","In order to reduce SO2 emissions from a lime kiln, BAT is to apply one or a combination of the techniques given below: (i) Fuel selection/low sulphur fuel; (ii) Limit incineration of sulphur-containing odorous strong gases in the lime kiln; (iii) Control of Na2S content in lime mud feed; (iv) Alkaline scrubber\n","kg S/ADt",5.0000000000000001E-3,7.0000000000000007E-2,"Green","Continuous",0,0,"Unspecified","Yearly","‘strong gases’ includes methanol and turpentine","PP (2014)\n2014/687/EU","1.2.2.3",25,25]
[560,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Recovery boiler","Emissions to air","Air","NH3 (ammonia slip from SNCR)","NH3 (ammonia slip from SNCR)","In order to reduce NOx emissions from a recovery boiler, BAT is to use an optimised firing system including one or a combination of the techniques given below: (i) Optimising the recovery boiler by controlling the firing conditions; (ii) Staged injection of spent liquor; (iii) Selective non-catalytic reduction (SNCR)","mg/Nm3","N/A",5,"Green","Periodic ",0,0,0.05,"Yearly",0,"PP (2014)\n2014/687/EU","1.2.2.4",32,32]
[534,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Gaseous fuels ","Lime kilns","Emissions to air","Air","NOx","Nitrogen dioxide","In order to reduce NOx emissions from a lime kiln, BAT is to apply a combination of the techniques given below: (i) Optimised combustion and combustion control; (ii) Good mixing of fuel and air; (iii) Low-NOx burner; (iv) Fuel selection/low-N fuel","mg /nm3",100,350,"Green","Continuous",0,0,0.06,"Yearly","When using gaseous fuels originating from vegetable matter (e.g. non-condensable gases), including those obtained as by-products of the pulping process, emission levels up to 450 mg/Nm3 (corresponding to 0,45 kg NOx/ADt) may occur.","PP (2014)\n2014/687/EU","1.2.2.3",26,26]
[535,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Gaseous fuels ","Lime kilns","Emissions to air","Air","NOx","Nitrogen dioxide","In order to reduce NOx emissions from a lime kiln, BAT is to apply a combination of the techniques given below: (i) Optimised combustion and combustion control; (ii) Good mixing of fuel and air; (iii) Low-NOx burner; (iv) Fuel selection/low-N fuel","kg NOx/Adt",0.1,0.3,"Green","Continuous",0,0,"Unspecified","Yearly","When using gaseous fuels originating from vegetable matter (e.g. non-condensable gases), including those obtained as by-products of the pulping process, emission levels up to 450 mg/Nm3 (corresponding to 0,45 kg NOx/ADt) may occur.","PP (2014)\n2014/687/EU","1.2.2.3",26,26]
[532,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Liquid fuels","Lime kilns","Emissions to air","Air","NOx","Nitrogen dioxide","In order to reduce NOx emissions from a lime kiln, BAT is to apply a combination of the techniques given below: (i) Optimised combustion and combustion control; (ii) Good mixing of fuel and air; (iii) Low-NOx burner; (iv) Fuel selection/low-N fuel","mg /nm3",100,200,"Green","Continuous",0,0,0.06,"Yearly","When using liquid fuels originating from vegetable matter (e.g. turpentine, methanol, tall-oil), including those obtained as by-products of the pulping process, emission levels up to 350 mg/Nm3 (corresponding to 0,35 kg NOx/ADt) may occur.","PP (2014)\n2014/687/EU","1.2.2.3",26,26]
[533,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Liquid fuels","Lime kilns","Emissions to air","Air","NOx","Nitrogen dioxide","In order to reduce NOx emissions from a lime kiln, BAT is to apply a combination of the techniques given below: (i) Optimised combustion and combustion control; (ii) Good mixing of fuel and air; (iii) Low-NOx burner; (iv) Fuel selection/low-N fuel","kg NOx/Adt",0.1,0.2,"Green","Continuous",0,0,"Unspecified","Yearly","When using liquid fuels originating from vegetable matter (e.g. turpentine, methanol, tall-oil), including those obtained as by-products of the pulping process, emission levels up to 350 mg/Nm3 (corresponding to 0,35 kg NOx/ADt) may occur.","PP (2014)\n2014/687/EU","1.2.2.3",26,26]
[543,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","TRS burner for strong odorous gases ","Emissions to air","Air","NOx","Nitrogen dioxide","In order to reduce NOx emissions from the incineration of strong odorous gases in a dedicated TRS burner, BAT is to use one or a combination of the techniques given below: (i) Burner/firing optimisation; (ii) Staged incineration","mg/Nm3",50,400,"Green","Continuous",0,0,0.09,"Yearly","Where at existing plants a switch to staged incineration is not feasible, emissions levels up to 1 000 mg/Nm3 (corresponding to 0,2 kg/ADt) may occur.","PP (2014)\n2014/687/EU","1.2.2.4",27,27]
[544,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","TRS burner for strong odorous gases ","Emissions to air","Air","NOx","Nitrogen dioxide","In order to reduce NOx emissions from the incineration of strong odorous gases in a dedicated TRS burner, BAT is to use one or a combination of the techniques given below: (i) Burner/firing optimisation; (ii) Staged incineration","kg NOx/Adt",0.01,0.1,"Green","Continuous",0,0,"Unspecified","Yearly","Where at existing plants a switch to staged incineration is not feasible, emissions levels up to 1 000 mg/Nm3 (corresponding to 0,2 kg/ADt) may occur.","PP (2014)\n2014/687/EU","1.2.2.4",27,27]
[558,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Recovery boiler","Emissions to air","Air","NOx ","Nitrogen dioxide","In order to reduce NOx emissions from a recovery boiler, BAT is to use an optimised firing system including one or a combination of the techniques given below: (i) Optimising the recovery boiler by controlling the firing conditions; (ii) Staged injection of spent liquor; (iii) Selective non-catalytic reduction (SNCR)","mg/Nm3",100,350,"Green","Continuous",0,0,0.05,"Daily","For ammonium-based mills, higher emission levels of NOx may occur: up to 580 mg/Nm3 as daily average and up to 450 mg/Nm3 as yearly average.","PP (2014)\n2014/687/EU","1.2.2.4",32,32]
[559,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Recovery boiler","Emissions to air","Air","NOx ","Nitrogen dioxide","In order to reduce NOx emissions from a recovery boiler, BAT is to use an optimised firing system including one or a combination of the techniques given below: (i) Optimising the recovery boiler by controlling the firing conditions; (ii) Staged injection of spent liquor; (iii) Selective non-catalytic reduction (SNCR)","mg/Nm3",100,270,"Green","Continuous",0,0,0.05,"Yearly","For ammonium-based mills, higher emission levels of NOx may occur: up to 580 mg/Nm3 as daily average and up to 450 mg/Nm3 as yearly average.","PP (2014)\n2014/687/EU","1.2.2.4",32,32]
[520,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Recovery boiler","Emissions to air","Air","NOx (Hardwood)","NOx (Hardwood)","In order to reduce NOx emissions from a recovery boiler, BAT is to use an optimised firing system including all of the features given below: (i) Computerised combustion control; (ii) Good mixing of fuel and air; (iii) Staged air feed systems, e.g. by using different air registers and air inlet ports","mg/Nm3",120,200,"Green","Continuous",0,0,0.06,"Yearly","Increasing the DS content of the black liquor results in lower SO2 emissions and higher NOx emissions. Due to this, a recovery boiler with low emission levels for SO2, may be on the higher end of the range for NOx and vice versa.\n\nThe actual NOx emission level of a recovery boiler depends on the DS content and the nitrogen content of the black liquor, and the amount and combination of NCG and other nitrogen containing flows (e.g. dissolving tank vent gas, methanol separated from the condensate, biosludge) burnt. The higher the DS content, the nitrogen content in the black liquor, and the amount of NCG and other nitrogen containing flows burnt, the closer the emissions will be to the upper end of the BAT-AEL range.","PP (2014)\n2014/687/EU","1.2.2.2",23,23]
[521,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Recovery boiler","Emissions to air","Air","NOx (Hardwood) DS < 75%","NOx (Hardwood) DS < 75%","In order to reduce NOx emissions from a recovery boiler, BAT is to use an optimised firing system including all of the features given below: (i) Computerised combustion control; (ii) Good mixing of fuel and air; (iii) Staged air feed systems, e.g. by using different air registers and air inlet ports","kg NOx/Adt",0.8,1.4,"Green","Continuous",0,0,"Unspecified","Yearly","Increasing the DS content of the black liquor results in lower SO2 emissions and higher NOx emissions. Due to this, a recovery boiler with low emission levels for SO2, may be on the higher end of the range for NOx and vice versa.\n\nIf a recovery boiler were to burn black liquor with a DS > 83 %, then NOx emission levels should be reconsidered on a case-by-case basis.","PP (2014)\n2014/687/EU","1.2.2.2",23,23]
[522,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Recovery boiler","Emissions to air","Air","NOx (Hardwood) DS 75-83%","NOx (Hardwood) DS 75-83%","In order to reduce NOx emissions from a recovery boiler, BAT is to use an optimised firing system including all of the features given below: (i) Computerised combustion control; (ii) Good mixing of fuel and air; (iii) Staged air feed systems, e.g. by using different air registers and air inlet ports","kg NOx/Adt",1,1.7,"Green","Continuous",0,0,"Unspecified","Yearly","Increasing the DS content of the black liquor results in lower SO2 emissions and higher NOx emissions. Due to this, a recovery boiler with low emission levels for SO2, may be on the higher end of the range for NOx and vice versa.\n\nIf a recovery boiler were to burn black liquor with a DS > 83 %, then NOx emission levels should be reconsidered on a case-by-case basis.","PP (2014)\n2014/687/EU","1.2.2.2",23,23]
[517,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Recovery boiler","Emissions to air","Air","NOx (softwood)","NOx (softwood)","In order to reduce NOx emissions from a recovery boiler, BAT is to use an optimised firing system including all of the features given below: (i) Computerised combustion control; (ii) Good mixing of fuel and air; (iii) Staged air feed systems, e.g. by using different air registers and air inlet ports","mg/Nm3",120,200,"Green","Continuous",0,0,0.06,"Yearly","Increasing the DS content of the black liquor results in lower SO2 emissions and higher NOx emissions. Due to this, a recovery boiler with low emission levels for SO2, may be on the higher end of the range for NOx and vice versa.\n\nThe actual NOx emission level of a recovery boiler depends on the DS content and the nitrogen content of the black liquor, and the amount and combination of NCG and other nitrogen containing flows (e.g. dissolving tank vent gas, methanol separated from the condensate, biosludge) burnt. The higher the DS content, the nitrogen content in the black liquor, and the amount of NCG and other nitrogen containing flows burnt, the closer the emissions will be to the upper end of the BAT-AEL range.","PP (2014)\n2014/687/EU","1.2.2.2",23,23]
[519,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Recovery boiler","Emissions to air","Air","NOx (softwood) DS 75- 83%","NOx (softwood) DS 75- 83%","In order to reduce NOx emissions from a recovery boiler, BAT is to use an optimised firing system including all of the features given below: (i) Computerised combustion control; (ii) Good mixing of fuel and air; (iii) Staged air feed systems, e.g. by using different air registers and air inlet ports","kg NOx/Adt",1,1.6,"Green","Continuous",0,0,"Unspecified","Yearly","Increasing the DS content of the black liquor results in lower SO2 emissions and higher NOx emissions. Due to this, a recovery boiler with low emission levels for SO2, may be on the higher end of the range for NOx and vice versa.\n\nIf a recovery boiler were to burn black liquor with a DS > 83 %, then NOx emission levels should be reconsidered on a case-by-case basis.","PP (2014)\n2014/687/EU","1.2.2.2",23,23]
[518,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Recovery boiler","Emissions to air","Air","NOx (softwood) DS< 75%","NOx (softwood) DS< 75%","In order to reduce NOx emissions from a recovery boiler, BAT is to use an optimised firing system including all of the features given below: (i) Computerised combustion control; (ii) Good mixing of fuel and air; (iii) Staged air feed systems, e.g. by using different air registers and air inlet ports","kg NOx/Adt",0.8,1.4,"Green","Continuous",0,0,"Unspecified","Yearly","Increasing the DS content of the black liquor results in lower SO2 emissions and higher NOx emissions. Due to this, a recovery boiler with low emission levels for SO2, may be on the higher end of the range for NOx and vice versa.","PP (2014)\n2014/687/EU","1.2.2.2",23,23]
[562,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Recovery boiler","Emissions to air","Air","SO2","Sulphur Dioxide (24 Hour Mean)","In order to reduce dust and SO2 emissions from a recovery boiler, BAT is to use one of the techniques given below and to limit ‘acid operation’ of the scrubbers to the minimum required to ensure their proper functioning: (i) ESP or multicyclones with multistage venturi scrubbers; (ii) ESP or multicyclones with multistage double inlet downstream scrubbers","mg/Nm3",100,300,"Green","Continuous",0,0,0.05,"Daily","Due to process-specific higher emissions, the BAT-AEL for SO2 does not apply for recovery boilers operated permanently under ‘acidic’ conditions, i.e. using sulphite liquor as wet-scrubber washing media as part of the sulphite recovery process.\n\n For existing multistage venturi scrubbers, higher emissions of SO2 up to 400 mg/Nm3 as a daily average value and up to 350 mg/Nm3 as a yearly average may occur.\n\nNot applicable during ‘acid operation’, i.e. periods in which preventive flushing and cleaning of incrustation in the scrubbers takes place. During these periods emissions can be up to 300 – 500 mg SO2/Nm3 (at 5 % O2) for cleaning of one of the scrubbers and up to 1 200 mg SO2/Nm3 (half-hourly mean values, at 5 % O2) when cleaning the final washer.","PP (2014)\n2014/687/EU","1.2.2.4",33,33]
[563,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Recovery boiler","Emissions to air","Air","SO2","Sulphur Dioxide (24 Hour Mean)","In order to reduce dust and SO2 emissions from a recovery boiler, BAT is to use one of the techniques given below and to limit ‘acid operation’ of the scrubbers to the minimum required to ensure their proper functioning: (i) ESP or multicyclones with multistage venturi scrubbers; (ii) ESP or multicyclones with multistage double inlet downstream scrubbers","mg/Nm3",50,250,"Green","Continuous",0,0,0.05,"Yearly","Due to process-specific higher emissions, the BAT-AEL for SO2 does not apply for recovery boilers operated permanently under ‘acidic’ conditions, i.e. using sulphite liquor as wet-scrubber washing media as part of the sulphite recovery process.\n\nFor existing multistage venturi scrubbers, higher emissions of SO2 up to 400 mg/Nm3 as a daily average value and up to 350 mg/Nm3 as a yearly average may occur.","PP (2014)\n2014/687/EU","1.2.2.4",33,33]
[540,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","TRS burner for strong odorous gases ","Emissions to air","Air","SO2","Sulphur Dioxide (24 Hour Mean)","In order to reduce SO2 emissions from the incineration of strong odorous gases in a dedicated TRS burner, BAT is to use an alkaline SO2 scrubber.","mg/Nm3",20,120,"Green","Continuous",0,0,0.09,"Yearly",0,"PP (2014)\n2014/687/EU","1.2.2.4",27,27]
[511,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Recovery boiler","Emissions to air","Air","SO2  DS < 75%","Sulphur Dioxide (24 Hour Mean)","In order to reduce SO2 and TRS emissions from a recovery boiler, BAT is to use a combination of the techniques given below: (i) Increasing the dry solids (DS) content of black liquor; (ii) Optimised firing; (iii) Wet scrubber","mg/Nm3",10,70,"Green","Continuous",0,0,0.06,"Daily","Increasing the DS content of the black liquor results in lower SO2 emissions and higher NOx emissions. Due to this, a recovery boiler with low emission levels for SO2, may be on the higher end of the range for NOx and vice versa.\n\nBAT-AELs do not cover periods during which the recovery boiler is run on a DS content much lower than the normal DS content due to shut down or maintenance of the black liquor concentration plant.","PP (2014)\n2014/687/EU","1.2.2.2",22,22]
[512,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Recovery boiler","Emissions to air","Air","SO2  DS < 75%","Sulphur Dioxide (24 Hour Mean)","In order to reduce SO2 and TRS emissions from a recovery boiler, BAT is to use a combination of the techniques given below: (i) Increasing the dry solids (DS) content of black liquor; (ii) Optimised firing; (iii) Wet scrubber","mg/Nm3",5,50,"Green","Continuous",0,0,0.06,"Yearly","Increasing the DS content of the black liquor results in lower SO2 emissions and higher NOx emissions. Due to this, a recovery boiler with low emission levels for SO2, may be on the higher end of the range for NOx and vice versa.","PP (2014)\n2014/687/EU","1.2.2.2",22,22]
[513,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Recovery boiler","Emissions to air","Air","SO2  DS 75-83%","Sulphur Dioxide (24 Hour Mean)","In order to reduce SO2 and TRS emissions from a recovery boiler, BAT is to use a combination of the techniques given below: (i) Increasing the dry solids (DS) content of black liquor; (ii) Optimised firing; (iii) Wet scrubber","mg/Nm3",10,50,"Green","Continuous",0,0,0.06,"Daily","Increasing the DS content of the black liquor results in lower SO2 emissions and higher NOx emissions. Due to this, a recovery boiler with low emission levels for SO2, may be on the higher end of the range for NOx and vice versa.\n\nBAT-AELs do not cover periods during which the recovery boiler is run on a DS content much lower than the normal DS content due to shut down or maintenance of the black liquor concentration plant.\n\nIf a recovery boiler were to burn black liquor with a DS > 83 %, then SO2 and gaseous S emission levels should be reconsidered on a case-by-case basis.","PP (2014)\n2014/687/EU","1.2.2.2",22,22]
[514,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Recovery boiler","Emissions to air","Air","SO2  DS 75-83%","Sulphur Dioxide (24 Hour Mean)","In order to reduce SO2 and TRS emissions from a recovery boiler, BAT is to use a combination of the techniques given below: (i) Increasing the dry solids (DS) content of black liquor; (ii) Optimised firing; (iii) Wet scrubber","mg/Nm3",5,25,"Green","Continuous",0,0,0.06,"Yearly","Increasing the DS content of the black liquor results in lower SO2 emissions and higher NOx emissions. Due to this, a recovery boiler with low emission levels for SO2, may be on the higher end of the range for NOx and vice versa.\n\nIf a recovery boiler were to burn black liquor with a DS > 83 %, then SO2 and gaseous S emission levels should be reconsidered on a case-by-case basis.","PP (2014)\n2014/687/EU","1.2.2.2",22,22]
[527,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Lime kilns","Emissions to air","Air","SO2 (when gases are not burnt in lime kiln) ","Sulphur Dioxide (24 Hour Mean)","In order to reduce SO2 emissions from a lime kiln, BAT is to apply one or a combination of the techniques given below: (i) Fuel selection/low sulphur fuel; (ii) Limit incineration of sulphur-containing odorous strong gases in the lime kiln; (iii) Control of Na2S content in lime mud feed; (iv) Alkaline scrubber\n","mg/Nm3",5,70,"Green","Continuous",0,0,0.06,"Yearly","‘strong gases’ includes methanol and turpentine","PP (2014)\n2014/687/EU","1.2.2.3",24,24]
[528,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Lime kilns","Emissions to air","Air","SO2 when strong gases are burnt in the lime kiln","Sulphur Dioxide (24 Hour Mean)","In order to reduce SO2 emissions from a lime kiln, BAT is to apply one or a combination of the techniques given below: (i) Fuel selection/low sulphur fuel; (ii) Limit incineration of sulphur-containing odorous strong gases in the lime kiln; (iii) Control of Na2S content in lime mud feed; (iv) Alkaline scrubber\n","mg/Nm3",55,120,"Green","Continuous",0,0,0.06,"Yearly","‘strong gases’ includes methanol and turpentine","PP (2014)\n2014/687/EU","1.2.2.3",25,25]
[531,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Lime kilns","Emissions to air","Air","Total Reduced Sulphur (TRS) ","Total Reduced Sulphur (TRS) ","In order to reduce TRS emissions from a lime kiln, BAT is to apply one or a combination of the techniques given below: (i) Control of the excess oxygen; (ii) Control of Na2S content in lime mud feed; (iii) Combination of ESP and alkaline scrubber","mg S/nm3",1,10,"Green","Unspeciified",0,0,0.06,"Yearly","For lime kilns burning strong gases (including methanol and turpentine), the upper end of the AEL range may be up to 40 mg/Nm3.","PP (2014)\n2014/687/EU","1.2.2.3",25,25]
[510,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Emissions to air","Air","Total Reduced Sulphur (TRS) ","Total Reduced Sulphur (TRS) ","In order to reduce odour emissions and total reduced sulphur emissions due to strong and weak odorous gases, BAT is to prevent diffuse emissions by capturing all process-based sulphur containing off-gases, including all vents with sulphur-containing emissions, by applying all of the techniques given below: (i) Collection systems for strong and weak odorous gases; (ii) Incineration of strong and weak non-condensable gases; (iii) Recording unavailability of the incineration system and any resulting emissions","kg S/Adt",0.05,0.2,"Green","Unspeciified",0,0,"Unspecified","Unspeciified",0,"PP (2014)\n2014/687/EU","1.2.2.1",22,22]
[541,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","TRS burner for strong odorous gases ","Emissions to air","Air","TRS","Total Reduced Sulphur (TRS) ","In order to reduce SO2 emissions from the incineration of strong odorous gases in a dedicated TRS burner, BAT is to use an alkaline SO2 scrubber.","mg/Nm3",1,5,"Green","Continuous",0,0,0.09,"Yearly",0,"PP (2014)\n2014/687/EU","1.2.2.4",27,27]
[591,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Excluding speciality paper ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Emissions to water","Water"," ","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.","kg/t","N/A",0.05,"Green","Once every 2 months",0,0,"Unspecified","Yearly",0,"PP (2014)\n2014/687/EU","1.6.1",41,41]
[505,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Bleached kraft pulp mill","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Emissions to water","Water","Adsorabable organically bound halogens (AOX)","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions of pollutants into receiving waters from the whole mill, BAT is to use TCF or modern ECF bleaching (see description in Section 1.7.2.1), and a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Modified cooking before bleaching; (ii) Oxygen delignification before bleaching; (iii) Closed brown stock screening and efficient brown stock washing; (iv) Partial process water recycling in the bleach plant; (v) Effective spill monitoring and containment with a suitable recovery system; (vi) Maintaining sufficient black liquor evaporation and recovery boiler capacity to cope with peak loads; (vii) Stripping the contaminated (foul) condensates and reusing the condensates in the process","kg/Adt",0,0.2,"Green","Monthly",0,0,"Unspecified","Yearly","The BAT-AEL ranges refer to market pulp production and the pulp production part of integrated mills (emissions from papermaking are not included).\n\nApplicable for mills using chlorine containing bleaching chemicals.\n\nFor mills producing pulp with high strength, stiffness and high purity properties (e.g. for liquid packaging board and LWC), emissions level of AOX up to 0,25 kg/ADt may occur.","PP (2014)\n2014/687/EU","1.2.1",20,20]
[553,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Bleached sulphite paper grade pulp   ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Pulp mill","Emissions to water","Water","Adsorbable organically bound halogens (AOX)","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce emissions of pollutants into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Extended modified cooking before bleaching.; (ii) Oxygen delignification before bleaching; (iii) Closed brown stock screening and efficient brown stock washing.; (iv) Evaporation of effluents from the hot alkaline extraction stage and incineration of concentrates in a soda boiler; (v) TCF bleaching; (vi) Closed-loop bleaching; (vii) MgO-based pre-bleaching and recirculation of washing liquids from pre- bleaching to brown stock washing; (viii) pH adjustment of weak liquor before/ inside the evaporation plant; (ix) Anaerobic treatment of the condensates from the evaporators; (x) Stripping and recovery of SO2 from the condensates of evaporators; (xi) Effective spill monitoring and containment, also with chemical and energy recovery system","mg/l",0.5,1.5,"Green","Once every 2 months",0,0,"Unspecified","Yearly","The BAT-AEL ranges refer to market pulp production and the pulp production part of integrated mills (emissions from papermaking are not included).\n\nThe BAT-AELs do not apply to natural greaseproof pulp mills).\n\nSulphite market pulp mills may apply a gentle ClO2 bleaching stage in order to meet product requirements, thus resulting in AOX emissions.\n\nNot applicable to TCF mills","PP (2014)\n2014/687/EU","1.2.2.4",30,30]
[596,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Excluding speciality paper ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Non-integrated speciality paper mill ","Emissions to water","Water","Adsorbable organically bound halogens (AOX)","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.","kg/t","N/A",0.05,"Green","Once every 2 months",0,0,"Unspecified","Yearly",0,"PP (2014)\n2014/687/EU","1.6.1",41,41]
[585,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Paper and board from recycled fibres pulp, produced with deinking on site ","Wet strength paper ","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Emissions to water","Water","Adsorbable organically bound halogens (AOX)","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.","kg/t","N/A",0.05,"Green","Once every 2 months",0,0,"Unspecified","Yearly",0,"PP (2014)\n2014/687/EU","1.5.2",38,38]
[576,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Paper and board from recycled fibres pulp, produced without deinking on site ","Wet strength paper ","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Emissions to water","Water","Adsorbable organically bound halogens (AOX)","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.","kg/t","N/A",0.05,"Green","Once every 2 months",0,0,"Unspecified","Yearly",0,"PP (2014)\n2014/687/EU","1.5.2",38,38]
[500,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Bleached kraft pulp mill","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Emissions to water","Water","Chemical Oxygen Demand (COD) ","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions of pollutants into receiving waters from the whole mill, BAT is to use TCF or modern ECF bleaching (see description in Section 1.7.2.1), and a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Modified cooking before bleaching; (ii) Oxygen delignification before bleaching; (iii) Closed brown stock screening and efficient brown stock washing; (iv) Partial process water recycling in the bleach plant; (v) Effective spill monitoring and containment with a suitable recovery system; (vi) Maintaining sufficient black liquor evaporation and recovery boiler capacity to cope with peak loads; (vii) Stripping the contaminated (foul) condensates and reusing the condensates in the process","kg/Adt",7,20,"Green","Daily",0,0,"Unspecified","Yearly","The BAT-AEL ranges refer to market pulp production and the pulp production part of integrated mills (emissions from papermaking are not included).","PP (2014)\n2014/687/EU","1.2.1",20,20]
[545,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Bleached sulphite paper grade pulp   ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Pulp mill","Emissions to water","Water","Chemical Oxygen Demand (COD) ","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce emissions of pollutants into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Extended modified cooking before bleaching.; (ii) Oxygen delignification before bleaching; (iii) Closed brown stock screening and efficient brown stock washing.; (iv) Evaporation of effluents from the hot alkaline extraction stage and incineration of concentrates in a soda boiler; (v) TCF bleaching; (vi) Closed-loop bleaching; (vii) MgO-based pre-bleaching and recirculation of washing liquids from pre- bleaching to brown stock washing; (viii) pH adjustment of weak liquor before/ inside the evaporation plant; (ix) Anaerobic treatment of the condensates from the evaporators; (x) Stripping and recovery of SO2 from the condensates of evaporators; (xi) Effective spill monitoring and containment, also with chemical and energy recovery system","kg/ADt",10,30,"Green","Daily",0,0,"Unspecified","Yearly","The BAT-AEL ranges refer to market pulp production and the pulp production part of integrated mills (emissions from papermaking are not included).\n\nThe BAT-AELs do not apply to natural greaseproof pulp mills).\n\nThe BAT-AEL for COD and total phosphorus do not apply to eucalyptus based market pulp","PP (2014)\n2014/687/EU","1.2.2.4",30,30]
[586,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Excluding speciality paper ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Emissions to water","Water","Chemical Oxygen Demand (COD) ","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.","kg/t",0.15,1.5,"Green","Daily",0,0,"Unspecified","Yearly","For graphic paper mills, the upper end of the range refers to mills manufacturing paper that use starch for the coating process.","PP (2014)\n2014/687/EU","1.6.1",41,41]
[592,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Excluding speciality paper ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Non-integrated speciality paper mill ","Emissions to water","Water","Chemical Oxygen Demand (COD) ","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.","kg/t",0.3,5,"Green","Daily",0,0,"Unspecified","Yearly","Mills having special characteristics, such as a high number of grade changes (e.g. of ≥ 5 per day as a yearly average) or producing very light-weight speciality papers (≤ 30 g/m2 as yearly average) might have higher emissions than the upper end of the range.\n\nThe upper end of the BAT-AEL range refers to mills producing highly comminuted paper which requires intensive refining and to mills with frequent changes of paper grades (e.g. ≥ 1 – 2 changes/day as yearly average).","PP (2014)\n2014/687/EU","1.6.1",41,41]
[546,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Magnefite paper grade pulp","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Pulp mill","Emissions to water","Water","Chemical Oxygen Demand (COD) ","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce emissions of pollutants into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Extended modified cooking before bleaching.; (ii) Oxygen delignification before bleaching; (iii) Closed brown stock screening and efficient brown stock washing.; (iv) Evaporation of effluents from the hot alkaline extraction stage and incineration of concentrates in a soda boiler; (v) TCF bleaching; (vi) Closed-loop bleaching; (vii) MgO-based pre-bleaching and recirculation of washing liquids from pre- bleaching to brown stock washing; (viii) pH adjustment of weak liquor before/ inside the evaporation plant; (ix) Anaerobic treatment of the condensates from the evaporators; (x) Stripping and recovery of SO2 from the condensates of evaporators; (xi) Effective spill monitoring and containment, also with chemical and energy recovery system","kg/ADt",20,35,"Green","Daily",0,0,"Unspecified","Yearly","The BAT-AEL ranges refer to market pulp production and the pulp production part of integrated mills (emissions from papermaking are not included).","PP (2014)\n2014/687/EU","1.2.2.4",30,30]
[554,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","NSSC pulp","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Sulphite pulp mill","Emissions to water","Water","Chemical Oxygen Demand (COD) ","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce emissions of pollutants into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Extended modified cooking before bleaching.; (ii) Oxygen delignification before bleaching; (iii) Closed brown stock screening and efficient brown stock washing.; (iv) Evaporation of effluents from the hot alkaline extraction stage and incineration of concentrates in a soda boiler; (v) TCF bleaching; (vi) Closed-loop bleaching; (vii) MgO-based pre-bleaching and recirculation of washing liquids from pre- bleaching to brown stock washing; (viii) pH adjustment of weak liquor before/ inside the evaporation plant; (ix) Anaerobic treatment of the condensates from the evaporators; (x) Stripping and recovery of SO2 from the condensates of evaporators; (xi) Effective spill monitoring and containment, also with chemical and energy recovery system","kg/ADt",3.2,11,"Green","Daily",0,0,"Unspecified","Yearly","The BAT-AEL ranges refer to market pulp production and the pulp production part of integrated mills (emissions from papermaking are not included).","PP (2014)\n2014/687/EU","1.2.2.4",31,31]
[564,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Paper and board","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Mechanical pulps prdouced on site ","Emissions to water","Water","Chemical Oxygen Demand (COD) ","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce fresh water use, waste water flow, and the pollution load, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Counter-current flow of process water and separation of water systems; (ii) High consistency bleaching.; (iii) Washing stage before the refining of softwood mechanical pulp using chip pre-treatment; (iv) Substitution of NaOH by Ca(OH)2 or Mg(OH)2 as alkali in peroxide bleaching; (v) Fibre and filler recovery and treatment of white water (papermaking); (vi) Optimum design and construction of tanks and chests (papermaking).","kg/ADt",12,20,"Green","Daily",0,0,"Unspecified","Yearly","In the case of highly bleached mechanical pulp (70-100 % of fibre in final paper), emission levels of up to 8 kg/t may occur.","PP (2014)\n2014/687/EU","1.4.1",35,35]
[578,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Paper and board from recycled fibres pulp, produced with deinking on site ","Tissue Paper","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Emissions to water","Water","Chemical Oxygen Demand (COD) ","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.","kg/t",0.9,4,"Green","Daily",0,0,"Unspecified","Yearly",0,"PP (2014)\n2014/687/EU","1.5.2",38,38]
[577,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Paper and board from recycled fibres pulp, produced with deinking on site ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Emissions to water","Water","Chemical Oxygen Demand (COD) ","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.","kg/t",0.9,3,"Green","Daily",0,0,"Unspecified","Yearly",0,"PP (2014)\n2014/687/EU","1.5.2",38,38]
[572,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Paper and board from recycled fibres pulp, produced without deinking on site ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Emissions to water","Water","Chemical Oxygen Demand (COD) ","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.","kg/t",0.4,1.4,"Green","Daily",0,0,"Unspecified","Yearly",0,"PP (2014)\n2014/687/EU","1.5.2",38,38]
[506,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Unbleached fraft pulp mill","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Emissions to water","Water","Chemical Oxygen Demand (COD) ","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions of pollutants into receiving waters from the whole mill, BAT is to use TCF or modern ECF bleaching (see description in Section 1.7.2.1), and a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Modified cooking before bleaching; (ii) Oxygen delignification before bleaching; (iii) Closed brown stock screening and efficient brown stock washing; (iv) Partial process water recycling in the bleach plant; (v) Effective spill monitoring and containment with a suitable recovery system; (vi) Maintaining sufficient black liquor evaporation and recovery boiler capacity to cope with peak loads; (vii) Stripping the contaminated (foul) condensates and reusing the condensates in the process","kg/ADt",2.5,8,"Green","Daily",0,0,"Unspecified","Yearly","The BAT-AEL ranges refer to market pulp production and the pulp production part of integrated mills (emissions from papermaking are not included).","PP (2014)\n2014/687/EU","1.2.1",21,21]
[568,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","CTMP or CMP pulp mill","Emissions to water","Water","Chemical Oxygen Demand (COD) ","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce fresh water use, waste water flow, and the pollution load, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Counter-current flow of process water and separation of water systems; (ii) High consistency bleaching.; (iii) Washing stage before the refining of softwood mechanical pulp using chip pre-treatment; (iv) Substitution of NaOH by Ca(OH)2 or Mg(OH)2 as alkali in peroxide bleaching; (v) Fibre and filler recovery and treatment of white water (papermaking); (vi) Optimum design and construction of tanks and chests (papermaking).","kg/ADt",12,20,"Green","Daily",0,0,"Unspecified","Yearly",0,"PP (2014)\n2014/687/EU","1.4.1",35,35]
[549,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Bleached sulphite paper grade pulp   ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Pulp mill","Emissions to water","Water","Total  Nitrogen","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce emissions of pollutants into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Extended modified cooking before bleaching.; (ii) Oxygen delignification before bleaching; (iii) Closed brown stock screening and efficient brown stock washing.; (iv) Evaporation of effluents from the hot alkaline extraction stage and incineration of concentrates in a soda boiler; (v) TCF bleaching; (vi) Closed-loop bleaching; (vii) MgO-based pre-bleaching and recirculation of washing liquids from pre- bleaching to brown stock washing; (viii) pH adjustment of weak liquor before/ inside the evaporation plant; (ix) Anaerobic treatment of the condensates from the evaporators; (x) Stripping and recovery of SO2 from the condensates of evaporators; (xi) Effective spill monitoring and containment, also with chemical and energy recovery system","kg/ADt",0.15,3,"Green","Weekly",0,0,"Unspecified","Yearly","The BAT-AEL ranges refer to market pulp production and the pulp production part of integrated mills (emissions from papermaking are not included).\n\nThe BAT-AELs do not apply to natural greaseproof pulp mills).","PP (2014)\n2014/687/EU","1.2.2.4",30,30]
[550,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Magnefite paper grade pulp","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Pulp mill","Emissions to water","Water","Total  Nitrogen","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce emissions of pollutants into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Extended modified cooking before bleaching.; (ii) Oxygen delignification before bleaching; (iii) Closed brown stock screening and efficient brown stock washing.; (iv) Evaporation of effluents from the hot alkaline extraction stage and incineration of concentrates in a soda boiler; (v) TCF bleaching; (vi) Closed-loop bleaching; (vii) MgO-based pre-bleaching and recirculation of washing liquids from pre- bleaching to brown stock washing; (viii) pH adjustment of weak liquor before/ inside the evaporation plant; (ix) Anaerobic treatment of the condensates from the evaporators; (x) Stripping and recovery of SO2 from the condensates of evaporators; (xi) Effective spill monitoring and containment, also with chemical and energy recovery system","kg/ADt",0.1,0.25,"Green","Weekly",0,0,"Unspecified","Yearly","The BAT-AEL ranges refer to market pulp production and the pulp production part of integrated mills (emissions from papermaking are not included).","PP (2014)\n2014/687/EU","1.2.2.4",30,30]
[502,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Bleached kraft pulp mill","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Emissions to water","Water","Total nitrogen","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions of pollutants into receiving waters from the whole mill, BAT is to use TCF or modern ECF bleaching (see description in Section 1.7.2.1), and a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Modified cooking before bleaching; (ii) Oxygen delignification before bleaching; (iii) Closed brown stock screening and efficient brown stock washing; (iv) Partial process water recycling in the bleach plant; (v) Effective spill monitoring and containment with a suitable recovery system; (vi) Maintaining sufficient black liquor evaporation and recovery boiler capacity to cope with peak loads; (vii) Stripping the contaminated (foul) condensates and reusing the condensates in the process","kg/Adt",0.05,0.25,"Green","Weekly",0,0,"Unspecified","Yearly","The BAT-AEL ranges refer to market pulp production and the pulp production part of integrated mills (emissions from papermaking are not included).\n\nA compact biological waste water treatment plant can result in slightly higher emission levels.","PP (2014)\n2014/687/EU","1.2.1",20,20]
[588,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Excluding speciality paper ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Emissions to water","Water","Total nitrogen","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.","kg/t",0.01,0.1,"Green","Weekly",0,0,"Unspecified","Yearly",0,"PP (2014)\n2014/687/EU","1.6.1",41,41]
[594,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Excluding speciality paper ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Non-integrated speciality paper mill ","Emissions to water","Water","Total nitrogen","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.","kg/t",1.4999999999999999E-2,0.4,"Green","Weekly",0,0,"Unspecified","Yearly",0,"PP (2014)\n2014/687/EU","1.6.1",41,41]
[556,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","NSSC pulp","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Sulphite pulp mill","Emissions to water","Water","Total nitrogen","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce emissions of pollutants into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Extended modified cooking before bleaching.; (ii) Oxygen delignification before bleaching; (iii) Closed brown stock screening and efficient brown stock washing.; (iv) Evaporation of effluents from the hot alkaline extraction stage and incineration of concentrates in a soda boiler; (v) TCF bleaching; (vi) Closed-loop bleaching; (vii) MgO-based pre-bleaching and recirculation of washing liquids from pre- bleaching to brown stock washing; (viii) pH adjustment of weak liquor before/ inside the evaporation plant; (ix) Anaerobic treatment of the condensates from the evaporators; (x) Stripping and recovery of SO2 from the condensates of evaporators; (xi) Effective spill monitoring and containment, also with chemical and energy recovery system","kg/ADt",0.1,0.2,"Green","Weekly",0,0,"Unspecified","Yearly","The BAT-AEL ranges refer to market pulp production and the pulp production part of integrated mills (emissions from papermaking are not included).\n\nDue to process-specific higher emissions, the BAT-AEL for total nitrogen does not apply to ammonium-based NSSC pulping.","PP (2014)\n2014/687/EU","1.2.2.4",31,31]
[566,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Paper and board","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Mechanical pulps prdouced on site ","Emissions to water","Water","Total nitrogen","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce fresh water use, waste water flow, and the pollution load, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Counter-current flow of process water and separation of water systems; (ii) High consistency bleaching.; (iii) Washing stage before the refining of softwood mechanical pulp using chip pre-treatment; (iv) Substitution of NaOH by Ca(OH)2 or Mg(OH)2 as alkali in peroxide bleaching; (v) Fibre and filler recovery and treatment of white water (papermaking); (vi) Optimum design and construction of tanks and chests (papermaking).","kg/ADt",0.15,0.18,"Green","Weekly",0,0,"Unspecified","Yearly","When biodegradable or eliminable chelating agents cannot be used due to pulp quality requirements (e.g. high brightness), the emissions of total nitrogen might be higher than this BAT-AEL and should be assessed on a case-by-case basis.","PP (2014)\n2014/687/EU","1.4.1",35,35]
[582,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Paper and board from recycled fibres pulp, produced with deinking on site ","Tissue Paper","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Emissions to water","Water","Total nitrogen","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.","kg/t",0.01,0.15,"Green","Weekly",0,0,"Unspecified","Yearly",0,"PP (2014)\n2014/687/EU","1.5.2",38,38]
[581,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Paper and board from recycled fibres pulp, produced with deinking on site ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Emissions to water","Water","Total nitrogen","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.","kg/t",0.01,0.1,"Green","Weekly",0,0,"Unspecified","Yearly",0,"PP (2014)\n2014/687/EU","1.5.2",38,38]
[574,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Paper and board from recycled fibres pulp, produced without deinking on site ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Emissions to water","Water","Total nitrogen","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.","kg/t",8.0000000000000002E-3,0.09,"Green","Weekly",0,0,"Unspecified","Yearly",0,"PP (2014)\n2014/687/EU","1.5.2",38,38]
[589,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Tissue paper (excluding speciality paper)","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Emissions to water","Water","Total nitrogen","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.",0,0.01,0.15,"Green","Weekly",0,0,"Unspecified","Yearly",0,"PP (2014)\n2014/687/EU","1.6.1",41,41]
[508,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Unbleached fraft pulp mill","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Emissions to water","Water","Total nitrogen","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions of pollutants into receiving waters from the whole mill, BAT is to use TCF or modern ECF bleaching (see description in Section 1.7.2.1), and a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Modified cooking before bleaching; (ii) Oxygen delignification before bleaching; (iii) Closed brown stock screening and efficient brown stock washing; (iv) Partial process water recycling in the bleach plant; (v) Effective spill monitoring and containment with a suitable recovery system; (vi) Maintaining sufficient black liquor evaporation and recovery boiler capacity to cope with peak loads; (vii) Stripping the contaminated (foul) condensates and reusing the condensates in the process","kg/ADt",0.1,0.2,"Green","Weekly",0,0,"Unspecified","Yearly","The BAT-AEL ranges refer to market pulp production and the pulp production part of integrated mills (emissions from papermaking are not included).\n\nA compact biological waste water treatment plant can result in slightly higher emission levels.","PP (2014)\n2014/687/EU","1.2.1",21,21]
[570,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","CTMP or CMP pulp mill","Emissions to water","Water","Total nitrogen","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce fresh water use, waste water flow, and the pollution load, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Counter-current flow of process water and separation of water systems; (ii) High consistency bleaching.; (iii) Washing stage before the refining of softwood mechanical pulp using chip pre-treatment; (iv) Substitution of NaOH by Ca(OH)2 or Mg(OH)2 as alkali in peroxide bleaching; (v) Fibre and filler recovery and treatment of white water (papermaking); (vi) Optimum design and construction of tanks and chests (papermaking).","kg/ADt",0.15,0.18,"Green","Weekly",0,0,"Unspecified","Yearly","When biodegradable or eliminable chelating agents cannot be used due to pulp quality requirements (e.g. high brightness), the emissions of total nitrogen might be higher than this BAT- AEL and should be assessed on a case-by-case basis.","PP (2014)\n2014/687/EU","1.4.1",35,35]
[503,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Bleached kraft pulp mill","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Emissions to water","Water","Total phosphorous","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions of pollutants into receiving waters from the whole mill, BAT is to use TCF or modern ECF bleaching (see description in Section 1.7.2.1), and a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Modified cooking before bleaching; (ii) Oxygen delignification before bleaching; (iii) Closed brown stock screening and efficient brown stock washing; (iv) Partial process water recycling in the bleach plant; (v) Effective spill monitoring and containment with a suitable recovery system; (vi) Maintaining sufficient black liquor evaporation and recovery boiler capacity to cope with peak loads; (vii) Stripping the contaminated (foul) condensates and reusing the condensates in the process","kg/Adt","0.01\n","0.03\n","Green","Weekly",0,0,"Unspecified","Yearly","The BAT-AEL ranges refer to market pulp production and the pulp production part of integrated mills (emissions from papermaking are not included).\n\nA compact biological waste water treatment plant can result in slightly higher emission levels.\n\nThe upper end of the range refers to mills using eucalyptus from regions with higher levels of phosphorus (e.g. Iberian eucalyptus).","PP (2014)\n2014/687/EU","1.2.1",20,20]
[504,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Bleached kraft pulp mill","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Emissions to water","Water","Total phosphorous","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions of pollutants into receiving waters from the whole mill, BAT is to use TCF or modern ECF bleaching (see description in Section 1.7.2.1), and a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Modified cooking before bleaching; (ii) Oxygen delignification before bleaching; (iii) Closed brown stock screening and efficient brown stock washing; (iv) Partial process water recycling in the bleach plant; (v) Effective spill monitoring and containment with a suitable recovery system; (vi) Maintaining sufficient black liquor evaporation and recovery boiler capacity to cope with peak loads; (vii) Stripping the contaminated (foul) condensates and reusing the condensates in the process","kg/Adt",0.02,0.11,"Green","Weekly",0,0,"Unspecified","Yearly"," The BAT-AEL ranges refer to market pulp production and the pulp production part of integrated mills (emissions from\npapermaking are not included).\n\nThe upper end of the range refers to mills using eucalyptus from regions with higher levels of phosphorus (e.g. Iberian\neucalyptus). ",0,0,0,0]
[551,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Bleached sulphite paper grade pulp   ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Pulp mill","Emissions to water","Water","Total phosphorous","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce emissions of pollutants into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Extended modified cooking before bleaching.; (ii) Oxygen delignification before bleaching; (iii) Closed brown stock screening and efficient brown stock washing.; (iv) Evaporation of effluents from the hot alkaline extraction stage and incineration of concentrates in a soda boiler; (v) TCF bleaching; (vi) Closed-loop bleaching; (vii) MgO-based pre-bleaching and recirculation of washing liquids from pre- bleaching to brown stock washing; (viii) pH adjustment of weak liquor before/ inside the evaporation plant; (ix) Anaerobic treatment of the condensates from the evaporators; (x) Stripping and recovery of SO2 from the condensates of evaporators; (xi) Effective spill monitoring and containment, also with chemical and energy recovery system","kg/ADt",0.01,0.05,"Green","Weekly",0,0,"Unspecified","Yearly","The BAT-AEL ranges refer to market pulp production and the pulp production part of integrated mills (emissions from papermaking are not included).\n\nThe BAT-AELs do not apply to natural greaseproof pulp mills).\n\nThe BAT-AEL for COD and total phosphorus do not apply to eucalyptus based market pulp","PP (2014)\n2014/687/EU","1.2.2.4",30,30]
[590,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Excluding speciality paper ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Emissions to water","Water","Total phosphorous","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.","kg/t",3.0000000000000001E-3,1.2E-2,"Green","Weekly",0,0,"Unspecified","Yearly",0,"PP (2014)\n2014/687/EU","1.6.1",41,41]
[595,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Excluding speciality paper ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Non-integrated speciality paper mill ","Emissions to water","Water","Total phosphorous","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.","kg/t",2E-3,0.04,"Green","Weekly",0,0,"Unspecified","Yearly",0,"PP (2014)\n2014/687/EU","1.6.1",41,41]
[552,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Magnefite paper grade pulp","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Pulp mill","Emissions to water","Water","Total phosphorous","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce emissions of pollutants into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Extended modified cooking before bleaching.; (ii) Oxygen delignification before bleaching; (iii) Closed brown stock screening and efficient brown stock washing.; (iv) Evaporation of effluents from the hot alkaline extraction stage and incineration of concentrates in a soda boiler; (v) TCF bleaching; (vi) Closed-loop bleaching; (vii) MgO-based pre-bleaching and recirculation of washing liquids from pre- bleaching to brown stock washing; (viii) pH adjustment of weak liquor before/ inside the evaporation plant; (ix) Anaerobic treatment of the condensates from the evaporators; (x) Stripping and recovery of SO2 from the condensates of evaporators; (xi) Effective spill monitoring and containment, also with chemical and energy recovery system","kg/ADt",0.01,7.0000000000000007E-2,"Green","Weekly",0,0,"Unspecified","Yearly","The BAT-AEL ranges refer to market pulp production and the pulp production part of integrated mills (emissions from papermaking are not included).","PP (2014)\n2014/687/EU","1.2.2.4",30,30]
[557,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","NSSC pulp","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Sulphite pulp mill","Emissions to water","Water","Total phosphorous","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce emissions of pollutants into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Extended modified cooking before bleaching.; (ii) Oxygen delignification before bleaching; (iii) Closed brown stock screening and efficient brown stock washing.; (iv) Evaporation of effluents from the hot alkaline extraction stage and incineration of concentrates in a soda boiler; (v) TCF bleaching; (vi) Closed-loop bleaching; (vii) MgO-based pre-bleaching and recirculation of washing liquids from pre- bleaching to brown stock washing; (viii) pH adjustment of weak liquor before/ inside the evaporation plant; (ix) Anaerobic treatment of the condensates from the evaporators; (x) Stripping and recovery of SO2 from the condensates of evaporators; (xi) Effective spill monitoring and containment, also with chemical and energy recovery system","kg/ADt",0.01,0.02,"Green","Weekly",0,0,"Unspecified","Yearly","The BAT-AEL ranges refer to market pulp production and the pulp production part of integrated mills (emissions from papermaking are not included).","PP (2014)\n2014/687/EU","1.2.2.4",31,31]
[567,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Paper and board from mechanical pupls produced on site","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Emissions to water","Water","Total phosphorous","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce fresh water use, waste water flow, and the pollution load, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Counter-current flow of process water and separation of water systems; (ii) High consistency bleaching.; (iii) Washing stage before the refining of softwood mechanical pulp using chip pre-treatment; (iv) Substitution of NaOH by Ca(OH)2 or Mg(OH)2 as alkali in peroxide bleaching; (v) Fibre and filler recovery and treatment of white water (papermaking); (vi) Optimum design and construction of tanks and chests (papermaking).","kg/ADt",1E-3,0.01,"Green","Weekly",0,0,"Unspecified","Yearly",0,"PP (2014)\n2014/687/EU","1.4.1",35,35]
[584,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Paper and board from recycled fibres pulp, produced with deinking on site ","Tissue Paper","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Emissions to water","Water","Total phosphorous","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.","kg/t",2E-3,1.4999999999999999E-2,"Green","Weekly",0,0,"Unspecified","Yearly",0,"PP (2014)\n2014/687/EU","1.5.2",38,38]
[583,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Paper and board from recycled fibres pulp, produced with deinking on site ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Emissions to water","Water","Total phosphorous","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.","kg/t",2E-3,0.01,"Green","Weekly",0,0,"Unspecified","Yearly",0,"PP (2014)\n2014/687/EU","1.5.2",38,38]
[575,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Paper and board from recycled fibres pulp, produced without deinking on site ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Emissions to water","Water","Total phosphorous","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.","kg/t",1E-3,5.0000000000000001E-3,"Green","Weekly",0,0,"Unspecified","Yearly","For mills with a waste water flow between 5 and 10 m3/t, the upper end of the range is 0,008 kg/t.","PP (2014)\n2014/687/EU","1.5.2",38,38]
[509,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Unbleached fraft pulp mill","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Emissions to water","Water","Total phosphorous","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions of pollutants into receiving waters from the whole mill, BAT is to use TCF or modern ECF bleaching (see description in Section 1.7.2.1), and a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Modified cooking before bleaching; (ii) Oxygen delignification before bleaching; (iii) Closed brown stock screening and efficient brown stock washing; (iv) Partial process water recycling in the bleach plant; (v) Effective spill monitoring and containment with a suitable recovery system; (vi) Maintaining sufficient black liquor evaporation and recovery boiler capacity to cope with peak loads; (vii) Stripping the contaminated (foul) condensates and reusing the condensates in the process","kg/ADt",0.01,0.02,"Green","Weekly",0,0,"Unspecified","Yearly","The BAT-AEL ranges refer to market pulp production and the pulp production part of integrated mills (emissions from papermaking are not included).\n\nA compact biological waste water treatment plant can result in slightly higher emission levels.","PP (2014)\n2014/687/EU","1.2.1",21,21]
[571,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","CTMP or CMP pulp mill","Emissions to water","Water","Total phosphorous","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce fresh water use, waste water flow, and the pollution load, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Counter-current flow of process water and separation of water systems; (ii) High consistency bleaching.; (iii) Washing stage before the refining of softwood mechanical pulp using chip pre-treatment; (iv) Substitution of NaOH by Ca(OH)2 or Mg(OH)2 as alkali in peroxide bleaching; (v) Fibre and filler recovery and treatment of white water (papermaking); (vi) Optimum design and construction of tanks and chests (papermaking).","kg/ADt",1E-3,0.01,"Green","Weekly",0,0,"Unspecified","Yearly",0,"PP (2014)\n2014/687/EU","1.4.1",35,35]
[501,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Bleached kraft pulp mill","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Emissions to water","Water","Total Suspended Solids (TSS) ","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions of pollutants into receiving waters from the whole mill, BAT is to use TCF or modern ECF bleaching (see description in Section 1.7.2.1), and a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Modified cooking before bleaching; (ii) Oxygen delignification before bleaching; (iii) Closed brown stock screening and efficient brown stock washing; (iv) Partial process water recycling in the bleach plant; (v) Effective spill monitoring and containment with a suitable recovery system; (vi) Maintaining sufficient black liquor evaporation and recovery boiler capacity to cope with peak loads; (vii) Stripping the contaminated (foul) condensates and reusing the condensates in the process","kg/Adt",0.3,1.5,"Green","Daily",0,0,"Unspecified","Yearly","The BAT-AEL ranges refer to market pulp production and the pulp production part of integrated mills (emissions from papermaking are not included).","PP (2014)\n2014/687/EU","1.2.1",20,20]
[547,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Bleached sulphite paper grade pulp   ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Pulp mill","Emissions to water","Water","Total Suspended Solids (TSS) ","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce emissions of pollutants into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Extended modified cooking before bleaching.; (ii) Oxygen delignification before bleaching; (iii) Closed brown stock screening and efficient brown stock washing.; (iv) Evaporation of effluents from the hot alkaline extraction stage and incineration of concentrates in a soda boiler; (v) TCF bleaching; (vi) Closed-loop bleaching; (vii) MgO-based pre-bleaching and recirculation of washing liquids from pre- bleaching to brown stock washing; (viii) pH adjustment of weak liquor before/ inside the evaporation plant; (ix) Anaerobic treatment of the condensates from the evaporators; (x) Stripping and recovery of SO2 from the condensates of evaporators; (xi) Effective spill monitoring and containment, also with chemical and energy recovery system","kg/ADt",0.4,1.5,"Green","Daily",0,0,"Unspecified","Yearly","The BAT-AEL ranges refer to market pulp production and the pulp production part of integrated mills (emissions from papermaking are not included).\n\nThe BAT-AELs do not apply to natural greaseproof pulp mills).","PP (2014)\n2014/687/EU","1.2.2.4",30,30]
[587,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Excluding speciality paper ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Emissions to water","Water","Total Suspended Solids (TSS) ","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.","kg/t",0.02,0.35,"Green","Daily",0,0,"Unspecified","Yearly",0,"PP (2014)\n2014/687/EU","1.6.1",41,41]
[593,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Excluding speciality paper ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Non-integrated speciality paper mill ","Emissions to water","Water","Total Suspended Solids (TSS) ","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.","kg/t",0.1,1,"Green","Daily",0,0,"Unspecified","Yearly",0,"PP (2014)\n2014/687/EU","1.6.1",41,41]
[548,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Magnefite paper grade pulp","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Pulp mill","Emissions to water","Water","Total Suspended Solids (TSS) ","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce emissions of pollutants into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Extended modified cooking before bleaching.; (ii) Oxygen delignification before bleaching; (iii) Closed brown stock screening and efficient brown stock washing.; (iv) Evaporation of effluents from the hot alkaline extraction stage and incineration of concentrates in a soda boiler; (v) TCF bleaching; (vi) Closed-loop bleaching; (vii) MgO-based pre-bleaching and recirculation of washing liquids from pre- bleaching to brown stock washing; (viii) pH adjustment of weak liquor before/ inside the evaporation plant; (ix) Anaerobic treatment of the condensates from the evaporators; (x) Stripping and recovery of SO2 from the condensates of evaporators; (xi) Effective spill monitoring and containment, also with chemical and energy recovery system","kg/ADt",0.5,2,"Green","Daily",0,0,"Unspecified","Yearly","The BAT-AEL ranges refer to market pulp production and the pulp production part of integrated mills (emissions from papermaking are not included).","PP (2014)\n2014/687/EU","1.2.2.4",30,30]
[555,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","NSSC pulp","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Sulphite pulp mill","Emissions to water","Water","Total Suspended Solids (TSS) ","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce emissions of pollutants into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Extended modified cooking before bleaching.; (ii) Oxygen delignification before bleaching; (iii) Closed brown stock screening and efficient brown stock washing.; (iv) Evaporation of effluents from the hot alkaline extraction stage and incineration of concentrates in a soda boiler; (v) TCF bleaching; (vi) Closed-loop bleaching; (vii) MgO-based pre-bleaching and recirculation of washing liquids from pre- bleaching to brown stock washing; (viii) pH adjustment of weak liquor before/ inside the evaporation plant; (ix) Anaerobic treatment of the condensates from the evaporators; (x) Stripping and recovery of SO2 from the condensates of evaporators; (xi) Effective spill monitoring and containment, also with chemical and energy recovery system","kg/ADt",0.5,1.3,"Green","Daily",0,0,"Unspecified","Yearly","The BAT-AEL ranges refer to market pulp production and the pulp production part of integrated mills (emissions from papermaking are not included).","PP (2014)\n2014/687/EU","1.2.2.4",31,31]
[565,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Paper and board","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Mechanical pulps prdouced on site ","Emissions to water","Water","Total Suspended Solids (TSS) ","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce fresh water use, waste water flow, and the pollution load, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Counter-current flow of process water and separation of water systems; (ii) High consistency bleaching.; (iii) Washing stage before the refining of softwood mechanical pulp using chip pre-treatment; (iv) Substitution of NaOH by Ca(OH)2 or Mg(OH)2 as alkali in peroxide bleaching; (v) Fibre and filler recovery and treatment of white water (papermaking); (vi) Optimum design and construction of tanks and chests (papermaking).","kg/ADt",0.5,0.9,"Green","Daily",0,0,"Unspecified","Yearly",0,"PP (2014)\n2014/687/EU","1.4.1",35,35]
[580,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Paper and board from recycled fibres pulp, produced with deinking on site ","Tissue Paper","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Emissions to water","Water","Total Suspended Solids (TSS) ","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.","kg/t",0.1,0.4,"Green","Daily",0,0,"Unspecified","Yearly",0,"PP (2014)\n2014/687/EU","1.5.2",38,38]
[579,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Paper and board from recycled fibres pulp, produced with deinking on site ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Emissions to water","Water","Total Suspended Solids (TSS) ","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.","kg/t",0.08,0.3,"Green","Daily",0,0,"Unspecified","Yearly",0,"PP (2014)\n2014/687/EU","1.5.2",38,38]
[573,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Paper and board from recycled fibres pulp, produced without deinking on site ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Emissions to water","Water","Total Suspended Solids (TSS) ","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.","kg/t",0.02,0.2,"Green","Daily",0,0,"Unspecified","Yearly","For existing plants, levels up to 0,45 kg/t may occur, due to the continuous decline in the quality of paper for recycling and the difficulty of continuously upgrading the effluent plant.","PP (2014)\n2014/687/EU","1.5.2",38,38]
[507,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Unbleached fraft pulp mill","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Emissions to water","Water","Total Suspended Solids (TSS) ","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions of pollutants into receiving waters from the whole mill, BAT is to use TCF or modern ECF bleaching (see description in Section 1.7.2.1), and a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Modified cooking before bleaching; (ii) Oxygen delignification before bleaching; (iii) Closed brown stock screening and efficient brown stock washing; (iv) Partial process water recycling in the bleach plant; (v) Effective spill monitoring and containment with a suitable recovery system; (vi) Maintaining sufficient black liquor evaporation and recovery boiler capacity to cope with peak loads; (vii) Stripping the contaminated (foul) condensates and reusing the condensates in the process","kg/ADt",0.3,1,"Green","Daily",0,0,"Unspecified","Yearly","The BAT-AEL ranges refer to market pulp production and the pulp production part of integrated mills (emissions from papermaking are not included).","PP (2014)\n2014/687/EU","1.2.1",21,21]
[569,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","CTMP or CMP pulp mill","Emissions to water","Water","Total Suspended Solids (TSS) ","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce fresh water use, waste water flow, and the pollution load, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Counter-current flow of process water and separation of water systems; (ii) High consistency bleaching.; (iii) Washing stage before the refining of softwood mechanical pulp using chip pre-treatment; (iv) Substitution of NaOH by Ca(OH)2 or Mg(OH)2 as alkali in peroxide bleaching; (v) Fibre and filler recovery and treatment of white water (papermaking); (vi) Optimum design and construction of tanks and chests (papermaking).","kg/ADt",0.5,0.9,"Green","Daily",0,0,"Unspecified","Yearly",0,"PP (2014)\n2014/687/EU","1.4.1",35,35]
[900,"Refineries","1. Energy industries","1.2. Refining of mineral oil and gas",0,0,"All","Unspecified","All","Unspecified","All units equipped with SCR or SNCR","Emission to air ","Air","Ammonia expressed as NH3","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce ammonia (NH3) emissions to air when applying selective catalytic reduction (SCR) or selective non-catalytic reduction (SNCR) techniques, BAT is to maintain suitable operating conditions of the SCR or SNCR waste gas treatment systems, with the aim of limiting emissions of unreacted NH3.","mg/Nm3",5,15,"Green","Continuous",0,0,0.03,"Monthly average","The higher end of the range is associated with higher inlet NOX concentrations, higher NOX reduction rates and the ageing\nof the catalyst. \n\nThe lower end of the range is associated with the use of the SCR technique. ","REF(2014)\n2014/738/EU","1.1.5",50,13]
[917,"Refineries","1. Energy industries","1.2. Refining of mineral oil and gas",0,0,"All","Unspecified","All","Unspecified","Loading and unloading operations of volatile liquid hydrocarbon compounds","Emission to air ","Air","Benzene","Benzene","In order to prevent or reduce VOC emissions to air from loading and unloading operations of volatile liquid hydrocarbon compounds, BAT is to use one or a combination of the techniques given below to achieve a recovery rate of at least 95 %:\n\nVapour recovery by:\n(i) Condensation\n(ii) Absorption\n(iii) Adsorption\n(iv) Membrane separation\n(v) Hybrid systems ","mg/Nm3","N/A",1,"Amber",0,0,0,0,"Hourly","Hourly values in continuous operation expressed and measured according to European Parliament and Council Directive 94/63/EC (OJ L 365, 31.12.1994, p. 24).","REF(2014)\n2014/738/EU",1.1499999999999999,71,34]
[916,"Refineries","1. Energy industries","1.2. Refining of mineral oil and gas",0,0,"All","Unspecified","All","Unspecified","Combustion unit","Emission to air ","Air","Carbon monoxide, expressed as CO","Carbon monoxide","In order to reduce carbon monoxide (CO) emissions to air from the combustion units, BAT is to use a combustion operation control.","mg/Nm3","N/A",100,"Amber",0,0,0,0.03,"Monthly ",0,"REF(2014)\n2014/738/EU",1.9,68,31]
[911,"Refineries","1. Energy industries","1.2. Refining of mineral oil and gas",0,0,"All","Unspecified","All","Unspecified","Regenerator in the catalytic cracking process- Partical combustion","Emission to air ","Air","Carbon monoxide, expressed as CO","Carbon monoxide","In order to reduce carbon monoxide (CO) emissions to air from the catalytic cracking process (regenerator), BAT is to use one or a combination of the techniques given below.\n(i) Combustion operation control; (ii) Catalysts with carbon monoxide (CO) oxidation promoters; (iii) Carbon monoxide (CO) boiler ","mg/Nm3","N/A",100,"Green","Continuous",0,0,0.03,"Monthly ","May not be achievable when not operating the CO boiler at full load.","REF(2014)\n2014/738/EU",1.5,59,22]
[911,"Refineries","1. Energy industries","1.2. Refining of mineral oil and gas",0,0,"All","Unspecified","All","Unspecified","Unit for calcining of green coke","Emission to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","In order to reduce dust emissions to air from the calcining of green coke process, BAT is to use a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Multistage cyclone\nseparators ","mg/Nm3",10,50,"Amber","Continuous",0,0,0,"Monthly ","The lower end of the range can be achieved with a 4-field ESP\n\nWhen an ESP is not applicable, values of up to 150 mg/Nm3 may occur. ","REF(2014)\n2014/738/EU",1.7,62,24]
[909,"Refineries","1. Energy industries","1.2. Refining of mineral oil and gas",0,0,"All","Existing","All","Unspecified","Regenerator in the catalytic cracking process","Emission to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metals emissions to air from the catalytic cracking process (regenerator), BAT is to use one or a combination of the techniques given below:\n\nPrimary techniques:\n(i) Use of an attrition-resistant catalyst; (ii) Use of low sulphur feedstock (e.g. by feedstock selection or by hydrotreatment of feed) \n\nSecondary techniqyes:\n(i) Electrostatic precipitator (ESP); (ii) Multistage cyclone separators; (iii) Third stage blowback\nfilter; (iv) Wet scrubbing ","mg/Nm3",10,50,"Green","Continuous",0,0,0.03,"Monthly ","Soot blowing in CO boiler and through the gas cooler is excluded.\n\nThe lower end of the range can be achieved with a 4-field ESP.","REF(2014)\n2014/738/EU",1.5,57,20]
[908,"Refineries","1. Energy industries","1.2. Refining of mineral oil and gas",0,0,"All","New","All","Unspecified","Regenerator in the catalytic cracking process","Emission to air ","Air","Dust","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metals emissions to air from the catalytic cracking process (regenerator), BAT is to use one or a combination of the techniques given below:\n\nPrimary techniques:\n(i) Use of an attrition-resistant catalyst; (ii) Use of low sulphur feedstock (e.g. by feedstock selection or by hydrotreatment of feed) \n\nSecondary techniqyes:\n(i) Electrostatic precipitator (ESP); (ii) Multistage cyclone separators; (iii) Third stage blowback\nfilter; (iv) Wet scrubbing ","mg/Nm3",10,25,"Green","Continuous",0,0,0.03,"Monthly ","Soot blowing in CO boiler and through the gas cooler is excluded.","REF(2014)\n2014/738/EU",1.5,57,20]
[914,"Refineries","1. Energy industries","1.2. Refining of mineral oil and gas",0,0,"All","Existing","All","Unspecified","Multi-fuel fired combustion unit  with the exception\nof gas turbines","Emission to air ","Air","Dust ","Particulates (PM10) (24 hr Mean)","In order to prevent or reduce dust and metal emissions to air from the combustion units, BAT is to use one or a combination of the techniques given below: \n\nPrimary techniques:\n(i) Selection or treatment of fuel; (ii) Combustion modifications\n\nSecondary techniques:\n(i) Electrostatic precipitator (ESP); (ii) Third stage blowback filter; (iii) Wet scrubbing; (iv) Centrifugal washers ","mg/Nm3",5,50,"Amber",0,0,0,0.03,"Monthly ","The lower end of the range is achievable for units with the use of end-of-pipe techniques. \n\nThe upper end of the range refers to the use of a high percentage of oil burning and where only primary techniques are\napplicable.","REF(2014)\n2014/738/EU",1.9,66,29]
[915,"Refineries","1. Energy industries","1.2. Refining of mineral oil and gas",0,0,"All","New","All","<50 MW","Multi-fuel fired combustion unit  with the exception\nof gas turbines","Emission to air ","Air","Dust ","Particulates (PM10) (24 hr Mean)","In order to prevent or reduce dust and metal emissions to air from the combustion units, BAT is to use one or a combination of the techniques given below: \n\nPrimary techniques:\n(i) Selection or treatment of fuel; (ii) Combustion modifications\n\nSecondary techniques:\n(i) Electrostatic precipitator (ESP); (ii) Third stage blowback filter; (iii) Wet scrubbing; (iv) Centrifugal washers ","mg/Nm3",5,25,"Green","Once a year and after significant fuel changes",0,0,0.03,"Monthly ",0,"REF(2014)\n2014/738/EU",1.9,66,29]
[917,"Refineries","1. Energy industries","1.2. Refining of mineral oil and gas",0,0,"All","Unspecified","All","Unspecified","Loading and unloading operations of volatile liquid hydrocarbon compounds","Emission to air ","Air","NMVOC","NMVOC","In order to prevent or reduce VOC emissions to air from loading and unloading operations of volatile liquid hydrocarbon compounds, BAT is to use one or a combination of the techniques given below to achieve a recovery rate of at least 95 %:\n\nVapour recovery by:\n(i) Condensation\n(ii) Absorption\n(iii) Adsorption\n(iv) Membrane separation\n(v) Hybrid systems ","g/Nm3",0.15,10,"Amber",0,0,0,0,"Hourly","Hourly values in continuousx operation expressed and measured according to European Parliament and Council Directive 94/63/EC (OJ L 365, 31.12.1994, p. 24).\n\nLower value achievable with two-stage hybrid systems. Upper value achievable with single-stage adsorption or membrane\nsystem. \n\nBenzene monitoring may not be necessary where emissions of NMVOC are at the lower end of the range","REF(2014)\n2014/738/EU",1.1499999999999999,71,34]
[913,"Refineries","1. Energy industries","1.2. Refining of mineral oil and gas",0,0,"All","Existing","All","Unspecified","Gas-fired combustion unit, with the exception of gas turbines","Emission to air ","Air","NOX expressed as NO2","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion units, BAT is to use one or a combination of the techniques given below: \n\nPrimary techniques:\n(i) Selection or treatment of fuel; (ii) Combustion modifications\n\nSeconary techniques:\n(i) Selective catalytic reduction (SCR) ; (ii) Selective non-catalytic reduction (SNCR), (iii) Low temperature oxidation; (iv) SNOX combined technique\n\n\n","mg/Nm3",30,150,"Amber",0,0,0,0.03,"Monthly ","For an existing unit using high air pre-heat (i.e. > 200 °C) or with H2 content in the fuel gas higher than 50 %, the upper end of the BAT-AEL range is 200 mg/Nm3.","REF(2014)\n2014/738/EU",1.9,64,27]
[914,"Refineries","1. Energy industries","1.2. Refining of mineral oil and gas",0,0,"All","Existing","All","Unspecified","Multi-fuel fired combustion unit  with the exception\nof gas turbines","Emission to air ","Air","NOX expressed as NO2","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion units, BAT is to use one or a combination of the techniques given below: \n\nPrimary techniques:\n(i) Selection or treatment of fuel; (ii) Combustion modifications\n\nSeconary techniques:\n(i) Selective catalytic reduction (SCR) ; (ii) Selective non-catalytic reduction (SNCR), (iii) Low temperature oxidation; (iv) SNOX combined technique\n\n\n","mg/Nm3",30,300,"Green","Continuous",0,0,0.03,"Monthly ","For existing units < 100 MW firing fuel oil with a nitrogen content higher than 0,5 % (w/w) or with liquid firing > 50 % or using air preheating, values up to 450 mg/Nm3 may occur\n\nThe lower end of the range can be achieved by using the SCR technique","REF(2014)\n2014/738/EU",1.9,65,28]
[912,"Refineries","1. Energy industries","1.2. Refining of mineral oil and gas",0,0,"All","New","All","Unspecified","Gas turbine","Emission to air ","Air","NOX expressed as NO2","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion units, BAT is to use one or a combination of the techniques given below: \n\nPrimary techniques:\n(i) Selection or treatment of fuel; (ii) Combustion modifications\n\nSeconary techniques:\n(i) Selective catalytic reduction (SCR) ; (ii) Selective non-catalytic reduction (SNCR), (iii) Low temperature oxidation; (iv) SNOX combined technique\n\n\n","mg/Nm3",20,50,"Amber",0,0,0,0.15,"Monthly "," BAT-AEL refers to combined emissions from the gas turbine and the supplementary firing recovery boiler, where present.\n\nFor fuel with high H2 content (i.e. above 10 %), the upper end of the range is 75 mg/Nm3. \n\nGas turbine (including combined cycle gas\nturbine — CCGT) and integrated gasification\ncombined cycle turbine (IGCC)) ","REF(2014)\n2014/738/EU",1.9,64,27]
[913,"Refineries","1. Energy industries","1.2. Refining of mineral oil and gas",0,0,"All","New","All","Unspecified","Gas-fired combustion unit, with the exception of gas turbines","Emission to air ","Air","NOX expressed as NO2","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion units, BAT is to use one or a combination of the techniques given below: \n\nPrimary techniques:\n(i) Selection or treatment of fuel; (ii) Combustion modifications\n\nSeconary techniques:\n(i) Selective catalytic reduction (SCR) ; (ii) Selective non-catalytic reduction (SNCR), (iii) Low temperature oxidation; (iv) SNOX combined technique\n\n\n","mg/Nm3",30,100,"Amber",0,0,0,0.03,"Monthly ",0,"REF(2014)\n2014/738/EU",1.9,64,27]
[912,"Refineries","1. Energy industries","1.2. Refining of mineral oil and gas",0,0,"All","Unspecified","All","Unspecified","Gas turbine- Existing","Emission to air ","Air","NOX expressed as NO2","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion units, BAT is to use one or a combination of the techniques given below: \n\nPrimary techniques:\n(i) Selection or treatment of fuel; (ii) Combustion modifications\n\nSeconary techniques:\n(i) Selective catalytic reduction (SCR) ; (ii) Selective non-catalytic reduction (SNCR), (iii) Low temperature oxidation; (iv) SNOX combined technique\n\n\n","mg/Nm3",40,120,"Amber",0,0,0,0.15,"Monthly ","\n\n BAT-AEL refers to combined emissions from the gas turbine and the supplementary firing recovery boiler, where present.\n\nGas turbine (including combined cycle gas\nturbine — CCGT) and integrated gasification\ncombined cycle turbine (IGCC)) ","REF(2014)\n2014/738/EU",1.9,64,27]
[907,"Refineries","1. Energy industries","1.2. Refining of mineral oil and gas",0,0,"All","New","All","Unspecified","Regenerator in the catalytic cracking process-all combustion mode ","Emission to air ","Air","NOX, expressed as NO2","NOX, expressed as NO2","In order to prevent or reduce NOX emissions to air from the catalytic cracking process (regenerator),\nBAT is to use one or a combination of the techniques given below: \n\nPrimary techniques\n(i) Process optimisation ; (ii) Low-NOX CO oxidation promoters; (iii) Specific additives for NOX reduction \n\nSecondary techniques\n(i) Selective catalytic reduction (SCR); (ii) Selective non-catalytic reduction (SNCR) ; (iii) Low temperature oxidation\n","mg/Nm3",30,100,"Green","Continuous",0,0,0.03,"Monthly ",0,"REF(2014)\n2014/738/EU",1.5,56,19]
[907,"Refineries","1. Energy industries","1.2. Refining of mineral oil and gas",0,0,"All","Existing","All","Unspecified","Regenerator in the catalytic cracking process- full combustion mode","Emission to air ","Air","NOX, expressed as NO3","NOX, expressed as NO3","In order to prevent or reduce NOX emissions to air from the catalytic cracking process (regenerator),\nBAT is to use one or a combination of the techniques given below: \n\nPrimary techniques\n(i) Process optimisation ; (ii) Low-NOX CO oxidation promoters; (iii) Specific additives for NOX reduction \n\nSecondary techniques\n(i) Selective catalytic reduction (SCR); (ii) Selective non-catalytic reduction (SNCR) ; (iii) Low temperature oxidation\n","mg/Nm3",100,300,"Green","Continuous",0,0,0.03,"Monthly ","When antimony (Sb) injection is used for metal passivation, NOX levels up to 700 mg/Nm3 may occur. The lower end of the range can be achieved by using the SCR technique.","REF(2014)\n2014/738/EU",1.5,56,19]
[908,"Refineries","1. Energy industries","1.2. Refining of mineral oil and gas",0,0,"All","Existing","All","Unspecified","Regenerator in the catalytic cracking process- partial combustion mode ","Emission to air ","Air","NOX, expressed as NO4","NOX, expressed as NO4","In order to prevent or reduce NOX emissions to air from the catalytic cracking process (regenerator),\nBAT is to use one or a combination of the techniques given below: \n\nPrimary techniques\n(i) Process optimisation ; (ii) Low-NOX CO oxidation promoters; (iii) Specific additives for NOX reduction \n\nSecondary techniques\n(i) Selective catalytic reduction (SCR); (ii) Selective non-catalytic reduction (SNCR) ; (iii) Low temperature oxidation\n","mg/Nm3",100,400,"Green","Continuous",0,0,0.03,"Monthly ","When antimony (Sb) injection is used for metal passivation, NOX levels up to 700 mg/Nm3 may occur. The lower end of the range can be achieved by using the SCR technique.","REF(2014)\n2014/738/EU",1.5,56,19]
[910,"Refineries","1. Energy industries","1.2. Refining of mineral oil and gas",0,0,"All","Existing","All","Unspecified","Regenerator in the catalytic cracking process- full combustion","Emission to air ","Air","SO2","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX emissions to air from the catalytic cracking process (regenerator), BAT is to use one or a combination of the techniques given below:\n\nPrimary techniques:\n(i) Use of SOX reducing catalyst additives, (ii) Use of low sulphur feedstock (e.g. by feedstock selection or by hydrotreatment of the feed) \n\nSecondary techniques:\n(i) i) Non-regenerative scrubbing; (ii) Regenerative scrubbing","mg/Nm3",100,800,"Green","Continuous",0,0,0.03,"Monthly ","Where selection of low sulphur (e.g. < 0,5 % w/w) feed (or hydrotreatment) and/or scrubbing is applicable, for all combustion modes: the upper end of the BAT-AEL range is ≤ 600 mg/Nm3.","REF(2014)\n2014/738/EU",1.5,59,22]
[910,"Refineries","1. Energy industries","1.2. Refining of mineral oil and gas",0,0,"All","Existing","All","Unspecified","Regenerator in the catalytic cracking process- partial combustion","Emission to air ","Air","SO2","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX emissions to air from the catalytic cracking process (regenerator), BAT is to use one or a combination of the techniques given below:\n\nPrimary techniques:\n(i) Use of SOX reducing catalyst additives, (ii) Use of low sulphur feedstock (e.g. by feedstock selection or by hydrotreatment of the feed) \n\nSecondary techniques:\n(i) i) Non-regenerative scrubbing; (ii) Regenerative scrubbing","mg/Nm3",100,1200,"Green","Continuous",0,0,0.03,"Monthly ","Where selection of low sulphur (e.g. < 0,5 % w/w) feed (or hydrotreatment) and/or scrubbing is applicable, for all combustion modes: the upper end of the BAT-AEL range is ≤ 600 mg/Nm3.","REF(2014)\n2014/738/EU",1.5,59,22]
[909,"Refineries","1. Energy industries","1.2. Refining of mineral oil and gas",0,0,"All","New","All","Unspecified","Regenerator in the catalytic cracking process","Emission to air ","Air","SO2","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX emissions to air from the catalytic cracking process (regenerator), BAT is to use one or a combination of the techniques given below:\n\nPrimary techniques:\n(i) Use of SOX reducing catalyst additives, (ii) Use of low sulphur feedstock (e.g. by feedstock selection or by hydrotreatment of the feed) \n\nSecondary techniques:\n(i) i) Non-regenerative scrubbing; (ii) Regenerative scrubbing","mg/Nm3","N/A",300,"Green","Continuous",0,0,0.03,"Monthly ",0,"REF(2014)\n2014/738/EU",1.5,59,22]
[916,"Refineries","1. Energy industries","1.2. Refining of mineral oil and gas",0,0,"All","Unspecified","All","Unspecified","Multi-fuel fired combustion units, with the exception of gas turbines and stationary gas engines","Emission to air ","Air","SO2","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX emissions to air from the combustion units, BAT is to use one or a combination of the techniques given below.\n\nPrimary techniques:\n(i) Use of gas to replace liquid fuel; (ii) Treatment of refinery fuel gas (RFG); (iii) Use of low sulphur\nrefinery fuel oil (RFO) e.g. by RFO selection or by hydrotreatment of RFO \n\nSecondary techniques:\n(i) Use of low sulphur refinery fuel oil (RFO) e. g. by RFO selection or by hydrotreatment of RFO; (ii) Regenerative scrubbing; (iii) SNOX combined technique","mg/Nm3",35,600,"Amber",0,0,0,0.03,"Monthly ",0,"REF(2014)\n2014/738/EU",1.9,68,31]
[915,"Refineries","1. Energy industries","1.2. Refining of mineral oil and gas",0,0,"All","Unspecified","Refinery fuel gas (RFG)","Unspecified","Combustion unit","Emission to air ","Air","SO2","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX emissions to air from the combustion units, BAT is to use one or a combination of the techniques given below.\n\nPrimary techniques:\n(i) Use of gas to replace liquid fuel; (ii) Treatment of refinery fuel gas (RFG); (iii) Use of low sulphur\nrefinery fuel oil (RFO) e.g. by RFO selection or by hydrotreatment of RFO \n\nSecondary techniques:\n(i) Use of low sulphur refinery fuel oil (RFO) e. g. by RFO selection or by hydrotreatment of RFO; (ii) Regenerative scrubbing; (iii) SNOX combined technique","mg/Nm3",5,35,"Amber",0,0,0,0.03,"Monthly ","In the specific configuration of RFG treatment with a low scrubber operative pressure and with a refinery fuel gas with an H/C molar ratio above 5, the upper end of the BAT-AEL range can be as high as 45 mg/Nm3.","REF(2014)\n2014/738/EU",1.9,68,31]
[905,"Refineries","1. Energy industries","1.2. Refining of mineral oil and gas",0,0,"All","Unspecified","All","Unspecified","Whole refinery ","Emission to water","Water","Benzene","Benzene","Removal of insoluble substances by recovering oil: \n— API Separators (APIs)\n— Corrugated Plate Interceptors (CPIs)\n— Parallel Plate Interceptors (PPIs)\n— Tilted Plate Interceptors (TPIs)\n— Buffer and/or equalisation tanks \n\nRemoval of insoluble substances by recovering suspended solid and dispersed oil:\nThese techniques generally include:\n— Dissolved Gas Flotation (DGF)\n— Induced Gas Flotation (IGF)\n— Sand Filtration \n\nRemoval of soluble substances including biological treatment and clarification:\nBiological treatment techniques may include:\n— Fixed bed systems\n— Suspended bed systems.\nOne of the most commonly used suspended bed system in refineries WWTP is\nthe activated sludge process. Fixed bed systems may include a biofilter or trickling\nfilter\n\nAdditional treatment step:\nA specific waste water treatment intended to complement the previous treatment\nsteps e.g. for further reducing nitrogen or carbon compounds. Generally used\nwhere specific local requirements for water preservation exist\n","mg/l",1E-3,0.05,"Green","Monthly",0,0,"N/A","Yearly ","Refers to a flow-proportional composite sample taken over a period of 24 hours or, provided that sufficient flow stability is demonstrated, a time-proportional sample.\n\nNot all parameters and sampling frequencies are applicable to effluent from gas refining sites","REF(2014)\n2014/738/EU","1.1.7",15,52]
[901,"Refineries","1. Energy industries","1.2. Refining of mineral oil and gas",0,0,"All","Unspecified","All","Unspecified","Whole refinery ","Emission to water","Water","BOD5","BOD5","Removal of insoluble substances by recovering oil: \n— API Separators (APIs)\n— Corrugated Plate Interceptors (CPIs)\n— Parallel Plate Interceptors (PPIs)\n— Tilted Plate Interceptors (TPIs)\n— Buffer and/or equalisation tanks \n\nRemoval of insoluble substances by recovering suspended solid and dispersed oil:\nThese techniques generally include:\n— Dissolved Gas Flotation (DGF)\n— Induced Gas Flotation (IGF)\n— Sand Filtration \n\nRemoval of soluble substances including biological treatment and clarification:\nBiological treatment techniques may include:\n— Fixed bed systems\n— Suspended bed systems.\nOne of the most commonly used suspended bed system in refineries WWTP is\nthe activated sludge process. Fixed bed systems may include a biofilter or trickling\nfilter\n\nAdditional treatment step:\nA specific waste water treatment intended to complement the previous treatment\nsteps e.g. for further reducing nitrogen or carbon compounds. Generally used\nwhere specific local requirements for water preservation exist\n","mg/l","N/A","N/A","Green","Weekly",0,0,"N/A","Yearly ","Refers to a flow-proportional composite sample taken over a period of 24 hours or, provided that sufficient flow stability is demonstrated, a time-proportional sample.\n\nNot all parameters and sampling frequencies are applicable to effluent from gas refining sites","REF(2014)\n2014/738/EU","1.1.7",15,52]
[903,"Refineries","1. Energy industries","1.2. Refining of mineral oil and gas",0,0,"All","Unspecified","All","Unspecified","Whole refinery ","Emission to water","Water","Cadmium, expressed as Cd","Cadmium and its compounds (< 40 mg/l Ca CO3)","Removal of insoluble substances by recovering oil: \n— API Separators (APIs)\n— Corrugated Plate Interceptors (CPIs)\n— Parallel Plate Interceptors (PPIs)\n— Tilted Plate Interceptors (TPIs)\n— Buffer and/or equalisation tanks \n\nRemoval of insoluble substances by recovering suspended solid and dispersed oil:\nThese techniques generally include:\n— Dissolved Gas Flotation (DGF)\n— Induced Gas Flotation (IGF)\n— Sand Filtration \n\nRemoval of soluble substances including biological treatment and clarification:\nBiological treatment techniques may include:\n— Fixed bed systems\n— Suspended bed systems.\nOne of the most commonly used suspended bed system in refineries WWTP is\nthe activated sludge process. Fixed bed systems may include a biofilter or trickling\nfilter\n\nAdditional treatment step:\nA specific waste water treatment intended to complement the previous treatment\nsteps e.g. for further reducing nitrogen or carbon compounds. Generally used\nwhere specific local requirements for water preservation exist\n","mg/l",2E-3,8.0000000000000002E-3,"Green","Quarterly",0,0,"N/A","Yearly ","Refers to a flow-proportional composite sample taken over a period of 24 hours or, provided that sufficient flow stability is demonstrated, a time-proportional sample.\n\nNot all parameters and sampling frequencies are applicable to effluent from gas refining sites","REF(2014)\n2014/738/EU","1.1.7",15,52]
[906,"Refineries","1. Energy industries","1.2. Refining of mineral oil and gas",0,0,"All","Unspecified","All","Unspecified","Whole refinery ","Emission to water","Water","Chemical oxygen demand","COD","Removal of insoluble substances by recovering oil: \n— API Separators (APIs)\n— Corrugated Plate Interceptors (CPIs)\n— Parallel Plate Interceptors (PPIs)\n— Tilted Plate Interceptors (TPIs)\n— Buffer and/or equalisation tanks \n\nRemoval of insoluble substances by recovering suspended solid and dispersed oil:\nThese techniques generally include:\n— Dissolved Gas Flotation (DGF)\n— Induced Gas Flotation (IGF)\n— Sand Filtration \n\nRemoval of soluble substances including biological treatment and clarification:\nBiological treatment techniques may include:\n— Fixed bed systems\n— Suspended bed systems.\nOne of the most commonly used suspended bed system in refineries WWTP is\nthe activated sludge process. Fixed bed systems may include a biofilter or trickling\nfilter\n\nAdditional treatment step:\nA specific waste water treatment intended to complement the previous treatment\nsteps e.g. for further reducing nitrogen or carbon compounds. Generally used\nwhere specific local requirements for water preservation exist\n","mg/l",30,125,"Green","Daily",0,0,"N/A","Yearly ","Refers to a flow-proportional composite sample taken over a period of 24 hours or, provided that sufficient flow stability is demonstrated, a time-proportional sample.\n\nWhere on-site correlation is available, COD may be replaced by TOC. The correlation between COD and TOC should be\nelaborated on a case-by-case basis. TOC monitoring would be the preferred option because it does not rely on the use of\nvery toxic compounds. \n\nNot all parameters and sampling frequencies are applicable to effluent from gas refining sites","REF(2014)\n2014/738/EU","1.1.7",14,51]
[901,"Refineries","1. Energy industries","1.2. Refining of mineral oil and gas",0,0,"All","Unspecified","All","Unspecified","Whole refinery ","Emission to water","Water","Hydrocarbon oil index (HOI)","Hydrocarbon oil index (HOI)","Removal of insoluble substances by recovering oil: \n— API Separators (APIs)\n— Corrugated Plate Interceptors (CPIs)\n— Parallel Plate Interceptors (PPIs)\n— Tilted Plate Interceptors (TPIs)\n— Buffer and/or equalisation tanks \n\nRemoval of insoluble substances by recovering suspended solid and dispersed oil:\nThese techniques generally include:\n— Dissolved Gas Flotation (DGF)\n— Induced Gas Flotation (IGF)\n— Sand Filtration \n\nRemoval of soluble substances including biological treatment and clarification:\nBiological treatment techniques may include:\n— Fixed bed systems\n— Suspended bed systems.\nOne of the most commonly used suspended bed system in refineries WWTP is\nthe activated sludge process. Fixed bed systems may include a biofilter or trickling\nfilter\n\nAdditional treatment step:\nA specific waste water treatment intended to complement the previous treatment\nsteps e.g. for further reducing nitrogen or carbon compounds. Generally used\nwhere specific local requirements for water preservation exist\n","mg/l",0.1,2.5,"Green","Daily",0,0,"N/A","Yearly ","Refers to a flow-proportional composite sample taken over a period of 24 hours or, provided that sufficient flow stability is demonstrated, a time-proportional sample.\n\nMoving from the current method to EN 9377-2 may require an adaptation period.\n\nNot all parameters and sampling frequencies are applicable to effluent from gas refining sites","REF(2014)\n2014/738/EU","1.1.7",14,51]
[902,"Refineries","1. Energy industries","1.2. Refining of mineral oil and gas",0,0,"All","Unspecified","All","Unspecified","Whole refinery ","Emission to water","Water","Lead, expressed as Pb","Lead and its compounds","Removal of insoluble substances by recovering oil: \n— API Separators (APIs)\n— Corrugated Plate Interceptors (CPIs)\n— Parallel Plate Interceptors (PPIs)\n— Tilted Plate Interceptors (TPIs)\n— Buffer and/or equalisation tanks \n\nRemoval of insoluble substances by recovering suspended solid and dispersed oil:\nThese techniques generally include:\n— Dissolved Gas Flotation (DGF)\n— Induced Gas Flotation (IGF)\n— Sand Filtration \n\nRemoval of soluble substances including biological treatment and clarification:\nBiological treatment techniques may include:\n— Fixed bed systems\n— Suspended bed systems.\nOne of the most commonly used suspended bed system in refineries WWTP is\nthe activated sludge process. Fixed bed systems may include a biofilter or trickling\nfilter\n\nAdditional treatment step:\nA specific waste water treatment intended to complement the previous treatment\nsteps e.g. for further reducing nitrogen or carbon compounds. Generally used\nwhere specific local requirements for water preservation exist\n","mg/l",5.0000000000000001E-3,0.03,"Green","Quarterly",0,0,"N/A","Yearly ","Refers to a flow-proportional composite sample taken over a period of 24 hours or, provided that sufficient flow stability is demonstrated, a time-proportional sample. \n\nNot all parameters and sampling frequencies are applicable to effluent from gas refining sites","REF(2014)\n2014/738/EU","1.1.7",15,52]
[904,"Refineries","1. Energy industries","1.2. Refining of mineral oil and gas",0,0,"All","Unspecified","All","Unspecified","Whole refinery ","Emission to water","Water","Mercury, expressed as Hg","Mercury and its compounds","Removal of insoluble substances by recovering oil: \n— API Separators (APIs)\n— Corrugated Plate Interceptors (CPIs)\n— Parallel Plate Interceptors (PPIs)\n— Tilted Plate Interceptors (TPIs)\n— Buffer and/or equalisation tanks \n\nRemoval of insoluble substances by recovering suspended solid and dispersed oil:\nThese techniques generally include:\n— Dissolved Gas Flotation (DGF)\n— Induced Gas Flotation (IGF)\n— Sand Filtration \n\nRemoval of soluble substances including biological treatment and clarification:\nBiological treatment techniques may include:\n— Fixed bed systems\n— Suspended bed systems.\nOne of the most commonly used suspended bed system in refineries WWTP is\nthe activated sludge process. Fixed bed systems may include a biofilter or trickling\nfilter\n\nAdditional treatment step:\nA specific waste water treatment intended to complement the previous treatment\nsteps e.g. for further reducing nitrogen or carbon compounds. Generally used\nwhere specific local requirements for water preservation exist\n","mg/l",1E-4,1E-3,"Green","Quarterly",0,0,"N/A","Yearly ","Refers to a flow-proportional composite sample taken over a period of 24 hours or, provided that sufficient flow stability is demonstrated, a time-proportional sample.\n\nNot all parameters and sampling frequencies are applicable to effluent from gas refining sites","REF(2014)\n2014/738/EU","1.1.7",15,52]
[903,"Refineries","1. Energy industries","1.2. Refining of mineral oil and gas",0,0,"All","Unspecified","All","Unspecified","Whole refinery ","Emission to water","Water","Nickel, expressed as Ni","Nickel and its compounds","Removal of insoluble substances by recovering oil: \n— API Separators (APIs)\n— Corrugated Plate Interceptors (CPIs)\n— Parallel Plate Interceptors (PPIs)\n— Tilted Plate Interceptors (TPIs)\n— Buffer and/or equalisation tanks \n\nRemoval of insoluble substances by recovering suspended solid and dispersed oil:\nThese techniques generally include:\n— Dissolved Gas Flotation (DGF)\n— Induced Gas Flotation (IGF)\n— Sand Filtration \n\nRemoval of soluble substances including biological treatment and clarification:\nBiological treatment techniques may include:\n— Fixed bed systems\n— Suspended bed systems.\nOne of the most commonly used suspended bed system in refineries WWTP is\nthe activated sludge process. Fixed bed systems may include a biofilter or trickling\nfilter\n\nAdditional treatment step:\nA specific waste water treatment intended to complement the previous treatment\nsteps e.g. for further reducing nitrogen or carbon compounds. Generally used\nwhere specific local requirements for water preservation exist\n","mg/l",5.0000000000000001E-3,0.1,"Green","Quarterly",0,0,"N/A","Yearly ","Refers to a flow-proportional composite sample taken over a period of 24 hours or, provided that sufficient flow stability is demonstrated, a time-proportional sample.\n\nNot all parameters and sampling frequencies are applicable to effluent from gas refining sites","REF(2014)\n2014/738/EU","1.1.7",15,52]
[905,"Refineries","1. Energy industries","1.2. Refining of mineral oil and gas",0,0,"All","Unspecified","All","Unspecified","Whole refinery ","Emission to water","Water","Phenol Index","Phenol Index","Removal of insoluble substances by recovering oil: \n— API Separators (APIs)\n— Corrugated Plate Interceptors (CPIs)\n— Parallel Plate Interceptors (PPIs)\n— Tilted Plate Interceptors (TPIs)\n— Buffer and/or equalisation tanks \n\nRemoval of insoluble substances by recovering suspended solid and dispersed oil:\nThese techniques generally include:\n— Dissolved Gas Flotation (DGF)\n— Induced Gas Flotation (IGF)\n— Sand Filtration \n\nRemoval of soluble substances including biological treatment and clarification:\nBiological treatment techniques may include:\n— Fixed bed systems\n— Suspended bed systems.\nOne of the most commonly used suspended bed system in refineries WWTP is\nthe activated sludge process. Fixed bed systems may include a biofilter or trickling\nfilter\n\nAdditional treatment step:\nA specific waste water treatment intended to complement the previous treatment\nsteps e.g. for further reducing nitrogen or carbon compounds. Generally used\nwhere specific local requirements for water preservation exist\n","mg/l","N/A","N/A","Green","Monthly",0,0,"N/A","Yearly ","Refers to a flow-proportional composite sample taken over a period of 24 hours or, provided that sufficient flow stability is demonstrated, a time-proportional sample.\n\nNot all parameters and sampling frequencies are applicable to effluent from gas refining sites","REF(2014)\n2014/738/EU","1.1.7",15,52]
[902,"Refineries","1. Energy industries","1.2. Refining of mineral oil and gas",0,0,"All","Unspecified","All","Unspecified","Whole refinery ","Emission to water","Water","Total nitrogen expressed as N","Total Nitrogen (TN)","Removal of insoluble substances by recovering oil: \n— API Separators (APIs)\n— Corrugated Plate Interceptors (CPIs)\n— Parallel Plate Interceptors (PPIs)\n— Tilted Plate Interceptors (TPIs)\n— Buffer and/or equalisation tanks \n\nRemoval of insoluble substances by recovering suspended solid and dispersed oil:\nThese techniques generally include:\n— Dissolved Gas Flotation (DGF)\n— Induced Gas Flotation (IGF)\n— Sand Filtration \n\nRemoval of soluble substances including biological treatment and clarification:\nBiological treatment techniques may include:\n— Fixed bed systems\n— Suspended bed systems.\nOne of the most commonly used suspended bed system in refineries WWTP is\nthe activated sludge process. Fixed bed systems may include a biofilter or trickling\nfilter\n\nAdditional treatment step:\nA specific waste water treatment intended to complement the previous treatment\nsteps e.g. for further reducing nitrogen or carbon compounds. Generally used\nwhere specific local requirements for water preservation exist\n","mg/l",1,25,"Green","Daily",0,0,"N/A","Yearly ","Refers to a flow-proportional composite sample taken over a period of 24 hours or, provided that sufficient flow stability is demonstrated, a time-proportional sample.\n\nWhen nitrification/denitrification is used, levels below 15 mg/l can be achieved. \n\nWhere total-nitrogen is the sum of total Kjeldahl nitrogen (TKN), nitrates and nitrites\n\nNot all parameters and sampling frequencies are applicable to effluent from gas refining sites","REF(2014)\n2014/738/EU","1.1.7",15,52]
[906,"Refineries","1. Energy industries","1.2. Refining of mineral oil and gas",0,0,"All","Unspecified","All","Unspecified","Whole refinery ","Emission to water","Water","Total Suspended Solids (TSS) ","Total Suspended Solids (TSS) ","Removal of insoluble substances by recovering oil: \n— API Separators (APIs)\n— Corrugated Plate Interceptors (CPIs)\n— Parallel Plate Interceptors (PPIs)\n— Tilted Plate Interceptors (TPIs)\n— Buffer and/or equalisation tanks \n\nRemoval of insoluble substances by recovering suspended solid and dispersed oil:\nThese techniques generally include:\n— Dissolved Gas Flotation (DGF)\n— Induced Gas Flotation (IGF)\n— Sand Filtration \n\nRemoval of soluble substances including biological treatment and clarification:\nBiological treatment techniques may include:\n— Fixed bed systems\n— Suspended bed systems.\nOne of the most commonly used suspended bed system in refineries WWTP is\nthe activated sludge process. Fixed bed systems may include a biofilter or trickling\nfilter\n\nAdditional treatment step:\nA specific waste water treatment intended to complement the previous treatment\nsteps e.g. for further reducing nitrogen or carbon compounds. Generally used\nwhere specific local requirements for water preservation exist\n","mg/l",5,25,"Green","Daily",0,0,"N/A","Yearly ","Refers to a flow-proportional composite sample taken over a period of 24 hours or, provided that sufficient flow stability is demonstrated, a time-proportional sample.\n\nNot all parameters and sampling frequencies are applicable to effluent from gas refining sites","REF(2014)\n2014/738/EU","1.1.7",14,51]
[904,"Refineries","1. Energy industries","1.2. Refining of mineral oil and gas",0,0,"All","Unspecified","All","Unspecified","Whole refinery ","Emission to water","Water","Vanadium","Vanadium (> 200 mg/l CaCO3)","Removal of insoluble substances by recovering oil: \n— API Separators (APIs)\n— Corrugated Plate Interceptors (CPIs)\n— Parallel Plate Interceptors (PPIs)\n— Tilted Plate Interceptors (TPIs)\n— Buffer and/or equalisation tanks \n\nRemoval of insoluble substances by recovering suspended solid and dispersed oil:\nThese techniques generally include:\n— Dissolved Gas Flotation (DGF)\n— Induced Gas Flotation (IGF)\n— Sand Filtration \n\nRemoval of soluble substances including biological treatment and clarification:\nBiological treatment techniques may include:\n— Fixed bed systems\n— Suspended bed systems.\nOne of the most commonly used suspended bed system in refineries WWTP is\nthe activated sludge process. Fixed bed systems may include a biofilter or trickling\nfilter\n\nAdditional treatment step:\nA specific waste water treatment intended to complement the previous treatment\nsteps e.g. for further reducing nitrogen or carbon compounds. Generally used\nwhere specific local requirements for water preservation exist\n","mg/l","N/A","N/A","Green","Quarterly",0,0,"N/A","Yearly ","Refers to a flow-proportional composite sample taken over a period of 24 hours or, provided that sufficient flow stability is demonstrated, a time-proportional sample.\n\nNot all parameters and sampling frequencies are applicable to effluent from gas refining sites","REF(2014)\n2014/738/EU","1.1.7",15,52]
[221,"Tanning of Hides and Skins","6. Other activities ","6.3. Plants for the tanning of hides and skins where the treatment capacity exceeds 12 tonnes of finished products per day.","Extraction ventilation and abatement system is used as an alternative to the use of water-borne finishing materials",0,"Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Emission to air","Air","VOC","VOC","In order to reduce the airborne emissions of halogenated volatile organic compounds, BAT is to replace halogenated volatile organic compounds used in the process with substances that are not halogenated.","g/m3",9,23,"Green","Monitoring of volatile organic compound emissions at the outlet of abatement equipment, and recording of production continuously or periodcally. Applicable to plants carrying out finishing using solvents and employing abatement.",0,0,"Unspecified ","annual average values per unit of finished leather","BAT-AEL range expressed as total carbon.","TAN (2013)\n2013/84/EU","1.6.2",27,27]
[201,"Tanning of Hides and Skins","6. Other activities ","6.3. Plants for the tanning of hides and skins where the treatment capacity exceeds 12 tonnes of finished products per day.","Bovine salted hides- Raw to wet blue/white",0,"Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Consumption","Consumption","Water","Water","In order to minimise water consumption, BAT is to use one or both of the techniques given below: (i) The optimisation of water use in all wet process steps, including the use of batch washing instead of running water washes; (ii) The use of short floats","m3/t",13,18,"Green","Measurement of water consumption in the two process stages: up to tanning and post-tanning, and recording of production in the same period.",0,0,"Unspecified ","Monthly ","Monthly average values. Processing of calfskins and vegetable tanning may require a higher water","TAN (2013)\n2013/84/EU",1.3,20,20]
[205,"Tanning of Hides and Skins","6. Other activities ","6.3. Plants for the tanning of hides and skins where the treatment capacity exceeds 12 tonnes of finished products per day.","Bovine salted hides- Total consumption ",0,"Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Consumption","Consumption","Water","Water","In order to minimise water consumption, BAT is to use one or both of the techniques given below: (i) The optimisation of water use in all wet process steps, including the use of batch washing instead of running water washes; (ii) The use of short floats","m3/t",19,28,"Green","Measurement of water consumption in the two process stages: up to tanning and post-tanning, and recording of production in the same period.",0,0,"Unspecified ","Monthly ","Monthly average values. Processing of calfskins and vegetable tanning may require a higher water","TAN (2013)\n2013/84/EU",1.3,20,20]
[200,"Tanning of Hides and Skins","6. Other activities ","6.3. Plants for the tanning of hides and skins where the treatment capacity exceeds 12 tonnes of finished products per day.","Bovine unsalted hides- Raw to wet blue/white",0,"Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Consumption","Consumption","Water","Water","In order to minimise water consumption, BAT is to use one or both of the techniques given below: (i) The optimisation of water use in all wet process steps, including the use of batch washing instead of running water washes; (ii) The use of short floats","m3/t",10,15,"Green","Measurement of water consumption in the two process stages: up to tanning and post-tanning, and recording of production in the same period.",0,0,"Unspecified ","Monthly ","Monthly average values. Processing of calfskins and vegetable tanning may require a higher water","TAN (2013)\n2013/84/EU",1.3,20,20]
[204,"Tanning of Hides and Skins","6. Other activities ","6.3. Plants for the tanning of hides and skins where the treatment capacity exceeds 12 tonnes of finished products per day.","Bovine unsalted hides- Total consumption",0,"Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Consumption","Consumption","Water","Water","In order to minimise water consumption, BAT is to use one or both of the techniques given below: (i) The optimisation of water use in all wet process steps, including the use of batch washing instead of running water washes; (ii) The use of short floats","m3/t",16,25,"Green","Measurement of water consumption in the two process stages: up to tanning and post-tanning, and recording of production in the same period.",0,0,"Unspecified ","Monthly ","Monthly average values. Processing of calfskins and vegetable tanning may require a higher water","TAN (2013)\n2013/84/EU",1.3,20,20]
[202,"Tanning of Hides and Skins","6. Other activities ","6.3. Plants for the tanning of hides and skins where the treatment capacity exceeds 12 tonnes of finished products per day.","Bovine-unsalted hides- Post tanning processes and finishing",0,"Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Consumption","Consumption","Water","Water","In order to minimise water consumption, BAT is to use one or both of the techniques given below: (i) The optimisation of water use in all wet process steps, including the use of batch washing instead of running water washes; (ii) The use of short floats","m3/t",6,10,"Green","Measurement of water consumption in the two process stages: up to tanning and post-tanning, and recording of production in the same period.",0,0,"Unspecified ","Monthly ","Monthly average values. Processing of calfskins and vegetable tanning may require a higher water","TAN (2013)\n2013/84/EU",1.3,20,20]
[203,"Tanning of Hides and Skins","6. Other activities ","6.3. Plants for the tanning of hides and skins where the treatment capacity exceeds 12 tonnes of finished products per day.","Bovine-unsalted hides- Post tanning processes and finishing",0,"Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Consumption","Consumption","Water","Water","In order to minimise water consumption, BAT is to use one or both of the techniques given below: (i) The optimisation of water use in all wet process steps, including the use of batch washing instead of running water washes; (ii) The use of short floats","m3/t",6,10,"Green","Measurement of water consumption in the two process stages: up to tanning and post-tanning, and recording of production in the same period.",0,0,"Unspecified ","Monthly ","Monthly average values. Processing of calfskins and vegetable tanning may require a higher water","TAN (2013)\n2013/84/EU",1.3,20,20]
[207,"Tanning of Hides and Skins","6. Other activities ","6.3. Plants for the tanning of hides and skins where the treatment capacity exceeds 12 tonnes of finished products per day.","Sheepskins- Pickle to wet blue",0,"Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Consumption","Consumption","Water","Water","In order to minimise water consumption, BAT is to use one or both of the techniques given below: (i) The optimisation of water use in all wet process steps, including the use of batch washing instead of running water washes; (ii) The use of short floats","m3/t",30,55,"Green","Measurement of water consumption in the two process stages: up to tanning and post-tanning, and recording of production in the same period.",0,0,"Unspecified ","Monthly ","Monthly average values. Processing of calfskins and vegetable tanning may require a higher water","TAN (2013)\n2013/84/EU",1.3,20,20]
[208,"Tanning of Hides and Skins","6. Other activities ","6.3. Plants for the tanning of hides and skins where the treatment capacity exceeds 12 tonnes of finished products per day.","Sheepskins- Post tanning processes and finishing",0,"Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Consumption","Consumption","Water","Water","In order to minimise water consumption, BAT is to use one or both of the techniques given below: (i) The optimisation of water use in all wet process steps, including the use of batch washing instead of running water washes; (ii) The use of short floats","m3/t",15,45,"Green","Measurement of water consumption in the two process stages: up to tanning and post-tanning, and recording of production in the same period.",0,0,"Unspecified ","Monthly ","Monthly average values. Processing of calfskins and vegetable tanning may require a higher water","TAN (2013)\n2013/84/EU",1.3,20,20]
[206,"Tanning of Hides and Skins","6. Other activities ","6.3. Plants for the tanning of hides and skins where the treatment capacity exceeds 12 tonnes of finished products per day.","Sheepskins- Raw to picle",0,"Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Consumption","Consumption","Water","Water","In order to minimise water consumption, BAT is to use one or both of the techniques given below: (i) The optimisation of water use in all wet process steps, including the use of batch washing instead of running water washes; (ii) The use of short floats","m3/t",65,80,"Green","Measurement of water consumption in the two process stages: up to tanning and post-tanning, and recording of production in the same period.",0,0,"Unspecified ","Monthly ","Monthly average values. Processing of calfskins and vegetable tanning may require a higher water","TAN (2013)\n2013/84/EU",1.3,20,20]
[209,"Tanning of Hides and Skins","6. Other activities ","6.3. Plants for the tanning of hides and skins where the treatment capacity exceeds 12 tonnes of finished products per day.","Sheepskins- Total",0,"Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Consumption","Consumption","Water","Water","In order to minimise water consumption, BAT is to use one or both of the techniques given below: (i) The optimisation of water use in all wet process steps, including the use of batch washing instead of running water washes; (ii) The use of short floats","m3/t",110,180,"Green","Measurement of water consumption in the two process stages: up to tanning and post-tanning, and recording of production in the same period.",0,0,"Unspecified ","Monthly ","Monthly average values. Processing of calfskins and vegetable tanning may require a higher water","TAN (2013)\n2013/84/EU",1.3,20,20]
[220,"Tanning of Hides and Skins","6. Other activities ","6.3. Plants for the tanning of hides and skins where the treatment capacity exceeds 12 tonnes of finished products per day.","Coated leathers (thickness > 0.15mm): Water-borne coatings used in combination with an efficient application system ",0,"Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Consumption rates","Consumption rates","Solvent use levels","Solvent use levels","N/A","g/m2",115,150,"Green","N/A",0,0,"Unspecified ","annual average values per unit of finished leather",0,"TAN (2013)\n2013/84/EU","1.6.2",26,26]
[219,"Tanning of Hides and Skins","6. Other activities ","6.3. Plants for the tanning of hides and skins where the treatment capacity exceeds 12 tonnes of finished products per day.","Footwear, garment, and leathergoods leathers: Water-borne coatings used in combination with an efficient application system ",0,"Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Consumption rates","Consumption rates","Solvent use levels","Solvent use levels","N/A","g/m2",40,85,"Green","N/A",0,0,"Unspecified ","annual average values per unit of finished leather",0,"TAN (2013)\n2013/84/EU","1.6.2",26,26]
[218,"Tanning of Hides and Skins","6. Other activities ","6.3. Plants for the tanning of hides and skins where the treatment capacity exceeds 12 tonnes of finished products per day.","Upholstery and automative leather: Water-borne coatings used in combination with an efficient application system ",0,"Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Consumption rates","Consumption rates","Solvent use levels","Solvent use levels","N/A","g/m2",10,25,"Green","N/A",0,0,"Unspecified ","annual average values per unit of finished leather",0,"TAN (2013)\n2013/84/EU","1.6.2",26,26]
[213,"Tanning of Hides and Skins","6. Other activities ","6.3. Plants for the tanning of hides and skins where the treatment capacity exceeds 12 tonnes of finished products per day.","Post treatment",0,"Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Emission to water","Water","Ammoniacal nitrogen NH4-N (as N)","Un-ionised ammonia as nitrogen","In order to reduce emissions to receiving waters, BAT is to apply waste water treatment comprising an appropriate on-site and/or off-site combination of the following techniques:\n(i) mechanical treatment;\n(ii) physico-chemical treatment;\n(iii) biological treatment;\n(iv) biological nitrogen elimination.","mg/l","N/A",10,"Green","Monitoring of chemical oxygen demand (COD), biochemical oxygen demand (BOD) and ammoniacal nitrogen after on-site or off-site effluent treatment for direct discharges to receiving water, by using flow-proportional 24-hour composite samples. Monitoring of total suspended solids after on-site or off-site effluent treatment for direct discharges to receiving water.",0,0,"Unspecified ","monthly average values based on the average of the 24-hour representative composite samples taken over a month)",0,"TAN (2013)\n2013/84/EU",1.5,24,24]
[211,"Tanning of Hides and Skins","6. Other activities ","6.3. Plants for the tanning of hides and skins where the treatment capacity exceeds 12 tonnes of finished products per day.","Post treatment",0,"Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Emission to water","Water","BOD5","BOD5","In order to reduce emissions to receiving waters, BAT is to apply waste water treatment comprising an appropriate on-site and/or off-site combination of the following techniques:\n(i) mechanical treatment;\n(ii) physico-chemical treatment;\n(iii) biological treatment;\n(iv) biological nitrogen elimination.","mg/l",15,25,"Green","Monitoring of chemical oxygen demand (COD), biochemical oxygen demand (BOD) and ammoniacal nitrogen after on-site or off-site effluent treatment for direct discharges to receiving water, by using flow-proportional 24-hour composite samples. Monitoring of total suspended solids after on-site or off-site effluent treatment for direct discharges to receiving water.",0,0,"Unspecified ","monthly average values based on the average of the 24-hour representative composite samples taken over a month)",0,"TAN (2013)\n2013/84/EU",1.5,24,24]
[210,"Tanning of Hides and Skins","6. Other activities ","6.3. Plants for the tanning of hides and skins where the treatment capacity exceeds 12 tonnes of finished products per day.","Post treatment",0,"Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Emission to water","Water","COD","COD","In order to reduce emissions to receiving waters, BAT is to apply waste water treatment comprising an appropriate on-site and/or off-site combination of the following techniques:\n(i) mechanical treatment;\n(ii) physico-chemical treatment;\n(iii) biological treatment;\n(iv) biological nitrogen elimination.","mg/l",200,500,"Green","Monitoring of chemical oxygen demand (COD), biochemical oxygen demand (BOD) and ammoniacal nitrogen after on-site or off-site effluent treatment for direct discharges to receiving water, by using flow-proportional 24-hour composite samples. Monitoring of total suspended solids after on-site or off-site effluent treatment for direct discharges to receiving water.",0,0,"Unspecified ","monthly average values based on the average of the 24-hour representative composite samples taken over a month)",0,"TAN (2013)\n2013/84/EU",1.5,24,24]
[215,"Tanning of Hides and Skins","6. Other activities ","6.3. Plants for the tanning of hides and skins where the treatment capacity exceeds 12 tonnes of finished products per day.","Post treatment",0,"Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Emission to water","Water","Sulphide (as S)","Sulphide (as S)","In order to reduce emissions to receiving waters, BAT is to apply waste water treatment comprising an appropriate on-site and/or off-site combination of the following techniques:\n(i) mechanical treatment;\n(ii) physico-chemical treatment;\n(iii) biological treatment;\n(iv) biological nitrogen elimination.","mg/l","N/A",1,"Green","Monitoring of the sulphide concentration and total chromium concentration in the final effluent after treatment for direct discharge to receiving water, by using flow proportional 24-hour composite samples. Monitoring of the sulphide concentration and total chromium concentration after chromium precipitation for indirect discharge, by using flow proportional 24-hour composite samples.",0,0,"Unspecified ","monthly average values based on the average of the 24-hour representative composite samples taken over a month)",0,"TAN (2013)\n2013/84/EU",1.5,24,24]
[217,"Tanning of Hides and Skins","6. Other activities ","6.3. Plants for the tanning of hides and skins where the treatment capacity exceeds 12 tonnes of finished products per day.","Unspecified",0,"Unspecified","Unspecified","Unspecified","Unspecified","Indirect discharges of waste water from tanneries into urban waste water treatment plants ","Emission to water","Water","Sulphide (as S)","Sulphide (as S)","In order to reduce total chromium and sulphide emissions through indirect discharges of waste water from tanneries into urban waste water treatment plants, BAT is to apply chromium precipitation and sulphide oxidation.","mg/l","N/A",1,"Green","Monitoring of the sulphide concentration and total chromium concentration in the final effluent after treatment for direct discharge to receiving water, by using flow proportional 24-hour composite samples. Monitoring of the sulphide concentration and total chromium concentration after chromium precipitation for indirect discharge, by using flow proportional 24-hour composite samples.",0,0,"Unspecified ","monthly average values based on the average of the 24-hour representative composite samples taken over a month","BAT-AELs for total chromium and sulphide emissions through indirect discharges of waste water from tanneries into urban waste water treatment plants","TAN (2013)\n2013/84/EU",1.5,25,25]
[212,"Tanning of Hides and Skins","6. Other activities ","6.3. Plants for the tanning of hides and skins where the treatment capacity exceeds 12 tonnes of finished products per day.","Post treatment",0,"Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Emission to water","Water","Total Suspended Solids (TSS) ","Total Suspended Solids (TSS) ","In order to reduce emissions to receiving waters, BAT is to apply waste water treatment comprising an appropriate on-site and/or off-site combination of the following techniques:\n(i) mechanical treatment;\n(ii) physico-chemical treatment;\n(iii) biological treatment;\n(iv) biological nitrogen elimination.","mg/l","N/A",35,"Green","Monitoring of chemical oxygen demand (COD), biochemical oxygen demand (BOD) and ammoniacal nitrogen after on-site or off-site effluent treatment for direct discharges to receiving water, by using flow-proportional 24-hour composite samples. Monitoring of total suspended solids after on-site or off-site effluent treatment for direct discharges to receiving water.",0,0,"Unspecified ",0,0,"TAN (2013)\n2013/84/EU",1.5,24,24]
[214,"Tanning of Hides and Skins","6. Other activities ","6.3. Plants for the tanning of hides and skins where the treatment capacity exceeds 12 tonnes of finished products per day.","Post treatment",0,"Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Emission to water","Water","Total chromium (as Cr)","Total chromium (as Cr)","In order to reduce emissions to receiving waters, BAT is to apply waste water treatment comprising an appropriate on-site and/or off-site combination of the following techniques:\n(i) mechanical treatment;\n(ii) physico-chemical treatment;\n(iii) biological treatment;\n(iv) biological nitrogen elimination.","mg/l",0.3,1,"Green","Monitoring of the sulphide concentration and total chromium concentration in the final effluent after treatment for direct discharge to receiving water, by using flow proportional 24-hour composite samples. Monitoring of the sulphide concentration and total chromium concentration after chromium precipitation for indirect discharge, by using flow proportional 24-hour composite samples.",0,0,"Unspecified ","monthly average values based on the average of the 24-hour representative composite samples taken over a month)",0,"TAN (2013)\n2013/84/EU",1.5,24,24]
[216,"Tanning of Hides and Skins","6. Other activities ","6.3. Plants for the tanning of hides and skins where the treatment capacity exceeds 12 tonnes of finished products per day.","Unspecified",0,"Unspecified","Unspecified","Unspecified","Unspecified","Indirect discharges of waste water from tanneries into urban waste water treatment plants ","Emission to water","Water","Total chromium (as Cr)","Total chromium (as Cr)","In order to reduce total chromium and sulphide emissions through indirect discharges of waste water from tanneries into urban waste water treatment plants, BAT is to apply chromium precipitation and sulphide oxidation.","mg/l",0.3,1,"Green","Monitoring of the sulphide concentration and total chromium concentration in the final effluent after treatment for direct discharge to receiving water, by using flow proportional 24-hour composite samples. Monitoring of the sulphide concentration and total chromium concentration after chromium precipitation for indirect discharge, by using flow proportional 24-hour composite samples.",0,0,"Unspecified ","monthly average values based on the average of the 24-hour representative composite samples taken over a month","BAT-AELs for total chromium and sulphide emissions through indirect discharges of waste water from tanneries into urban waste water treatment plants","TAN (2013)\n2013/84/EU",1.5,25,25]
[1001,"Wood-based Panels Production","6.   Other activities","6.1. (c) one or more of the following wood-based panels: oriented strand board, particleboard or fibreboard with a production capacity exceeding 600 m3 per day\n ",0,"Fibre","Unspecified","Unspecified","Unspecified","Unspecified","Dryer- all types ","Emissions to air","Air","Dust ","Particulates (PM10) (24 hr Mean)","In order to prevent or reduce emissions to air from the dryer, BAT is to achieve and manage a balanced operation of the\ndrying process and to use one or a combination of the techniques given below: (i) Dust abatement of inlet hot gas to a\ndirectly heated dryer in combination with one or a combination of the other techniques listed below; (ii) Bag filter; (iii) Cyclone; (iv) UTWS dryer and combustion with heat exchanger and thermal treatment of discharged dryer waste gasl (v) Wet electrostatic precipitator; (vi) Wet scrubber; (vii) Bioscrubber; (viii) Chemical degradation or capture of formaldehyde with chemicals in combination with a wet scrubbing system \n\n","mg/Nm3",3,20,"Green","Periodic (at least once every 6 months)",0,0,"N/A","Average over sampling period ",0,"WBP (2015) 2015/2119 \n",1.2,44,14]
[1000,"Wood-based Panels Production","6.   Other activities","6.1. (c) one or more of the following wood-based panels: oriented strand board, particleboard or fibreboard with a production capacity exceeding 600 m3 per day\n ",0,"PB or OSB","Unspecified","Unspecified","Unspecified","Unspecified","Dryer- Directly heated","Emissions to air","Air","Dust ","Particulates (PM10) (24 hr Mean)","In order to prevent or reduce emissions to air from the dryer, BAT is to achieve and manage a balanced operation of the\ndrying process and to use one or a combination of the techniques given below: (i) Dust abatement of inlet hot gas to a\ndirectly heated dryer in combination with one or a combination of the other techniques listed below; (ii) Bag filter; (iii) Cyclone; (iv) UTWS dryer and combustion with heat exchanger and thermal treatment of discharged dryer waste gasl (v) Wet electrostatic precipitator; (vi) Wet scrubber; (vii) Bioscrubber; (viii) Chemical degradation or capture of formaldehyde with chemicals in combination with a wet scrubbing system \n\n","mg/Nm3",3,30,"Green","Periodic (at least once every 6 months)",0,0,0.15,"Average over sampling period ",0,"WBP (2015) 2015/2119 \n",1.2,44,14]
[1001,"Wood-based Panels Production","6.   Other activities","6.1. (c) one or more of the following wood-based panels: oriented strand board, particleboard or fibreboard with a production capacity exceeding 600 m3 per day\n ",0,"PB or OSB","Unspecified","Unspecified","Unspecified","Unspecified","Dryer-Indirectly heated ","Emissions to air","Air","Dust ","Particulates (PM10) (24 hr Mean)","In order to prevent or reduce emissions to air from the dryer, BAT is to achieve and manage a balanced operation of the\ndrying process and to use one or a combination of the techniques given below: (i) Dust abatement of inlet hot gas to a\ndirectly heated dryer in combination with one or a combination of the other techniques listed below; (ii) Bag filter; (iii) Cyclone; (iv) UTWS dryer and combustion with heat exchanger and thermal treatment of discharged dryer waste gasl (v) Wet electrostatic precipitator; (vi) Wet scrubber; (vii) Bioscrubber; (viii) Chemical degradation or capture of formaldehyde with chemicals in combination with a wet scrubbing system \n\n","mg/Nm3",3,10,"Green","Periodic (at least once every 6 months)",0,0,0.15,"Average over sampling period ",0,"WBP (2015) 2015/2119 \n",1.2,44,14]
[1005,"Wood-based Panels Production","6.   Other activities","6.1. (c) one or more of the following wood-based panels: oriented strand board, particleboard or fibreboard with a production capacity exceeding 600 m3 per day\n ",0,"Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Press","Emissions to air","Air","Dust ","Particulates (PM10) (24 hr Mean)","In order to prevent or reduce emissions to air from the press, BAT is to use in-duct quenching of collected press waste gas and an appropriate combination of the techniques given below.: (i) Select resins with a low formaldehyde content; (ii) Controlled operation of the press with balanced press temperature, applied pressure and press speed; (iii) Wet scrubbing of collected press\nwaste gases using Venturi scrubbers or hydrocyclones, etc.; (iv) Wet electrostatic precipitator; (v) Bioscrubber; (vi) Post-combustion as the last treatment step after application of a wet scrubber ","mg/Nm3",3,15,"Green","Periodic (at least once every 6 months)",0,0,"N/A","Average over sampling period ",0,"WBP (2015) 2015/2119 \n",1.2,46,16]
[1007,"Wood-based Panels Production","6.   Other activities","6.1. (c) one or more of the following wood-based panels: oriented strand board, particleboard or fibreboard with a production capacity exceeding 600 m3 per day\n ",0,"Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Upstream and downstream wood processing, conveying of wood materials and mat forming ","Emissions to air","Air","Dust ","Particulates (PM10) (24 hr Mean)","In order to reduce dust emissions to air from upstream and downstream wood processing, conveying of wood materials and mat forming, BAT is to use either a bag filter or a cyclofilter.","mg/Nm3",3,5,"Green","Periodic (at least once a year)",0,0,"N/A","Average over sampling period ","When a bag filter or a cyclofilter is not applicable, the upper end of the range can be up to 10 mg/Nm3","WBP (2015) 2015/2119 \n",1.2,46,16]
[1004,"Wood-based Panels Production","6.   Other activities","6.1. (c) one or more of the following wood-based panels: oriented strand board, particleboard or fibreboard with a production capacity exceeding 600 m3 per day\n ",0,"Fibre","Unspecified","Unspecified","Unspecified","Unspecified","Dryer- all types ","Emissions to air","Air","Formaldehyde","Formaldehyde","In order to prevent or reduce emissions to air from the dryer, BAT is to achieve and manage a balanced operation of the\ndrying process and to use one or a combination of the techniques given below: (i) Dust abatement of inlet hot gas to a\ndirectly heated dryer in combination with one or a combination of the other techniques listed below; (ii) Bag filter; (iii) Cyclone; (iv) UTWS dryer and combustion with heat exchanger and thermal treatment of discharged dryer waste gasl (v) Wet electrostatic precipitator; (vi) Wet scrubber; (vii) Bioscrubber; (viii) Chemical degradation or capture of formaldehyde with chemicals in combination with a wet scrubbing system \n\n","mg/Nm3",5,15,"Green","Periodic (at least once every 6 months)",0,0,"N/A","Average over sampling period ",0,"WBP (2015) 2015/2119 \n",1.2,44,14]
[1004,"Wood-based Panels Production","6.   Other activities","6.1. (c) one or more of the following wood-based panels: oriented strand board, particleboard or fibreboard with a production capacity exceeding 600 m3 per day\n ",0,"OSB","Unspecified","Unspecified","Unspecified","Unspecified","Dryer- all types ","Emissions to air","Air","Formaldehyde","Formaldehyde","In order to prevent or reduce emissions to air from the dryer, BAT is to achieve and manage a balanced operation of the\ndrying process and to use one or a combination of the techniques given below: (i) Dust abatement of inlet hot gas to a\ndirectly heated dryer in combination with one or a combination of the other techniques listed below; (ii) Bag filter; (iii) Cyclone; (iv) UTWS dryer and combustion with heat exchanger and thermal treatment of discharged dryer waste gasl (v) Wet electrostatic precipitator; (vi) Wet scrubber; (vii) Bioscrubber; (viii) Chemical degradation or capture of formaldehyde with chemicals in combination with a wet scrubbing system \n\n","mg/Nm3",5,20,"Green","Periodic (at least once every 6 months)",0,0,0.15,"Average over sampling period ",0,"WBP (2015) 2015/2119 \n",1.2,44,14]
[1003,"Wood-based Panels Production","6.   Other activities","6.1. (c) one or more of the following wood-based panels: oriented strand board, particleboard or fibreboard with a production capacity exceeding 600 m3 per day\n ",0,"PB","Unspecified","Unspecified","Unspecified","Unspecified","Dryer- all types ","Emissions to air","Air","Formaldehyde","Formaldehyde","In order to prevent or reduce emissions to air from the dryer, BAT is to achieve and manage a balanced operation of the\ndrying process and to use one or a combination of the techniques given below: (i) Dust abatement of inlet hot gas to a\ndirectly heated dryer in combination with one or a combination of the other techniques listed below; (ii) Bag filter; (iii) Cyclone; (iv) UTWS dryer and combustion with heat exchanger and thermal treatment of discharged dryer waste gasl (v) Wet electrostatic precipitator; (vi) Wet scrubber; (vii) Bioscrubber; (viii) Chemical degradation or capture of formaldehyde with chemicals in combination with a wet scrubbing system \n\n","mg/Nm3",5,10,"Green","Periodic (at least once every 6 months)",0,0,0.15,"Average over sampling period ","When using almost exclusively recovered wood, the upper end of the range may be up to 15 mg/Nm3","WBP (2015) 2015/2119 \n",1.2,44,14]
[1006,"Wood-based Panels Production","6.   Other activities","6.1. (c) one or more of the following wood-based panels: oriented strand board, particleboard or fibreboard with a production capacity exceeding 600 m3 per day\n ",0,"Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Press","Emissions to air","Air","Formaldehyde","Formaldehyde","In order to prevent or reduce emissions to air from the press, BAT is to use in-duct quenching of collected press waste gas and an appropriate combination of the techniques given below.: (i) Select resins with a low formaldehyde content; (ii) Controlled operation of the press with balanced press temperature, applied pressure and press speed; (iii) Wet scrubbing of collected press\nwaste gases using Venturi scrubbers or hydrocyclones, etc.; (iv) Wet electrostatic precipitator; (v) Bioscrubber; (vi) Post-combustion as the last treatment step after application of a wet scrubber ","mg/Nm3",2,15,"Green","Periodic (at least once every 6 months)",0,0,"N/A","Average over sampling period ",0,"WBP (2015) 2015/2119 \n",1.2,46,16]
[1008,"Wood-based Panels Production","6.   Other activities","6.1. (c) one or more of the following wood-based panels: oriented strand board, particleboard or fibreboard with a production capacity exceeding 600 m3 per day\n ",0,"Impregnation of paper ","Unspecified","Unspecified","Unspecified","Unspecified","Drying oven","Emissions to air","Air","Formaldehyde ","Formaldehyde","In order to reduce emissions of volatile organic compounds to air from the drying ovens for the impregnation of paper, BAT is to use one or a combination of the techniques given below: (i) Select and use resins with a low formaldehyde content; (ii) Controlled operation of ovens with balanced temperature\nand speed; (iii) Thermal oxidation of waste gas in a regenerative thermal\noxidiser or a catalytic thermal oxidiser; (iv) Post-combustion or incineration of waste gas in a\ncombustion plant ; (v) Wet scrubbing of waste gas followed by treatment in a\nbiofilter","mg/Nm3",5,10,"Green","Periodic (at least once a year)",0,0,"N/A","Average over sampling period ",0,"WBP (2015) 2015/2119 \n",1.2,47,17]
[1005,"Wood-based Panels Production","6.   Other activities","6.1. (c) one or more of the following wood-based panels: oriented strand board, particleboard or fibreboard with a production capacity exceeding 600 m3 per day\n ",0,"Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Dryer- Directly heated","Emissions to air","Air","NOx","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from directly heated dryers, BAT is to use technique (i) or technique (i) in combination with technique (ii): (i) Efficient operation of the combustion process using\nair- and fuel-staged combustion, while applying pulverised\ncombustion, fluidised bed boilers or moving\ngrate firing; (ii) Selective non-catalytic reduction (SNCR) by injection\nand reaction with urea or liquid ammonia","mg/Nm3",30,250,"Green","Periodic (at least once every 6 months)",0,0,"Unspecified ","Average over sampling period ",0,"WBP (2015) 2015/2119 \n",1.2,45,15]
[1003,"Wood-based Panels Production","6.   Other activities","6.1. (c) one or more of the following wood-based panels: oriented strand board, particleboard or fibreboard with a production capacity exceeding 600 m3 per day\n ",0,"Fibre","Unspecified","Unspecified","Unspecified","Unspecified","Dryer- all types ","Emissions to air","Air","TVOC","VOC","In order to prevent or reduce emissions to air from the dryer, BAT is to achieve and manage a balanced operation of the\ndrying process and to use one or a combination of the techniques given below: (i) Dust abatement of inlet hot gas to a\ndirectly heated dryer in combination with one or a combination of the other techniques listed below; (ii) Bag filter; (iii) Cyclone; (iv) UTWS dryer and combustion with heat exchanger and thermal treatment of discharged dryer waste gasl (v) Wet electrostatic precipitator; (vi) Wet scrubber; (vii) Bioscrubber; (viii) Chemical degradation or capture of formaldehyde with chemicals in combination with a wet scrubbing system \n\n","mg/Nm3",20,120,"Green","Periodic (at least once every 6 months)",0,0,"N/A","Average over sampling period ",0,"WBP (2015) 2015/2119 \n",1.2,44,14]
[1007,"Wood-based Panels Production","6.   Other activities","6.1. (c) one or more of the following wood-based panels: oriented strand board, particleboard or fibreboard with a production capacity exceeding 600 m3 per day\n ",0,"Impregnation of paper ","Unspecified","Unspecified","Unspecified","Unspecified","Drying oven","Emissions to air","Air","TVOC","VOC","In order to reduce emissions of volatile organic compounds to air from the drying ovens for the impregnation of paper, BAT is to use one or a combination of the techniques given below: (i) Select and use resins with a low formaldehyde content; (ii) Controlled operation of ovens with balanced temperature\nand speed; (iii) Thermal oxidation of waste gas in a regenerative thermal\noxidiser or a catalytic thermal oxidiser; (iv) Post-combustion or incineration of waste gas in a\ncombustion plant ; (v) Wet scrubbing of waste gas followed by treatment in a\nbiofilter","mg/Nm3",5,30,"Green","Periodic (at least once a year)",0,0,"N/A","Average over sampling period ",0,"WBP (2015) 2015/2119 \n",1.2,47,17]
[1002,"Wood-based Panels Production","6.   Other activities","6.1. (c) one or more of the following wood-based panels: oriented strand board, particleboard or fibreboard with a production capacity exceeding 600 m3 per day\n ",0,"OSB","Unspecified","Unspecified","Unspecified","Unspecified","Dryer- all types ","Emissions to air","Air","TVOC","VOC","In order to prevent or reduce emissions to air from the dryer, BAT is to achieve and manage a balanced operation of the\ndrying process and to use one or a combination of the techniques given below: (i) Dust abatement of inlet hot gas to a\ndirectly heated dryer in combination with one or a combination of the other techniques listed below; (ii) Bag filter; (iii) Cyclone; (iv) UTWS dryer and combustion with heat exchanger and thermal treatment of discharged dryer waste gasl (v) Wet electrostatic precipitator; (vi) Wet scrubber; (vii) Bioscrubber; (viii) Chemical degradation or capture of formaldehyde with chemicals in combination with a wet scrubbing system \n\n","mg/Nm3",10,400,"Green","Periodic (at least once every 6 months)",0,0,0.15,"Average over sampling period ","Emissions below 30 mg/Nm3 can be achieved using UTWS dryer.","WBP (2015) 2015/2119 \n",1.2,44,14]
[1002,"Wood-based Panels Production","6.   Other activities","6.1. (c) one or more of the following wood-based panels: oriented strand board, particleboard or fibreboard with a production capacity exceeding 600 m3 per day\n ",0,"PB","Unspecified","Unspecified","Unspecified","Unspecified","Dryer- all types ","Emissions to air","Air","TVOC","VOC","In order to prevent or reduce emissions to air from the dryer, BAT is to achieve and manage a balanced operation of the\ndrying process and to use one or a combination of the techniques given below: (i) Dust abatement of inlet hot gas to a\ndirectly heated dryer in combination with one or a combination of the other techniques listed below; (ii) Bag filter; (iii) Cyclone; (iv) UTWS dryer and combustion with heat exchanger and thermal treatment of discharged dryer waste gasl (v) Wet electrostatic precipitator; (vi) Wet scrubber; (vii) Bioscrubber; (viii) Chemical degradation or capture of formaldehyde with chemicals in combination with a wet scrubbing system \n\n","mg/Nm3",20,200,"Green","Periodic (at least once every 6 months)",0,0,0.15,"Average over sampling period ","This BAT-AEL does not apply when using pine as the predominant raw material. \n\nEmissions below 30 mg/Nm3 can be achieved using UTWS dryer. \n","WBP (2015) 2015/2119 \n",1.2,44,14]
[1006,"Wood-based Panels Production","6.   Other activities","6.1. (c) one or more of the following wood-based panels: oriented strand board, particleboard or fibreboard with a production capacity exceeding 600 m3 per day\n ",0,"Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Press","Emissions to air","Air","TVOC","VOC","In order to prevent or reduce emissions to air from the press, BAT is to use in-duct quenching of collected press waste gas and an appropriate combination of the techniques given below.: (i) Select resins with a low formaldehyde content; (ii) Controlled operation of the press with balanced press temperature, applied pressure and press speed; (iii) Wet scrubbing of collected press\nwaste gases using Venturi scrubbers or hydrocyclones, etc.; (iv) Wet electrostatic precipitator; (v) Bioscrubber; (vi) Post-combustion as the last treatment step after application of a wet scrubber ","mg/Nm3",10,100,"Green","Periodic (at least once every 6 months)",0,0,"N/A","Average over sampling period ",0,"WBP (2015) 2015/2119 \n",1.2,46,16]
[1009,"Wood-based Panels Production","6.   Other activities","6.1. (c) one or more of the following wood-based panels: oriented strand board, particleboard or fibreboard with a production capacity exceeding 600 m3 per day\n ",0,"Wood fibre","Unspecified","Unspecified","Unspecified","Unspecified","All plant","Emissions to water ","Water","COD","COD","In order to reduce emissions to water from wood fibre production, BAT is to use a combination of the techniques given below: (i) Mechanical separation of coarse materials by screens\nand sieves; (ii) Physico-chemical separation, e.g. using sand filters,\ndissolved air flotation, coagulation and flocculation; (iii) Biological treatment","mg/l",20,200,"Green","Periodic (at least once a week) ",0,0,"N/A","Average of samples obtained during one year ",0,"WBP (2015) 2015/2119 \n",1.3,49,19]
[1008,"Wood-based Panels Production","6.   Other activities","6.1. (c) one or more of the following wood-based panels: oriented strand board, particleboard or fibreboard with a production capacity exceeding 600 m3 per day\n ",0,"Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Surface run-off ","Emissions to water ","Water","Total Suspended Solids (TSS) ","Total Suspended Solids (TSS) ","In order to reduce emissions to water from surface run-off water, BAT is to use a combination of the techniques given below: (i) Mechanical separation of coarse materials by screens\nand sieves as preliminary treatment; (ii) Oil-water separation; (iii) Removal of solids by sedimentation in retention basins\nor settlement tanks","mg/l",10,40,"Green","Periodic (at least once every 3 months) ",0,0,"N/A","Average of samples obtained during one year ",0,"WBP (2015) 2015/2119 \n","1.2.2",48,18]
[1009,"Wood-based Panels Production","6.   Other activities","6.1. (c) one or more of the following wood-based panels: oriented strand board, particleboard or fibreboard with a production capacity exceeding 600 m3 per day\n ",0,"Wood fibre","Unspecified","Unspecified","Unspecified","Unspecified","All plant","Emissions to water ","Water","Total Suspended Solids (TSS) ","Total Suspended Solids (TSS) ","In order to reduce emissions to water from wood fibre production, BAT is to use a combination of the techniques given below: (i) Mechanical separation of coarse materials by screens\nand sieves; (ii) Physico-chemical separation, e.g. using sand filters,\ndissolved air flotation, coagulation and flocculation; (iii) Biological treatment","mg/l",5,35,"Green","Periodic (at least once a week) ",0,0,"N/A","Average of samples obtained during one year ",0,"WBP (2015) 2015/2119 \n",1.3,49,19]
[1308,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Copper","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Emissions to water","Water","Cadmium (Cd)","Cadmium and its compounds (≥ 200 mg/l CaCO3)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l",0.02,0.1,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[1313,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Ferro-alloys Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates",0,"Water","Cadmium (Cd)","Cadmium and its compounds (≥ 200 mg/l CaCO3)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.05,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[1309,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Lead and/or Tin Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Emissions to water","Water","Cadmium (Cd)","Cadmium and its compounds (≥ 200 mg/l CaCO3)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.1,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[1312,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Nickel and/or Cobalt Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates",0,"Water","Cadmium (Cd)","Cadmium and its compounds (≥ 200 mg/l CaCO3)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.1,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[1311,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Precious metals","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates",0,"Water","Cadmium (Cd)","Cadmium and its compounds (≥ 200 mg/l CaCO3)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.05,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[1310,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Zinc and/or Cadmium Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Emissions to water","Water","Cadmium (Cd)","Cadmium and its compounds (≥ 200 mg/l CaCO3)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.1,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[903,"Refineries","1. Energy industries","1.2. Refining of mineral oil and gas",0,0,"All","Unspecified","All","Unspecified","Whole refinery ","Emission to water","Water","Cadmium, expressed as Cd","Cadmium and its compounds (≥ 200 mg/l CaCO3)","Removal of insoluble substances by recovering oil: \n— API Separators (APIs)\n— Corrugated Plate Interceptors (CPIs)\n— Parallel Plate Interceptors (PPIs)\n— Tilted Plate Interceptors (TPIs)\n— Buffer and/or equalisation tanks \n\nRemoval of insoluble substances by recovering suspended solid and dispersed oil:\nThese techniques generally include:\n— Dissolved Gas Flotation (DGF)\n— Induced Gas Flotation (IGF)\n— Sand Filtration \n\nRemoval of soluble substances including biological treatment and clarification:\nBiological treatment techniques may include:\n— Fixed bed systems\n— Suspended bed systems.\nOne of the most commonly used suspended bed system in refineries WWTP is\nthe activated sludge process. Fixed bed systems may include a biofilter or trickling\nfilter\n\nAdditional treatment step:\nA specific waste water treatment intended to complement the previous treatment\nsteps e.g. for further reducing nitrogen or carbon compounds. Generally used\nwhere specific local requirements for water preservation exist\n","mg/l",2E-3,8.0000000000000002E-3,"Green","Quarterly",0,0,"N/A","Yearly ","Refers to a flow-proportional composite sample taken over a period of 24 hours or, provided that sufficient flow stability is demonstrated, a time-proportional sample.\n\nNot all parameters and sampling frequencies are applicable to effluent from gas refining sites","REF(2014)\n2014/738/EU","1.1.7",15,52]
[1308,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Copper","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Emissions to water","Water","Cadmium (Cd)","Cadmium and its compounds (100 - <200 mg/l CaCO3)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l",0.02,0.1,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[1313,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Ferro-alloys Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates",0,"Water","Cadmium (Cd)","Cadmium and its compounds (100 - <200 mg/l CaCO3)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.05,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[1309,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Lead and/or Tin Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Emissions to water","Water","Cadmium (Cd)","Cadmium and its compounds (100 - <200 mg/l CaCO3)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.1,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[1312,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Nickel and/or Cobalt Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates",0,"Water","Cadmium (Cd)","Cadmium and its compounds (100 - <200 mg/l CaCO3)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.1,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[1311,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Precious metals","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates",0,"Water","Cadmium (Cd)","Cadmium and its compounds (100 - <200 mg/l CaCO3)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.05,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[1310,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Zinc and/or Cadmium Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Emissions to water","Water","Cadmium (Cd)","Cadmium and its compounds (100 - <200 mg/l CaCO3)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.1,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[903,"Refineries","1. Energy industries","1.2. Refining of mineral oil and gas",0,0,"All","Unspecified","All","Unspecified","Whole refinery ","Emission to water","Water","Cadmium, expressed as Cd","Cadmium and its compounds (100 - <200 mg/l CaCO3)","Removal of insoluble substances by recovering oil: \n— API Separators (APIs)\n— Corrugated Plate Interceptors (CPIs)\n— Parallel Plate Interceptors (PPIs)\n— Tilted Plate Interceptors (TPIs)\n— Buffer and/or equalisation tanks \n\nRemoval of insoluble substances by recovering suspended solid and dispersed oil:\nThese techniques generally include:\n— Dissolved Gas Flotation (DGF)\n— Induced Gas Flotation (IGF)\n— Sand Filtration \n\nRemoval of soluble substances including biological treatment and clarification:\nBiological treatment techniques may include:\n— Fixed bed systems\n— Suspended bed systems.\nOne of the most commonly used suspended bed system in refineries WWTP is\nthe activated sludge process. Fixed bed systems may include a biofilter or trickling\nfilter\n\nAdditional treatment step:\nA specific waste water treatment intended to complement the previous treatment\nsteps e.g. for further reducing nitrogen or carbon compounds. Generally used\nwhere specific local requirements for water preservation exist\n","mg/l",2E-3,8.0000000000000002E-3,"Green","Quarterly",0,0,"N/A","Yearly ","Refers to a flow-proportional composite sample taken over a period of 24 hours or, provided that sufficient flow stability is demonstrated, a time-proportional sample.\n\nNot all parameters and sampling frequencies are applicable to effluent from gas refining sites","REF(2014)\n2014/738/EU","1.1.7",15,52]
[1308,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Copper","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Emissions to water","Water","Cadmium (Cd)","Cadmium and its compounds (40 - < 50 mg/l CaCO3)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l",0.02,0.1,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[1313,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Ferro-alloys Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates",0,"Water","Cadmium (Cd)","Cadmium and its compounds (40 - < 50 mg/l CaCO3)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.05,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[1309,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Lead and/or Tin Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Emissions to water","Water","Cadmium (Cd)","Cadmium and its compounds (40 - < 50 mg/l CaCO3)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.1,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[1312,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Nickel and/or Cobalt Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates",0,"Water","Cadmium (Cd)","Cadmium and its compounds (40 - < 50 mg/l CaCO3)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.1,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[1311,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Precious metals","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates",0,"Water","Cadmium (Cd)","Cadmium and its compounds (40 - < 50 mg/l CaCO3)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.05,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[1310,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Zinc and/or Cadmium Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Emissions to water","Water","Cadmium (Cd)","Cadmium and its compounds (40 - < 50 mg/l CaCO3)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.1,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[903,"Refineries","1. Energy industries","1.2. Refining of mineral oil and gas",0,0,"All","Unspecified","All","Unspecified","Whole refinery ","Emission to water","Water","Cadmium, expressed as Cd","Cadmium and its compounds (40 - < 50 mg/l CaCO3)","Removal of insoluble substances by recovering oil: \n— API Separators (APIs)\n— Corrugated Plate Interceptors (CPIs)\n— Parallel Plate Interceptors (PPIs)\n— Tilted Plate Interceptors (TPIs)\n— Buffer and/or equalisation tanks \n\nRemoval of insoluble substances by recovering suspended solid and dispersed oil:\nThese techniques generally include:\n— Dissolved Gas Flotation (DGF)\n— Induced Gas Flotation (IGF)\n— Sand Filtration \n\nRemoval of soluble substances including biological treatment and clarification:\nBiological treatment techniques may include:\n— Fixed bed systems\n— Suspended bed systems.\nOne of the most commonly used suspended bed system in refineries WWTP is\nthe activated sludge process. Fixed bed systems may include a biofilter or trickling\nfilter\n\nAdditional treatment step:\nA specific waste water treatment intended to complement the previous treatment\nsteps e.g. for further reducing nitrogen or carbon compounds. Generally used\nwhere specific local requirements for water preservation exist\n","mg/l",2E-3,8.0000000000000002E-3,"Green","Quarterly",0,0,"N/A","Yearly ","Refers to a flow-proportional composite sample taken over a period of 24 hours or, provided that sufficient flow stability is demonstrated, a time-proportional sample.\n\nNot all parameters and sampling frequencies are applicable to effluent from gas refining sites","REF(2014)\n2014/738/EU","1.1.7",15,52]
[1308,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Copper","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Emissions to water","Water","Cadmium (Cd)","Cadmium and its compounds (50 - <100 mg/l CaCO3)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l",0.02,0.1,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[1313,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Ferro-alloys Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates",0,"Water","Cadmium (Cd)","Cadmium and its compounds (50 - <100 mg/l CaCO3)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.05,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[1309,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Lead and/or Tin Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Emissions to water","Water","Cadmium (Cd)","Cadmium and its compounds (50 - <100 mg/l CaCO3)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.1,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[1312,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Nickel and/or Cobalt Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates",0,"Water","Cadmium (Cd)","Cadmium and its compounds (50 - <100 mg/l CaCO3)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.1,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[1311,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Precious metals","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates",0,"Water","Cadmium (Cd)","Cadmium and its compounds (50 - <100 mg/l CaCO3)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.05,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[1310,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Zinc and/or Cadmium Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Emissions to water","Water","Cadmium (Cd)","Cadmium and its compounds (50 - <100 mg/l CaCO3)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.1,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[903,"Refineries","1. Energy industries","1.2. Refining of mineral oil and gas",0,0,"All","Unspecified","All","Unspecified","Whole refinery ","Emission to water","Water","Cadmium, expressed as Cd","Cadmium and its compounds (50 - <100 mg/l CaCO3)","Removal of insoluble substances by recovering oil: \n— API Separators (APIs)\n— Corrugated Plate Interceptors (CPIs)\n— Parallel Plate Interceptors (PPIs)\n— Tilted Plate Interceptors (TPIs)\n— Buffer and/or equalisation tanks \n\nRemoval of insoluble substances by recovering suspended solid and dispersed oil:\nThese techniques generally include:\n— Dissolved Gas Flotation (DGF)\n— Induced Gas Flotation (IGF)\n— Sand Filtration \n\nRemoval of soluble substances including biological treatment and clarification:\nBiological treatment techniques may include:\n— Fixed bed systems\n— Suspended bed systems.\nOne of the most commonly used suspended bed system in refineries WWTP is\nthe activated sludge process. Fixed bed systems may include a biofilter or trickling\nfilter\n\nAdditional treatment step:\nA specific waste water treatment intended to complement the previous treatment\nsteps e.g. for further reducing nitrogen or carbon compounds. Generally used\nwhere specific local requirements for water preservation exist\n","mg/l",2E-3,8.0000000000000002E-3,"Green","Quarterly",0,0,"N/A","Yearly ","Refers to a flow-proportional composite sample taken over a period of 24 hours or, provided that sufficient flow stability is demonstrated, a time-proportional sample.\n\nNot all parameters and sampling frequencies are applicable to effluent from gas refining sites","REF(2014)\n2014/738/EU","1.1.7",15,52]
[608,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Unspecified","Unspecified","Unspecified","Unspecified",0,"Direct discharges from flue-gas treatment  to receiving water body","Water","Cd","Cadmium and its compounds (≥ 200 mg/l CaCO3)","In order to reduce emissions to water from flue-gas treatment, BAT is to use an appropriate combination of the techniques given below, and to use secondary techniques as close as possible to the source in order to avoid dilution: (i) Optimised combustion (see BAT 6) and flue-gas treatment systems (e.g. SCR/SNCR, see BAT 7); (ii) Adsorption on activated carbon; (iii) Aerobic biological treatment; (iv) Anoxic/anaerobic biological treatment; (v) Coagulation and flocculation; (vi) Crystallisation; (vii) Filtration (e.g. sand filtration, microfiltration, ultrafiltration); (viii) Flotation; (ix) Ion exchange; (x) Neutralisation; (xi) Oxidation; (xii) Precipitation; (xiii) Sedimentation; (xiv) Stripping","ug/l",2,5,"Green","Once every month",0,0,"Unspecified ","Daily ",0,"LCP (2017)\n2017/1450",1.5,25,25]
[608,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Unspecified","Unspecified","Unspecified","Unspecified",0,"Direct discharges from flue-gas treatment  to receiving water body","Water","Cd","Cadmium and its compounds (100 - <200 mg/l CaCO3)","In order to reduce emissions to water from flue-gas treatment, BAT is to use an appropriate combination of the techniques given below, and to use secondary techniques as close as possible to the source in order to avoid dilution: (i) Optimised combustion (see BAT 6) and flue-gas treatment systems (e.g. SCR/SNCR, see BAT 7); (ii) Adsorption on activated carbon; (iii) Aerobic biological treatment; (iv) Anoxic/anaerobic biological treatment; (v) Coagulation and flocculation; (vi) Crystallisation; (vii) Filtration (e.g. sand filtration, microfiltration, ultrafiltration); (viii) Flotation; (ix) Ion exchange; (x) Neutralisation; (xi) Oxidation; (xii) Precipitation; (xiii) Sedimentation; (xiv) Stripping","ug/l",2,5,"Green","Once every month",0,0,"Unspecified ","Daily ",0,"LCP (2017)\n2017/1450",1.5,25,25]
[608,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Unspecified","Unspecified","Unspecified","Unspecified",0,"Direct discharges from flue-gas treatment  to receiving water body","Water","Cd","Cadmium and its compounds (40 - < 50 mg/l CaCO3)","In order to reduce emissions to water from flue-gas treatment, BAT is to use an appropriate combination of the techniques given below, and to use secondary techniques as close as possible to the source in order to avoid dilution: (i) Optimised combustion (see BAT 6) and flue-gas treatment systems (e.g. SCR/SNCR, see BAT 7); (ii) Adsorption on activated carbon; (iii) Aerobic biological treatment; (iv) Anoxic/anaerobic biological treatment; (v) Coagulation and flocculation; (vi) Crystallisation; (vii) Filtration (e.g. sand filtration, microfiltration, ultrafiltration); (viii) Flotation; (ix) Ion exchange; (x) Neutralisation; (xi) Oxidation; (xii) Precipitation; (xiii) Sedimentation; (xiv) Stripping","ug/l",2,5,"Green","Once every month",0,0,"Unspecified ","Daily ",0,"LCP (2017)\n2017/1450",1.5,25,25]
[608,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Unspecified","Unspecified","Unspecified","Unspecified",0,"Direct discharges from flue-gas treatment  to receiving water body","Water","Cd","Cadmium and its compounds (50 - <100 mg/l CaCO3)","In order to reduce emissions to water from flue-gas treatment, BAT is to use an appropriate combination of the techniques given below, and to use secondary techniques as close as possible to the source in order to avoid dilution: (i) Optimised combustion (see BAT 6) and flue-gas treatment systems (e.g. SCR/SNCR, see BAT 7); (ii) Adsorption on activated carbon; (iii) Aerobic biological treatment; (iv) Anoxic/anaerobic biological treatment; (v) Coagulation and flocculation; (vi) Crystallisation; (vii) Filtration (e.g. sand filtration, microfiltration, ultrafiltration); (viii) Flotation; (ix) Ion exchange; (x) Neutralisation; (xi) Oxidation; (xii) Precipitation; (xiii) Sedimentation; (xiv) Stripping","ug/l",2,5,"Green","Once every month",0,0,"Unspecified ","Daily ",0,"LCP (2017)\n2017/1450",1.5,25,25]
[1107,"Common Waste Water and Waste Gas Treatment","4. Chemical industry","4: Chemical industry;\n6.11: Independently operated treatment of waste water not covered by Council Directive 91/271/EEC and discharged by an installation undertaking activities covered under Section 4 of Annex I to Directive 2010/75/EU.\n \n",0,0,"Unspecified","Unspecified","Unspecified","Unspecified","Whole plant","Emissions to water","Water","Chromium (expressed as Cr) ","Chromium III (95%ile) (dissolved)","Appropriate final waste water treatment techniques, depending on the pollutant, include:\n\nPreliminary and primary treatment:(i) Equalisation; (ii) Neutralisation; (iii) Physical separation, e.g.\nscreens, sieves, grit separators,\ngrease separators or\nprimary settlement tanks \n\nBiological treatment: (i) Activated sludge process; (ii) Membrane bioreactor\n\nNitrogen removal: (i) Nitrification/denitrification\n\nPhosphorus removal: (i) Chemical precipitation\n\nFinal solids removal: (i) Coagulation and flocculation; (ii) Sedimentation; (iii) Filtration (e.g. sand filtration,\nmicrofiltration, ultrafiltration); (iv) Flotation\n","mg/l",5,25,"Green","Monthly",0,0,"N/A","Yearly","The lower end of the range is typically achieved when few of the corresponding metal (compounds) are used or produced by the installation\n\nThis BAT-AEL may not apply to inorganic effluents when the main pollutant load originates from the production of inorganic\nheavy metal compounds.\n\nThis BAT-AEL may not apply when the main pollutant load originates from the processing of large volumes of solid inorganic raw\nmaterials that are contaminated with metals (e.g. soda ash from the Solvay process, titanium dioxide).       \n\nThis BAT-AEL may not apply when the main pollutant load originates from the production of chromium-organic compounds.","CWW (2016) 2016/902 \n",3.4,35,13]
[1316,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Ferro-alloys Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates",0,"Water","Chromium total (Cr)","Chromium III (95%ile) (dissolved)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.2,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[609,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"Unspecified","Unspecified","Unspecified","Unspecified",0,"Direct discharges from flue-gas treatment  to receiving water body","Water","Cr","Chromium III (95%ile) (dissolved)","In order to reduce emissions to water from flue-gas treatment, BAT is to use an appropriate combination of the techniques given below, and to use secondary techniques as close as possible to the source in order to avoid dilution: (i) Optimised combustion (see BAT 6) and flue-gas treatment systems (e.g. SCR/SNCR, see BAT 7); (ii) Adsorption on activated carbon; (iii) Aerobic biological treatment; (iv) Anoxic/anaerobic biological treatment; (v) Coagulation and flocculation; (vi) Crystallisation; (vii) Filtration (e.g. sand filtration, microfiltration, ultrafiltration); (viii) Flotation; (ix) Ion exchange; (x) Neutralisation; (xi) Oxidation; (xii) Precipitation; (xiii) Sedimentation; (xiv) Stripping","ug/l",10,50,"Green","Once every month",0,0,"Unspecified ","Daily ",0,"LCP (2017)\n2017/1451",1.5,25,25]
[1314,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Lead and/or Tin Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates",0,"Water","Cobalt (Co)","Cobalt (dissolved)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.1,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[1315,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Nickel and/or Cobalt Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates",0,"Water","Cobalt (Co)","Cobalt (dissolved)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l",0.1,0.5,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[1301,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Precious metals","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Emissions to water","Water","Silver (Ag)","Silver (dissolved)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.6,"Green","Once per month",0,0,0,"Daily average",0,"NFM (2016) 2016/1032 \n","1.1.9",49,18]
[904,"Refineries","1. Energy industries","1.2. Refining of mineral oil and gas",0,0,"All","Unspecified","All","Unspecified","Whole refinery ","Emission to water","Water","Vanadium","Vanadium (0 - 200 mg/l CaCO3)","Removal of insoluble substances by recovering oil: \n— API Separators (APIs)\n— Corrugated Plate Interceptors (CPIs)\n— Parallel Plate Interceptors (PPIs)\n— Tilted Plate Interceptors (TPIs)\n— Buffer and/or equalisation tanks \n\nRemoval of insoluble substances by recovering suspended solid and dispersed oil:\nThese techniques generally include:\n— Dissolved Gas Flotation (DGF)\n— Induced Gas Flotation (IGF)\n— Sand Filtration \n\nRemoval of soluble substances including biological treatment and clarification:\nBiological treatment techniques may include:\n— Fixed bed systems\n— Suspended bed systems.\nOne of the most commonly used suspended bed system in refineries WWTP is\nthe activated sludge process. Fixed bed systems may include a biofilter or trickling\nfilter\n\nAdditional treatment step:\nA specific waste water treatment intended to complement the previous treatment\nsteps e.g. for further reducing nitrogen or carbon compounds. Generally used\nwhere specific local requirements for water preservation exist\n","mg/l","N/A","N/A","Green","Quarterly",0,0,"N/A","Yearly ","Refers to a flow-proportional composite sample taken over a period of 24 hours or, provided that sufficient flow stability is demonstrated, a time-proportional sample.\n\nNot all parameters and sampling frequencies are applicable to effluent from gas refining sites","REF(2014)\n2014/738/EU","1.1.7",15,52]
[1077,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Filament glass fibre","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes (forming and coating)","Emissions to air","Air","Ammonia","Ammonia (human health receptor)","BAT is to reduce emissions from downstream processes by using one or a combination of the following techniques: (i) Wet scrubbing systems; (ii) Wet electrostatic precipitator; (iii) Filtration system (bag filter)","mg/Nm3","N/A","20","Amber",0,"273.15","101.3","N/A","Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.4.6",32,32]
[1187,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes- Curing oven emissions ","Emissions to air","Air","Ammonia","Ammonia (human health receptor)","BAT is to reduce emissions from downstream processes by using one or a combination of the following techniques: (i) Impact jets and cyclones; (ii) Wet scrubbers; (iii) Wet electrostatic precipitators; (iv) Stone wool filters; (v) Waste gas incineration","mg/Nm3","20","60","Green","Continuous or regular periodic measurements of NH 3 emissions, when selective catalytic reduction (SCR) or selective non-catalytic reduction (SNCR) techniques are applied","273.15","101.3","N/A","Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.7.7",50,50]
[1184,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes- Curing oven emissions ","Emissions to air","Air","Ammonia","Ammonia (human health receptor)","BAT is to reduce emissions from downstream processes by using one or a combination of the following techniques: (i) Impact jets and cyclones; (ii) Wet scrubbers; (iii) Wet electrostatic precipitators; (iv) Stone wool filters; (v) Waste gas incineration","kg/tonne melted glass","N/A","0.4","Amber",0,"273.15","101.3","N/A","Daily average (continuous)","The specific mass emissions refer to 1 tonne of produced glass","GLS (2012) - 2012/134/EU","1.7.7",50,50]
[1178,"Glass","3. Mineral industry","3.3. Manufacture of glass including glass fibre with a melting capacity exceeding 20 tonnes per day;","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes- Forming area ","Emissions to air","Air","Ammonia","Ammonia (human health receptor)","BAT is to reduce emissions from downstream processes by using one or a combination of the following techniques: (i) Impact jets and cyclones; (ii) Wet scrubbers; (iii) Wet electrostatic precipitators; (iv) Stone wool filters; (v) Waste gas incineration","mg/Nm3","30","60","Green","Continuous or regular periodic measurements of NH 3 emissions, when selective catalytic reduction (SCR) or selective non-catalytic reduction (SNCR) techniques are applied","273.15","101.3","N/A","Daily average (continuous)",0,"GLS (2012) - 2012/134/EU","1.7.7",49,49]
[900,"Refineries","1. Energy industries","1.2. Refining of mineral oil and gas",0,0,"All","Unspecified","All","Unspecified","All units equipped with SCR or SNCR","Emission to air ","Air","Ammonia expressed as NH3","Ammonia (human health receptor)","In order to prevent and reduce ammonia (NH3) emissions to air when applying selective catalytic reduction (SCR) or selective non-catalytic reduction (SNCR) techniques, BAT is to maintain suitable operating conditions of the SCR or SNCR waste gas treatment systems, with the aim of limiting emissions of unreacted NH3.","mg/Nm3",5,15,"Green","Continuous",0,0,0.03,"Monthly average","The higher end of the range is associated with higher inlet NOX concentrations, higher NOX reduction rates and the ageing\nof the catalyst. \n\nThe lower end of the range is associated with the use of the SCR technique. ","REF(2014)\n2014/738/EU","1.1.5",50,13]
[1239,"Iron and steel","2. Production and processing of metals","1.3. Coke production","Coke Oven Plants",0,"Unspecified","Unspecified","Unspecified","Unspecified","Coke grading and handling","Emissions to air ","Air","Dust","Particulates (PM10) (Annual Mean)","BAT for coke grading and handling is to prevent or reduce dust emissions by using the following techniques in combination: (i)use of building or device enclosures; (ii) efficient extraction and subsequent dry dedusting ","mg/Nm3","N/A",10,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0,"IS (2012)\n2012/135/EU",1.4,88,26]
[1235,"Iron and steel","2. Production and processing of metals","1.3. Coke production","Coke Oven Plants",0,"Unspecified","Unspecified","Unspecified","Unspecified","Coke pushing","Emissions to air ","Air","Dust","Particulates (PM10) (Annual Mean)","BAT for coke pushing is to reduce dust emissions by using the following techniques: (i)  extraction by means of an integrated coke transfer machine equipped with a hood; (ii) using a one point or a mobile quenching car","mg/Nm3","N/A",20,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0,"IS (2012)\n2012/135/EU",1.4,87,25]
[1234,"Iron and steel","2. Production and processing of metals","1.3. Coke production","Coke Oven Plants",0,"Unspecified","Unspecified","Unspecified","Unspecified","Coke pushing","Emissions to air ","Air","Dust","Particulates (PM10) (Annual Mean)","BAT for coke pushing is to reduce dust emissions by using the following techniques: (i) using land-based extraction gas treatment with a bag filter or other abatement systems","mg/Nm3","N/A",10,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0,"IS (2012)\n2012/135/EU",1.4,87,25]
[1236,"Iron and steel","2. Production and processing of metals","1.3. Coke production","Coke Oven Plants",0,"Unspecified","Unspecified","Unspecified","Unspecified","Coke quenching","Emissions to air ","Air","Dust","Particulates (PM10) (Annual Mean)","BAT for coke quenching is to reduce dust emissions by using one of the following techniques: (i) using coke dry quenching (CDQ) with the recovery of sensible heat and the removal of dust from charging, handling\nand screening operations by means of a bag filter","mg/Nm3","N/A",20,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0,"IS (2012)\n2012/135/EU",1.4,88,26]
[1238,"Iron and steel","2. Production and processing of metals","1.3. Coke production","Coke Oven Plants",0,"Unspecified","Unspecified","Unspecified","Unspecified","Coke quenching","Emissions to air ","Air","Dust","Particulates (PM10) (Annual Mean)","BAT for coke quenching is to reduce dust emissions by using one of the following techniques: (i) using coke stabilisation quenching (CSQ)","g/t","N/A",10,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0,"IS (2012)\n2012/135/EU",1.4,88,26]
[1237,"Iron and steel","2. Production and processing of metals","1.3. Coke production","Coke Oven Plants",0,"Unspecified","Unspecified","Unspecified","Unspecified","Coke quenching","Emissions to air ","Air","Dust","Particulates (PM10) (Annual Mean)","BAT for coke quenching is to reduce dust emissions by using one of the following techniques: (i) using emission-minimised conventional wet quenching","g/t","N/A",25,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0,"IS (2012)\n2012/135/EU",1.4,88,26]
[1259,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.",0,0,"Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: Basic oxygen furnace (BOF) gas recovery by supressed combustion","Emissions to air ","Air","Dust","Particulates (PM10) (Annual Mean)","BAT for basic oxygen furnace (BOF) gas recovery by suppressed combustion is to extract the BOF gas during blowing as much as possible and to clean it by using the following techniques in combination: (i) use of a suppressed combustion process; (ii) prededusting to remove coarse dust by means of dry separation techniques (e.g. deflector, cyclone) or wet separators; (iii) dust abatement by means of dry dedusting for new and existing plants or wet dedusting for existing plants\n","mg/Nm3",10,30,"Green","Continuous",0,0,"Unspecified ",0,"This BAT AEL is for dust abatement by dry dedusting","IS (2012)\n2012/135/EU",1.6,93,31]
[1260,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.",0,0,"Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: Basic oxygen furnace (BOF) gas recovery by supressed combustion","Emissions to air ","Air","Dust","Particulates (PM10) (Annual Mean)","BAT for basic oxygen furnace (BOF) gas recovery by suppressed combustion is to extract the BOF gas during blowing as much as possible and to clean it by using the following techniques in combination: (i) use of a suppressed combustion process; (ii) prededusting to remove coarse dust by means of dry separation techniques (e.g. deflector, cyclone) or wet separators; (iii) dust abatement by means of dry dedusting for new and existing plants or wet dedusting for existing plants\n","mg/Nm3","N/A",50,"Green","Continuous",0,0,"Unspecified ",0,"This BAT AEL is for dust abatement by wet dedusting","IS (2012)\n2012/135/EU",1.6,93,31]
[1261,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.",0,0,"Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: Basic oxygen furnace (BOF) gas recovery during oxygen blowing in the case of full combustion","Emissions to air ","Air","Dust","Particulates (PM10) (Annual Mean)","BAT for basic oxygen furnace (BOF) gas recovery during oxygen blowing in the case of full combustion is to\nreduce dust emissions by using one of the following techniques:  dry dedusting (e.g. ESP or bag filter) for new and existing plants","mg/Nm3",10,30,"Green","Continuous",0,0,"Unspecified ","Average over the sampling period",0,"IS (2012)\n2012/135/EU",1.6,93,31]
[1262,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.",0,0,"Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: Basic oxygen furnace (BOF) gas recovery during oxygen blowing in the case of full combustion","Emissions to air ","Air","Dust","Particulates (PM10) (Annual Mean)","BAT for basic oxygen furnace (BOF) gas recovery during oxygen blowing in the case of full combustion is to\nreduce dust emissions by using one of the following techniques:  wet dedusting (e.g. ESP or bag filter) for existing plants","mg/Nm3","N/A",50,"Green","Continuous",0,0,"Unspecified ","Average over the sampling period",0,"IS (2012)\n2012/135/EU",1.6,93,31]
[1267,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.",0,0,"Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: On-site slag processing ","Emissions to air ","Air","Dust","Particulates (PM10) (Annual Mean)","BAT for on-site slag processing is to reduce dust emissions by using one or a combination of the following\ntechniques: (i) Efficient extraction of the slag crusher and screening devices with subsequent off-gas cleaning, if relevant; (ii) transport of untreated slag by shovel loaders; (iii) extraction or wetting of conveyor transfer points for broken material; (iv) wetting of slag storage heaps; (v) use of water fogs when broken slag is loaded\n","mg/Nm3",10,20,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0,"IS (2012)\n2012/135/EU",1.6,94,32]
[1268,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.",0,0,"Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: Waste water from continous casting machines ","Emissions to air ","Air","Dust","Particulates (PM10) (Annual Mean)","BAT is to minimise the waste water discharge from continuous casting by using the following techniques in combination: (i) the removal of solids by flocculation, sedimentation and/or filtration; (ii) the removal of oil in skimming tanks or any other effective device; (iii) the recirculation of cooling water and water from vacuum generation as much as possible.","mg/l","N/A",20,"Green","Discontinuous ",0,0,"Unspecified ","Random sample or a 24 hour composite sample ",0,"IS (2012)\n2012/135/EU",1.6,95,33]
[1269,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.",0,0,"Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: Waste water from continous casting machines ","Emissions to air ","Air","Dust","Particulates (PM10) (Annual Mean)","BAT is to minimise the waste water discharge from continuous casting by using the following techniques in combination: (i) the removal of solids by flocculation, sedimentation and/or filtration; (ii) the removal of oil in skimming tanks or any other effective device; (iii) the recirculation of cooling water and water from vacuum generation as much as possible.","mg/l","N/A",5,"Green","Discontinuous ",0,0,"Unspecified ","Random sample or a 24 hour composite sample ",0,"IS (2012)\n2012/135/EU",1.6,95,33]
[1270,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.",0,0,"Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: Waste water from continous casting machines ","Emissions to air ","Air","Dust","Particulates (PM10) (Annual Mean)","BAT is to minimise the waste water discharge from continuous casting by using the following techniques in combination: (i) the removal of solids by flocculation, sedimentation and/or filtration; (ii) the removal of oil in skimming tanks or any other effective device; (iii) the recirculation of cooling water and water from vacuum generation as much as possible.","mg/l","N/A",2,"Green","Discontinuous ",0,0,"Unspecified ","Random sample or a 24 hour composite sample ",0,"IS (2012)\n2012/135/EU",1.6,95,33]
[1271,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.",0,0,"Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: Waste water from continous casting machines ","Emissions to air ","Air","Dust","Particulates (PM10) (Annual Mean)","BAT is to minimise the waste water discharge from continuous casting by using the following techniques in combination: (i) the removal of solids by flocculation, sedimentation and/or filtration; (ii) the removal of oil in skimming tanks or any other effective device; (iii) the recirculation of cooling water and water from vacuum generation as much as possible.","mg/l","N/A",0.5,"Green","Discontinuous ",0,0,"Unspecified ","Random sample or a 24 hour composite sample ",0,"IS (2012)\n2012/135/EU",1.6,95,33]
[1272,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.",0,0,"Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: Waste water from continous casting machines ","Emissions to air ","Air","Dust","Particulates (PM10) (Annual Mean)","BAT is to minimise the waste water discharge from continuous casting by using the following techniques in combination: (i) the removal of solids by flocculation, sedimentation and/or filtration; (ii) the removal of oil in skimming tanks or any other effective device; (iii) the recirculation of cooling water and water from vacuum generation as much as possible.","mg/l","N/A",0.5,"Green","Discontinuous ",0,0,"Unspecified ","Random sample or a 24 hour composite sample ",0,"IS (2012)\n2012/135/EU",1.6,95,33]
[1273,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.",0,0,"Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: Waste water from continous casting machines ","Emissions to air ","Air","Dust","Particulates (PM10) (Annual Mean)","BAT is to minimise the waste water discharge from continuous casting by using the following techniques in combination: (i) the removal of solids by flocculation, sedimentation and/or filtration; (ii) the removal of oil in skimming tanks or any other effective device; (iii) the recirculation of cooling water and water from vacuum generation as much as possible.","mg/l","N/A",5,"Green","Discontinuous ",0,0,"Unspecified ","Random sample or a 24 hour composite sample ",0,"IS (2012)\n2012/135/EU",1.6,95,33]
[1250,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.",0,0,"Unspecified","Unspecified","Unspecified","Unspecified","Blast Furnaces: Blast furnace gas ","Emissions to air ","Air","Dust","Particulates (PM10) (Annual Mean)","BAT is to reduce dust emissions from the blast furnace gas by using one or a combination of the following techniques:\n\nUsing dry predusting devices: (i) deflectors; (ii) dust catchers; (iii) cyclones; (iv) electrostatic precipitators.\n\nSubsequent dust abatement: (i) hurdle-type scrubbers; (ii) venturi scrubbers; (iii) annular gap scrubbers; (iv) wet electrostatic precipitators; (v) disintegrators ","mg/Nm3","N/A",10,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0,"IS (2012)\n2012/135/EU",1.5,90,28]
[1248,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.",0,0,"Unspecified","Unspecified","Unspecified","Unspecified","Blast Furnaces: Loading from the storage bunkers of the coal injection unit","Emissions to air ","Air","Dust","Particulates (PM10) (Annual Mean)","BAT for displaced air during loading from the storage bunkers of the coal injection unit is to capture dust emissions and perform subsequent dry dedusting.","mg/Nm3","N/A",20,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0,"IS (2012)\n2012/135/EU",1.4,89,27]
[1277,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.",0,0,"Unspecified","Unspecified","Unspecified","Unspecified","Electric arc furnace steelmaking and casting: On-site slag processing ","Emissions to air ","Air","Dust","Particulates (PM10) (Annual Mean)","BAT for on-site slag processing is to reduce dust emissions by using one or a combination of the following techniques: (i) efficient extraction of the slag crusher and screening devices with subsequent off-gas cleaning, if relevant; (ii) transport of untreated slag by shovel loaders; (iii) extraction or wetting of conveyor transfer points for broken material; (iv) wetting of slag storage heaps; (v) use of water fogs when broken slag is loaded","mg/Nm3",10,20,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0,"IS (2012)\n2012/135/EU",1.7,97,35]
[1226,"Iron and steel","2. Production and processing of metals","1.3. Coke production","Coke Oven Plants",0,"Unspecified","Unspecified","Unspecified","Unspecified","Coal charging systems ","Emissions to air ","Air","Dust ","Particulates (PM10) (Annual Mean)","BAT is to charge coke oven chambers with emission-reduced charging systems. \n\nIf, however, the gases are extracted and treated outside the coke oven, charging with a land-based treatment of the\nextracted gases is the preferred method. Treatment should consist of an efficient extraction of the emissions with\nsubsequent combustion to reduce organic compounds and the use of a bag filter to reduce particulates.","g/t","N/A",5,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0,"IS (2012)\n2012/135/EU",1.4,85,23]
[1227,"Iron and steel","2. Production and processing of metals","1.3. Coke production","Coke Oven Plants",0,"Unspecified","Unspecified","Unspecified","Unspecified","Coal charging systems ","Emissions to air ","Air","Dust ","Particulates (PM10) (Annual Mean)","BAT is to charge coke oven chambers with emission-reduced charging systems. \n\nIf, however, the gases are extracted and treated outside the coke oven, charging with a land-based treatment of the\nextracted gases is the preferred method. Treatment should consist of an efficient extraction of the emissions with\nsubsequent combustion to reduce organic compounds and the use of a bag filter to reduce particulates.","mg/Nm3","N/A",50,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0,"IS (2012)\n2012/135/EU",1.4,85,23]
[1225,"Iron and steel","2. Production and processing of metals","1.3. Coke production","Coke Oven Plants",0,"Unspecified","Unspecified","Unspecified","Unspecified","Storage and handling of pulverised coal","Emissions to air ","Air","Dust ","Particulates (PM10) (Annual Mean)","BAT for storage and handling of pulverised coal is to prevent or reduce diffuse dust emissions by using one or a combination of the following techniques: (i) storing pulverised materials in bunkers and warehouses; (ii) using closed or enclosed conveyors; (iii)  minimising the drop heights depending on the plant size and construction; (iv) reducing emissions from charging of the coal tower and the charging car; (v) using efficient extraction and subsequent dedusting\n","mg/Nm3",10,20,"Amber",0,0,0,"Unspecified ","Average over the sampling period",0,"IS (2012)\n2012/135/EU",1.4,85,23]
[1224,"Iron and steel","2. Production and processing of metals","1.3. Coke production","Coke Oven Plants",0,"Unspecified","Unspecified","Unspecified","Unspecified","Coal grinding plants ","Emissions to air","Air","Dust","Particulates (PM10) (Annual Mean)","BAT for coal grinding plants (coal preparation including crushing, grinding, pulverising and screening) is to prevent or reduce dust emissions by using one or a combination of the following techniques: (i) building and/or device enclosure (crusher, pulveriser, sieves); (ii) efficient extraction and use of a subsequent dry dedusting systems.","mg/Nm3",10,20,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0,"IS (2012)\n2012/135/EU",1.4,85,23]
[867,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"IGCC","Unspecified ","Unspecified","≥ 100 MWth",0,"Emissions to air ","Air","Dust and particulate-bound metal emissions","Particulates (PM10) (Annual Mean)",0,"mg/Nm3","N/A","0.025","Green","Continuous",0,0,0.15,"Average over the sampling period",0,"LCP (2017)\n2017/1709","7.1.4",76,76]
[868,"LCP","1. Energy industries","\n1.1: Combustion of fuels in installations with a total rated thermal input of 50 MW or more, only when this activity takes place in combustion plants with a total rated thermal input of 50 MW or more.\n \n1.4: Gasification of coal or other fuels in installations with a total rated thermal input of 20 MW or more, only when this activity is directly associated to a combustion plant.\n \n5.2: Disposal or recovery of waste in waste co-incineration plants for non-hazardous waste with a capacity exceeding 3 tonnes per hour or for hazardous waste with a capacity exceeding 10 tonnes per day, only when this activity takes place in combustion plants covered under 1.1 above.\n \n",0,0,"IGCC","Unspecified ","Unspecified","≥ 100 MWth",0,"Emissions to air ","Air","Dust and particulate-bound metal emissions","Particulates (PM10) (Annual Mean)",0,"ug/Nm3","N/A","1","Green","Continuous",0,0,0.15,"Average over the sampling period",0,"LCP (2017)\n2017/1710","7.1.4",76,76]
[1374,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Alumina and Anode production","Primary aluminium production","Unspecified","Unspecified","Unspecified","Unspecified","Storage, handling and transport of raw materials","Emissions to air ","Air","Dust","Particulates (PM10) (Annual Mean)","In order to reduce dust emissions from the storage, handling and transport of raw materials, BAT is to use a bag filter.","mg/Nm3",5,10,"Green","Oncer per year ",0,0,0,"Average over sampling period",0,"NFM (2016) 2016/1032 \n","1.3.3.1.1",65,34]
[1382,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Alumina and Anode production","Secondary aluminium production ","Unspecified","Unspecified","Unspecified","Unspecified","Remelting","Emissions to air ","Air","Dust","Particulates (PM10) (Annual Mean)","In order to reduce dust and metal emissions to air from remelting in secondary aluminium production, BAT is to use one or a combination of the techniques given below: (i) Use of uncontaminated aluminium material i.e. solid material free of substances such as paint, plastic\nor oil (e.g. billets); (ii) Optimise combustion conditions to reduce the emissions of dust; (iii) Bag filter","mg/Nm3",2,5,"Green","Once per year",0,0,0,"Average over the sampling period","For furnaces designed to use and using only uncontaminated raw material, for which dust emissions are below 1 kg/h, the upper end of the range is 25 mg/Nm3 as an average of the samples obtained over a year.","NFM (2016) 2016/1032 \n","1.3.4.3.2",71,40]
[1380,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Alumina and Anode production","Secondary aluminium production ","Unspecified","Unspecified","Unspecified","Unspecified","Swarf drying and the removal of oil and organic compounds from the swarf, from the crushing, milling and dry separation of non-metallic constituents and metals other than aluminium, and from the storage, handling and transport","Emissions to air ","Air","Dust","Particulates (PM10) (Annual Mean)","In order to reduce dust and metal emissions from the swarf drying and the removal of oil and organic compounds from the swarf, from the crushing, milling and dry separation of non-metallic constituents and metals other than aluminium, and from the storage, handling and transport in secondary aluminium production, BAT is to use a bag filter.","mg/Nm3","N/A",5,"Green","Oncer per year ",0,0,0,"Average over the sampling period",0,"NFM (2016) 2016/1032 \n","1.3.4.3.2",70,39]
[1437,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Carbon and/or Graphite Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Baking","Emissions to air ","Air","Dust","Particulates (PM10) (Annual Mean)","In order to reduce dust and PAH emissions to air from baking, BAT is to use one or a combination of the techniques given below: (i) ESP, in combination with a thermal oxidation step (e.g.\nregenerative thermal oxidiser) when highly volatile\ncompounds are expected; (ii) Regenerative thermal oxidiser, in combination with a\npretreatment (e.g. ESP) in cases of a high dust content\nin the exhaust gas; (iii) Thermal oxidiser","mg/Nm3",2,10,"Green","Once per year",0,0,0,"Average over the sampling period","The lower end of the range is associated with the use of a combination of an ESP and a regenerative thermal oxidiser. The higher end of the range is associated with the use of a thermal oxidiser.","NFM (2016) 2016/1032 \n","1.9.1.2",101,70]
[1439,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Carbon and/or Graphite Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Impregnation","Emissions to air ","Air","Dust","Particulates (PM10) (Annual Mean)","In order to reduce dust and PAH emissions to air from impregnation, BAT is to use one or a combination of the techniques given below: (i) Dry scrubber followed by a bag filter; (ii) Coke filter; (iii) Thermal oxidiser","mg/Nm3",2,10,"Green","Once per year",0,0,0,"Average over the sampling period",0,"NFM (2016) 2016/1032 \n","1.9.1.2",102,71]
[1435,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Carbon and/or Graphite Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Production of green paste and green shapes","Emissions to air ","Air","Dust","Particulates (PM10) (Annual Mean)","In order to reduce dust and PAH emissions to air from the production of green paste and green shapes, BAT is to use one or a combination of the techniques given below: (i) Dry scrubber using coke as the adsorbent agent and with or without precooling, followed by a bag\nfilter; (ii) Coke filter; (iii) Regenerative thermal oxidiser; (iv) Thermal oxidiser","mg/Nm3",2,10,"Green","Once per year",0,0,0,"Average over the sampling period",0,"NFM (2016) 2016/1032 \n","1.9.1.2",101,70]
[1433,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Carbon and/or Graphite Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Storage, handling and transportation of coke and pitch, and mechanical processes (such as grinding) and graphitising and machining","Emissions to air ","Air","Dust","Particulates (PM10) (Annual Mean)","In order to reduce dust emissions to air from the storage, handling and transportation of coke and pitch, and mechanical processes (such as grinding) and graphitising and machining, BAT is to use a bag filter.","mg/Nm3",2,5,"Green","Once per year",0,0,0,"Average over the sampling period",0,"NFM (2016) 2016/1032 \n","1.9.1.2",100,69]
[1353,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Copper production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Copper-rich slag furnace processing","Emissions to air ","Air","Dust","Particulates (PM10) (Annual Mean)","In order to reduce dust and metal emissions to air from copper-rich slag furnace processing, BAT is to use a bag filter or a scrubber in combination with an ESP.","mg/Nm3",2,5,"Green","Once per year ",0,0,0,"Average over sampling period","Dust emissions are expected to be towards the lower end of the range when emissions of lead are above 1 mg/Nm3","NFM (2016) 2016/1032 \n","1.2.3.7",57,26]
[1348,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Copper production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Reception,           storage,           handling,           transport,           metering,           mixing,           \nblending,  crushing,  drying,  cutting  and  screening  of  raw  \nmaterials,  and  the  pyrolytic  treatment  of  copper  turnings  \nin  primary  and  secondary  copper  production","Emissions to air ","Air","Dust","Particulates (PM10) (Annual Mean)","In order to reduce dust and metal emissions to air from the reception, storage, handling, transport, metering, mixing, blending, crushing, drying, cutting and screening of raw materials, and the pyrolytic treatment of copper turnings in primary and secondary copper production, BAT is to use a bag filter.","mg/Nm3",2,5,"Green","Once per year ",0,0,0,"Average over sampling period",0,"NFM (2016) 2016/1032 \n","1.2.3.2",56,25]
[1352,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Copper production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Secondary copper holding furnace","Emissions to air ","Air","Dust","Particulates (PM10) (Annual Mean)","In order to reduce dust and metal emissions to air from the secondary copper holding furnace, BAT is to use a bag filter","mg/Nm3","N/A",5,"Green","Once per year ",0,0,0,"Average over sampling period","Dust emissions are expected to be towards the lower end of the range when emissions of heavy metals are above the following levels: 1 mg/Nm3 for lead, 1 mg/Nm3 for copper, 0,05 mg/Nm3 for arsenic, 0,05 mg/Nm3 for cadmium","NFM (2016) 2016/1032 \n","1.2.3.6",57,26]
[1424,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Ferro-alloys Production","All","Unspecified","Unspecified","Unspecified","Unspecified","— Storage, handling and transport of solid materials — Pretreatment operations such as metering, mixing, blending and degreasing — Tapping, casting and packaging","Emissions to air ","Air","Dust","Particulates (PM10) (Annual Mean)","In order to reduce dust and metal emissions to air from the storage, handling and transport of solid materials, and from pretreatment operations such as metering, mixing, blending and degreasing, and from tapping, casting and packaging, BAT is to use a bag filter.","mg/Nm3",2,5,"Green","Continuous",0,0,0,"As an average over the sampling period.",0,"NFM (2016) 2016/1032 \n","1.7.2.2",95,64]
[1393,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Lead and/or Tin Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Battery preparation (crushing, screning and classifying) ","Emissions to air ","Air","Dust","Particulates (PM10) (Annual Mean)","In order to reduce dust and metal emissions to air from battery preparation (crushing, screening and classifying), BAT is to use a bag filter or a wet scrubber.","mg/Nm3","N/A",5,"Green","Once per year",0,0,0,"Average over the sampling period ",0,"NFM (2016) 2016/1032 \n","1.4.1.2",76,45]
[1414,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Zinc and/or Cadmium Production","Cadmium Production","Unspecified","Unspecified","Unspecified","Unspecified","Pyrometallurgical cadmium production and the melting, alloying and casting of cadmium ingots","Emissions to air ","Air","Dust","Particulates (PM10) (Annual Mean)","In order to reduce dust and metal emissions to air from pyrometallurgical cadmium production and the melting, alloying and casting of cadmium ingots, BAT is to use one or a combination of the techniques given below: (i) Bag filter; (ii) ESP; (iii) Wet scrubber ","mg/Nm3",2,3,"Green","Once per year",0,0,0,"Average over the sampling period",0,"NFM (2016) 2016/1032 \n","1.5.4.1.2",87,56]
[1401,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Zinc and/or Cadmium Production","Hydrometallurgical zinc production","Unspecified","Unspecified","Unspecified","Unspecified","Handling and storage of raw materials, dry roaster feed preparation, dry roaster feeding and calcine processing","Emissions to air ","Air","Dust","Particulates (PM10) (Annual Mean)","In order to reduce dust and metal emissions to air from the handling and storage of raw materials, dry roaster feed preparation, dry roaster feeding and calcine processing, BAT is to use a bag filter.","mg/Nm3","N/A",5,"Green","Once per year",0,0,0,"Average over the sampling period",0,"NFM (2016) 2016/1032 \n","1.5.1.1.2.2",81,50]
[1413,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Zinc and/or Cadmium Production","Melting, alloying and casting of zinc ingots and zinc power production","Unspecified","Unspecified","Unspecified","Unspecified","Melting, alloying and casting of zinc ingots and zinc powder production","Emissions to air ","Air","Dust","Particulates (PM10) (Annual Mean)","In order to reduce dust and metal emissions to air from the melting, alloying and casting of zinc ingots and zinc powder production, BAT is to use a bag filter.","mg/Nm3","N/A",5,"Green","Once per year",0,0,0,"Average over the sampling period",0,"NFM (2016) 2016/1032 \n","1.5.3.1.2",86,55]
[1407,"Non-ferrous Metals Industries","2.  Processing of non-ferrous metals","2.1: Metal ore (including sulphide ore) roasting or sintering; \n2.5: (a) production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; (b) melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals;\n6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.\nprocesses","Zinc and/or Cadmium Production","Secondary ","Unspecified","Unspecified","Unspecified","Unspecified","Pelletising and slag processing","Emissions to air ","Air","Dust","Particulates (PM10) (Annual Mean)","In order to reduce dust and metal emissions to air from pelletising and slag processing, BAT is to use a bag filter.","mg/Nm3","N/A",5,"Green","Once per year",0,0,0,"Average over the sampling period ",0,"NFM (2016) 2016/1032 \n","1.5.2.1.1",84,53]
[561,"Pulp and paper","6. Other activities","6.1.   Production in industrial installations of (a) pulp from timber or other fibrous materials; (b) paper or card board with a production capacity exceeding 20 tonnes per day\n \n","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Recovery boiler","Emissions to air","Air","Dust","Particulates (PM10) (Annual Mean)","In order to reduce dust and SO2 emissions from a recovery boiler, BAT is to use one of the techniques given below and to limit ‘acid operation’ of the scrubbers to the minimum required to ensure their proper functioning: (i) ESP or multicyclones with multistage venturi scrubbers; (ii) ESP or multicyclones with multistage double inlet downstream scrubbers","mg/Nm3",5,20,"Green","Periodic ",0,0," ","Average over the sampling period","For recovery boilers operated in mills using more than 25 % of hardwood (potassium-rich) in raw materials, higher dust emissions up to 30 mg/Nm3 may occur.\n\nThe BAT-AEL for dust does not apply for ammonium-based mills.","PP (2014)\n2014/687/EU","1.2.2.4",32,32]
[911,"Refineries","1. Energy industries","1.2. Refining of mineral oil and gas",0,0,"All","Unspecified","All","Unspecified","Unit for calcining of green coke","Emission to air ","Air","Dust","Particulates (PM10) (Annual Mean)","In order to reduce dust emissions to air from the calcining of green coke process, BAT is to use a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Multistage cyclone\nseparators ","mg/Nm3",10,50,"Amber","Continuous",0,0,0,"Monthly ","The lower end of the range can be achieved with a 4-field ESP\n\nWhen an ESP is not applicable, values of up to 150 mg/Nm3 may occur. ","REF(2014)\n2014/738/EU",1.7,62,24]
[909,"Refineries","1. Energy industries","1.2. Refining of mineral oil and gas",0,0,"All","Existing","All","Unspecified","Regenerator in the catalytic cracking process","Emission to air ","Air","Dust","Particulates (PM10) (Annual Mean)","In order to reduce dust and metals emissions to air from the catalytic cracking process (regenerator), BAT is to use one or a combination of the techniques given below:\n\nPrimary techniques:\n(i) Use of an attrition-resistant catalyst; (ii) Use of low sulphur feedstock (e.g. by feedstock selection or by hydrotreatment of feed) \n\nSecondary techniqyes:\n(i) Electrostatic precipitator (ESP); (ii) Multistage cyclone separators; (iii) Third stage blowback\nfilter; (iv) Wet scrubbing ","mg/Nm3",10,50,"Green","Continuous",0,0,0.03,"Monthly ","Soot blowing in CO boiler and through the gas cooler is excluded.\n\nThe lower end of the range can be achieved with a 4-field ESP.","REF(2014)\n2014/738/EU",1.5,57,20]
[908,"Refineries","1. Energy industries","1.2. Refining of mineral oil and gas",0,0,"All","New","All","Unspecified","Regenerator in the catalytic cracking process","Emission to air ","Air","Dust","Particulates (PM10) (Annual Mean)","In order to reduce dust and metals emissions to air from the catalytic cracking process (regenerator), BAT is to use one or a combination of the techniques given below:\n\nPrimary techniques:\n(i) Use of an attrition-resistant catalyst; (ii) Use of low sulphur feedstock (e.g. by feedstock selection or by hydrotreatment of feed) \n\nSecondary techniqyes:\n(i) Electrostatic precipitator (ESP); (ii) Multistage cyclone separators; (iii) Third stage blowback\nfilter; (iv) Wet scrubbing ","mg/Nm3",10,25,"Green","Continuous",0,0,0.03,"Monthly ","Soot blowing in CO boiler and through the gas cooler is excluded.","REF(2014)\n2014/738/EU",1.5,57,20]
[914,"Refineries","1. Energy industries","1.2. Refining of mineral oil and gas",0,0,"All","Existing","All","Unspecified","Multi-fuel fired combustion unit  with the exception\nof gas turbines","Emission to air ","Air","Dust ","Particulates (PM10) (Annual Mean)","In order to prevent or reduce dust and metal emissions to air from the combustion units, BAT is to use one or a combination of the techniques given below: \n\nPrimary techniques:\n(i) Selection or treatment of fuel; (ii) Combustion modifications\n\nSecondary techniques:\n(i) Electrostatic precipitator (ESP); (ii) Third stage blowback filter; (iii) Wet scrubbing; (iv) Centrifugal washers ","mg/Nm3",5,50,"Amber",0,0,0,0.03,"Monthly ","The lower end of the range is achievable for units with the use of end-of-pipe techniques. \n\nThe upper end of the range refers to the use of a high percentage of oil burning and where only primary techniques are\napplicable.","REF(2014)\n2014/738/EU",1.9,66,29]
[915,"Refineries","1. Energy industries","1.2. Refining of mineral oil and gas",0,0,"All","New","All","<50 MW","Multi-fuel fired combustion unit  with the exception\nof gas turbines","Emission to air ","Air","Dust ","Particulates (PM10) (Annual Mean)","In order to prevent or reduce dust and metal emissions to air from the combustion units, BAT is to use one or a combination of the techniques given below: \n\nPrimary techniques:\n(i) Selection or treatment of fuel; (ii) Combustion modifications\n\nSecondary techniques:\n(i) Electrostatic precipitator (ESP); (ii) Third stage blowback filter; (iii) Wet scrubbing; (iv) Centrifugal washers ","mg/Nm3",5,25,"Green","Once a year and after significant fuel changes",0,0,0.03,"Monthly ",0,"REF(2014)\n2014/738/EU",1.9,66,29]
[1001,"Wood-based Panels Production","6.   Other activities","6.1. (c) one or more of the following wood-based panels: oriented strand board, particleboard or fibreboard with a production capacity exceeding 600 m3 per day\n ",0,"Fibre","Unspecified","Unspecified","Unspecified","Unspecified","Dryer- all types ","Emissions to air","Air","Dust ","Particulates (PM10) (Annual Mean)","In order to prevent or reduce emissions to air from the dryer, BAT is to achieve and manage a balanced operation of the\ndrying process and to use one or a combination of the techniques given below: (i) Dust abatement of inlet hot gas to a\ndirectly heated dryer in combination with one or a combination of the other techniques listed below; (ii) Bag filter; (iii) Cyclone; (iv) UTWS dryer and combustion with heat exchanger and thermal treatment of discharged dryer waste gasl (v) Wet electrostatic precipitator; (vi) Wet scrubber; (vii) Bioscrubber; (viii) Chemical degradation or capture of formaldehyde with chemicals in combination with a wet scrubbing system \n\n","mg/Nm3",3,20,"Green","Periodic (at least once every 6 months)",0,0,"N/A","Average over sampling period ",0,"WBP (2015) 2015/2119 \n",1.2,44,14]
[1000,"Wood-based Panels Production","6.   Other activities","6.1. (c) one or more of the following wood-based panels: oriented strand board, particleboard or fibreboard with a production capacity exceeding 600 m3 per day\n ",0,"PB or OSB","Unspecified","Unspecified","Unspecified","Unspecified","Dryer- Directly heated","Emissions to air","Air","Dust ","Particulates (PM10) (Annual Mean)","In order to prevent or reduce emissions to air from the dryer, BAT is to achieve and manage a balanced operation of the\ndrying process and to use one or a combination of the techniques given below: (i) Dust abatement of inlet hot gas to a\ndirectly heated dryer in combination with one or a combination of the other techniques listed below; (ii) Bag filter; (iii) Cyclone; (iv) UTWS dryer and combustion with heat exchanger and thermal treatment of discharged dryer waste gasl (v) Wet electrostatic precipitator; (vi) Wet scrubber; (vii) Bioscrubber; (viii) Chemical degradation or capture of formaldehyde with chemicals in combination with a wet scrubbing system \n\n","mg/Nm3",3,30,"Green","Periodic (at least once every 6 months)",0,0,0.15,"Average over sampling period ",0,"WBP (2015) 2015/2119 \n",1.2,44,14]
[1001,"Wood-based Panels Production","6.   Other activities","6.1. (c) one or more of the following wood-based panels: oriented strand board, particleboard or fibreboard with a production capacity exceeding 600 m3 per day\n ",0,"PB or OSB","Unspecified","Unspecified","Unspecified","Unspecified","Dryer-Indirectly heated ","Emissions to air","Air","Dust ","Particulates (PM10) (Annual Mean)","In order to prevent or reduce emissions to air from the dryer, BAT is to achieve and manage a balanced operation of the\ndrying process and to use one or a combination of the techniques given below: (i) Dust abatement of inlet hot gas to a\ndirectly heated dryer in combination with one or a combination of the other techniques listed below; (ii) Bag filter; (iii) Cyclone; (iv) UTWS dryer and combustion with heat exchanger and thermal treatment of discharged dryer waste gasl (v) Wet electrostatic precipitator; (vi) Wet scrubber; (vii) Bioscrubber; (viii) Chemical degradation or capture of formaldehyde with chemicals in combination with a wet scrubbing system \n\n","mg/Nm3",3,10,"Green","Periodic (at least once every 6 months)",0,0,0.15,"Average over sampling period ",0,"WBP (2015) 2015/2119 \n",1.2,44,14]
[1005,"Wood-based Panels Production","6.   Other activities","6.1. (c) one or more of the following wood-based panels: oriented strand board, particleboard or fibreboard with a production capacity exceeding 600 m3 per day\n ",0,"Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Press","Emissions to air","Air","Dust ","Particulates (PM10) (Annual Mean)","In order to prevent or reduce emissions to air from the press, BAT is to use in-duct quenching of collected press waste gas and an appropriate combination of the techniques given below.: (i) Select resins with a low formaldehyde content; (ii) Controlled operation of the press with balanced press temperature, applied pressure and press speed; (iii) Wet scrubbing of collected press\nwaste gases using Venturi scrubbers or hydrocyclones, etc.; (iv) Wet electrostatic precipitator; (v) Bioscrubber; (vi) Post-combustion as the last treatment step after application of a wet scrubber ","mg/Nm3",3,15,"Green","Periodic (at least once every 6 months)",0,0,"N/A","Average over sampling period ",0,"WBP (2015) 2015/2119 \n",1.2,46,16]
[1007,"Wood-based Panels Production","6.   Other activities","6.1. (c) one or more of the following wood-based panels: oriented strand board, particleboard or fibreboard with a production capacity exceeding 600 m3 per day\n ",0,"Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Upstream and downstream wood processing, conveying of wood materials and mat forming ","Emissions to air","Air","Dust ","Particulates (PM10) (Annual Mean)","In order to reduce dust emissions to air from upstream and downstream wood processing, conveying of wood materials and mat forming, BAT is to use either a bag filter or a cyclofilter.","mg/Nm3",3,5,"Green","Periodic (at least once a year)",0,0,"N/A","Average over sampling period ","When a bag filter or a cyclofilter is not applicable, the upper end of the range can be up to 10 mg/Nm3","WBP (2015) 2015/2119 \n",1.2,46,16]
[1282,"Iron and steel","2. Production and processing of metals","2.1. Metal ore (including sulphide ore) roasting or sintering installations.",0,0,"Unspecified","Unspecified","Unspecified","Unspecified","Electric arc furnace steelmaking and casting: Waste water from continous casting machines ","Emissions to air ","Air","Total chromium","Chromium, chromium (II) compounds and chromium (III) compounds as Cr","BAT is to minimise the waste water discharge from continuous casting by using the following techniques in combination: (i) the removal of solids by flocculation, sedimentation and/or filtration; (ii) the removal of oil in skimming tanks or any other effective device; (iii) the recirculation of cooling water and water from vacuum generation as much as possible","mg/Nm3","N/A",0.5,"Green","Discontinuous ",0,0,"Unspecified ","Qualified random sample or a 24 hour composite",0,"IS (2012)\n2012/135/EU",1.7,97,35]

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["Sector","IED Annex I Activity Category","Product / sub-sector","Sub-Product / sub-sub-sector","Plant type","Plant age","Fuel type","Plant capacity","Emission Source","Release type","Pollutant","BAT","BAT-AEL units","BAT-AEL lower value","BAT-AEL upper value","Colour","Monitoring","Reference temperature (K)","Reference Pressure (kPa)","Reference O2 content (% waste gas volume)","Averaging period","Notes",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Sector","IED Annex I Activity Category","Product / sub-sector","Sub-Product / sub-sub-sector","Plant type","Plant age","Fuel type","Plant capacity","Emission Source","Release type","Pollutant","BAT","BAT-AEL units","BAT-AEL lower value","BAT-AEL upper value","Colour","Monitoring","Reference temperature (K)","Reference Pressure (kPa)","Reference O2 content (% waste gas volume)","Averaging period","Notes"]
["Cement lime and MgO","3. Mineral Industry ","Lime","Unspecified","PFRK, OSK, LRK, PRK","Unspecified","Unspecified","Unspecified","Kiln firing process","Air","Carbon monoxide, expressed as CO ","In order to reduce the emissions of CO from the flue-gases of kiln firing processes, BAT is to use one or a combination of the following techniques: (i) Selecting, raw materials with a low content of organic matter; (ii) Using process optimisation techniques to achieve a stable and complete combustion","mg/Nm3","N/A","500","Green","Continuous",0,0,0.11,"daily average value or average over the sampling period (spot measurements for at least half an hour)","Emissions can be higher depending on raw materials used and/or type of lime produced, e.g. hydraulic lime.\n\nBAT-AEL does not apply to MFSK and ASK",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Cement lime and MgO","3. Mineral Industry ","Cement","Unspecified","Lepol and long rotary kilns","Unspecified","Unspecified","Unspecified","Kiln firing proceeses","Air","Nitrogen dioxide","In order to reduce the emissions of NO x from the flue-gases of kiln firing and/or preheating/precalcining processes, BAT is to use one or a combination of the following techniques: (i) Primary techniques; (ii) Staged combustion (conventional or waste fuels), also in combination with a precalciner and the use of optimised fuel mix; (iii) Selective non-catalytic reduction (SNCR); (iv) Selective catalytic reduction (SCR)","mg/Nm3",400,"800","Green","Continuous",0,0,0.1,"Daily ","Depending on initial levels and NH 3 slip."]
["Cement lime and MgO","3. Mineral Industry ","Magnesium oxide","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Kiln firing process","Air","Carbon monoxide, expressed as CO ","In order to reduce the emissions of CO from the flue-gases of kiln firing processes, BAT is to use a combination of the following techniques: (i) Selecting raw materials with a low content of organic matter; (ii) Process control optimisation; (iii) Feeding fuels controlled, constantly and continuously","mg/Nm3",50,"1000","Green","Continuous",0,0,0.1,"Daily",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Cement lime and MgO","3. Mineral Industry ","Cement","Unspecified","Preheater kilns","Unspecified","Unspecified","Unspecified","Kiln firing processes","Air","Nitrogen dioxide","In order to reduce the emissions of NO x from the flue-gases of kiln firing and/or preheating/precalcining processes, BAT is to use one or a combination of the following techniques: (i) Primary techniques; (ii) Staged combustion (conventional or waste fuels), also in combination with a precalciner and the use of optimised fuel mix; (iii) Selective non-catalytic reduction (SNCR); (iv) Selective catalytic reduction (SCR)","mg/Nm3",200,"450","Green","Continuous",0,0,0.1,"Daily ","The upper level of the BAT-AEL range is 500 mg/Nm 3 , if the initial NO x level after primary techniques is > 1 000 mg/Nm 3.\n\nExisting kiln system design, fuel mix properties including waste and raw material burnability (e.g. special cement or white cement clinker) can influence the ability to be within the range. Levels below 350 mg/Nm 3 are achieved at kilns with favourable conditions when using SNCR. In 2008, the lower value of 200 mg/Nm 3 has been reported as a monthly average for three plants (easy burning mix used) using SNCR."]
["Cement lime and MgO","3. Mineral Industry ","Cement","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Chanelled dust emissions from dusty oeprations","Air","Particulates (PM10) (24 hr Mean)","In order to reduce channelled dust emissions, BAT is to apply a maintenance management system which especially addresses the performance of filters applied to dusty operations, other than those from kiln firing, cooling and main milling processes. Taking this management system into account, BAT is to use dry flue-gas cleaning with a filter.","mg/Nm3","N/A",10,"Green","Continuous",0,0,"N/A","Daily","It should be noted that for small sources (< 10 000 Nm 3 /h) a priority approach, based on the maintenance management system, regarding the frequency for checking the performance of the filter has to be taken into account",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Cement lime and MgO","3. Mineral Industry ","Lime","Unspecified","LRK, PRK","Unspecified","Unspecified","Unspecified","Kiln firing process","Air","Nitrogen dioxide","In order to reduce the emissions of NO X from the flue-gases of kiln firing processes, BAT is to use one or a combination of the following techniques:(i) Primary techniques; (ii) SNCR","mg/Nm3",200,"500","Green","Continuous",0,0,0.11,"daily average value or average over the sampling period (spot measurements for at least half an hour), stated as NO 2","The higher ends of the ranges are related to the production of dolime and hard burned lime. Higher levels than the upper end of the range may be associated with the production of sintered dolime.\n\nWhere primary techniques as indicated in BAT 45 (a)I are not sufficient to reach this level and where secondary techniques are not applicable to reduce the NO x emissions to 350 mg/Nm 3 , the upper level is 500 mg/Nm 3 , especially for hard burned lime and for the use of biomass as fuel."]
["Cement lime and MgO","3. Mineral Industry ","Cement","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Cooling and milling processes","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust emissions from the flue-gases of cooling and milling processes, BAT is to use dry flue-gas cleaning with a filter","mg/Nm3",10,"20","Green","Continuous",0,0,"N/A","Daily ","When applying fabric filters or new or upgraded ESPs, the lower level is achieved.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Cement lime and MgO","3. Mineral Industry ","Lime","Unspecified","PFRK, ASK, MFSK, OSK","Unspecified","Unspecified","Unspecified","Kiln firing process","Air","Nitrogen dioxide","In order to reduce the emissions of NO X from the flue-gases of kiln firing processes, BAT is to use one or a combination of the following techniques:(i) Primary techniques; (ii) SNCR","mg/Nm3",100,"350","Green","Continuous",0,0,0.11,"daily average value or average over the sampling period (spot measurements for at least half an hour), stated as NO 2","The higher ends of the ranges are related to the production of dolime and hard burned lime. Higher levels than the upper end of the range may be associated with the production of sintered dolime.\n\nWhere primary techniques as indicated in BAT 45 (a)I are not sufficient to reach this level and where secondary techniques are not applicable to reduce the NO x emissions to 350 mg/Nm 3 , the upper level is 500 mg/Nm 3 , especially for hard burned lime and for the use of biomass as fuel."]
["Cement lime and MgO","3. Mineral Industry ","Cement","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Kiln firing process","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust emissions from flue-gases of kiln firing processes, BAT is to use dry flue-gas cleaning with a filter.","mg/Nm3",10,"20","Green","Continuous",0,0,0.1,"Daily ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Cement lime and MgO","3. Mineral Industry ","Magnesium oxide","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Kiln firing process","Air","Nitrogen dioxide","In order to reduce the emissions of NO x from the flue-gases of kiln firing processes, BAT is to use a combination of the following techniques: (i) Appropriate fuel selection along with a limited nitrogen content in the fuel; (ii) Process optimisation and improved firing technique","mg/Nm3",500,"1500","Green","Continuous",0,0,0.1,"Daily","The higher values are related to the high temperature DBM process."]
["Cement lime and MgO","3. Mineral Industry ","Lime","Unspecified","ESP or other filters","Unspecified","Unspecified","Unspecified","Kiln firing process","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust emissions from the flue-gases of kiln firing processes, BAT is to use flue-gas cleaning with a filter. One or a combination of the following techniques can be used: (i) ESP; (ii) Fabric filter; (iii) Wet dust separator; (iv) Centrifugal separator/cyclone","mg/Nm3","N/A","20","Green","Continuous",0,0,0.11,"daily average value or average over the sampling period (spot measurements for at least half an hour)","In exceptional cases where the resistivity of dust is high, the BAT-AEL could be higher, up to 30 mg/Nm 3 , as the daily average value.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Container glass","Nitrates in batch formulation","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Primary techniques ","mg/Nm3","N/A",1000,"Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","If nitrates are used in the batch formulation for short campaigns or for melting furnaces with a capacity of < 100 t/day"]
["Cement lime and MgO","3. Mineral Industry ","Lime","Unspecified","Fabric filter","Unspecified","Unspecified","Unspecified","Chanelled dust emissions from dusty oeprations","Air","Particulates (PM10) (24 hr Mean)","In order to reduce channelled dust emissions from dusty operations other than those from kiln firing processes, BAT is to use one of the following techniques and to use a maintenance management system which specifically addresses the performance of filters: (i) Fabric filter; (ii) Wet scrubbers","mg/Nm3","N/A","10","Green","Continuous",0,0,"N/A","daily average or average over the sampling period (spot measurements for at least half an hour)","daily average or average over the sampling period (spot measurements for at least half an hour)",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Container glass","Nitrates in batch formulation","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Primary techniques ","kg/tonne melted glass","N/A",3,"Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","If nitrates are used in the batch formulation for short campaigns or for melting furnaces with a capacity of < 100 t/day"]
["Cement lime and MgO","3. Mineral Industry ","Lime","Unspecified","Fabric filter","Unspecified","Unspecified","Unspecified","Kiln firing process","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust emissions from the flue-gases of kiln firing processes, BAT is to use flue-gas cleaning with a filter. One or a combination of the following techniques can be used: (i) ESP; (ii) Fabric filter; (iii) Wet dust separator; (iv) Centrifugal separator/cyclone","mg/Nm3","N/A","10","Green","Continuous",0,0,0.11,"daily average value or average over the sampling period (spot measurements for at least half an hour)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Container glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Combustion modifications, special furnace designs","mg/Nm3","500","800","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The lower value refers to the use of special furnace designs, where applicable\n\nThese values should be reconsidered in the occasion of a normal or complete rebuild of the melting furnace"]
["Cement lime and MgO","3. Mineral Industry ","Lime","Unspecified","Wet scrubber","Unspecified","Unspecified","Unspecified","Chanelled dust emissions from dusty oeprations","Air","Particulates (PM10) (24 hr Mean)","In order to reduce channelled dust emissions from dusty operations other than those from kiln firing processes, BAT is to use one of the following techniques and to use a maintenance management system which specifically addresses the performance of filters: (i) Fabric filter; (ii) Wet scrubbers","mg/Nm3","N/A","10","Green","Continuous",0,0,"N/A","daily average or average over the sampling period (spot measurements for at least half an hour)","daily average or average over the sampling period (spot measurements for at least half an hour)",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Container glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Combustion modifications, special furnace designs","kg/tonne melted glass",0.75,1.2,"Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The conversion factor reported in Table 2 for general cases (1,5 × 10 –3 ) has been applied, with the exception of electric melting (specific cases: 3 × 10 –3 )\n\nThe lower value refers to the use of special furnace designs, where applicable\n\nThese values should be reconsidered in the occasion of a normal or complete rebuild of the melting furnace"]
["Cement lime and MgO","3. Mineral Industry ","Magnesium oxide","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Chanelled dust emissions from dusty oeprations","Air","Particulates (PM10) (24 hr Mean)","In order to reduce channelled dust emissions from dusty operations other than those from kiln firing processes, BAT is to use flue-gas cleaning with a filter by applying one or a combination of the following techniques, and to use a maintenance management system which specifically addresses the performance of techniques: (i) Fabric filters; (ii) Centrifugal separators/ cyclones; (iii) Wet dust separators","mg/Nm3","N/A","10","Green","Continuous",0,0,"N/A","Daily","It should be noted that for small sources (< 10 000 Nm 3 /h) a priority approach, based on a maintenance management system regarding the frequency for checking the performance of the filter has to be taken into account",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Container glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Electric melting","mg/Nm3","N/A",100,"Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)",0]
["Cement lime and MgO","3. Mineral Industry ","Magnesium oxide","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Kiln firing process","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust emissions from the flue-gases of kiln firing processes, BAT is to use flue-gas cleaning with a filter by applying one or a combination of the following techniques: (i) Electrostatic precipitators (ESPs); (ii) Fabric filters; (iii) Centrifugal separators/ cyclones; (iv) Wet dust separators","mg/Nm3",20,"35","Green","Continuous",0,0,0.1,"Daily",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Container glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Electric melting","kg/tonne melted glass","N/A",0.3,"Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The conversion factor reported in Table 2 for general cases (1,5 × 10 –3 ) has been applied, with the exception of electric melting (specific cases: 3 × 10 –3 )"]
["Cement lime and MgO","3. Mineral Industry ","Cement","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Kiln firing process","Air","Mercury and compounds, except mercury alkyls, (as","In order to minimise the emissions of metals from the flue-gases of the kiln firing processes, BAT is to use one or a combination of the following techniques: (i) Selecting materials with a low content of relevant metals and limiting the content of relevant metals in materials, especially mercury; (ii) Using a quality assurance system to guarantee the characteristics of the waste materials used; (iii) Using effective dust removal techniques as set out in BAT 17","mg/Nm3","N/A","0.05","Green","Periodic",0,0,0.1,"average over the sampling period (spot measurements, for at least half an hour)","Low levels have been reported based on the quality of the raw materials and the fuels. Values higher than 0,03 mg/Nm 3 have to be further investigated. Values close to 0,05 mg/Nm 3 require consideration of additional techniques (e.g. lowering of the flue-gas temperature, activated carbon).",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Container glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Oxy-fuel melting","mg/Nm3","N/A","N/A","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The achievable levels depend on the quality of the natural gas and oxygen available (nitrogen content)."]
["Cement lime and MgO","3. Mineral Industry ","Lime","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Kiln firing process","Air","Mercury and compounds, except mercury alkyls, (as","In order to minimise the emissions of metals from the flue-gases of kiln firing processes, BAT is to use one or a combination of the following techniques: (i) Selecting fuels with a low content of metals; (ii) Using a quality assurance system to guarantee the characteristics of the waste fuels used; (iii) Limiting the content of relevant metals in materials, especially mercury; (iv) Using one or a combination of dust removal techniques as set out in BAT 43","mg/Nm3","N/A","0.05","Green","Periodic",0,0,0.11,"average over the sampling period (spot measurements for at least half an hour)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Container glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Oxy-fuel melting","kg/tonne melted glass","0.5","0.8","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The achievable levels depend on the quality of the natural gas and oxygen available (nitrogen content)\n\nThe conversion factor reported in Table 2 for general cases (1,5 × 10 –3 ) has been applied, with the exception of electric melting (specific cases: 3 × 10 –3 )"]
["Cement lime and MgO","3. Mineral Industry ","Cement","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Kiln firing process","Air","Hydrogen chloride, expressed as HCl","In order prevent/reduce the emissions of HCl from flue-gases of the kiln firing processes, BAT is to use one or a combination of the following primary techniques: (i) Using raw materials and fuels with a low chlorine content; (ii) Limiting the amount of chlorine content for any waste that is to be used as raw material and/or fuel in a cement kiln","mg/Nm3","N/A","10","Green","Continuous",0,0,0.1,"Daily",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Container glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Secondary techniques","mg/Nm3","N/A",500,"Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)",0]
["Cement lime and MgO","3. Mineral Industry ","Lime","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Kiln firing process","Air","Hydrogen chloride, expressed as HCl","In order to reduce the emissions of HCl and the emissions of HF from the flue-gas of kiln firing processes, when using waste, BAT is to use the following primary techniques: (i) Using conventional fuels with a low chlorine and fluorine content; (ii) Limiting the amount of chlorine and fluorine content for any waste that is to be used as fuel in a lime kiln","mg/Nm3","N/A","10","Green","Continuous",0,0,0.11,0,0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Container glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Secondary techniques","kg/tonne melted glass","N/A",0.75,"Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The achievable levels depend on the quality of the natural gas and oxygen available (nitrogen content)"]
["Cement lime and MgO","3. Mineral Industry ","Lime","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Kiln firing process","Air","Hydrogen flouride, expressed as HF","In order to reduce the emissions of HCl and the emissions of HF from the flue-gas of kiln firing processes, when using waste, BAT is to use the following primary techniques: (i) Using conventional fuels with a low chlorine and fluorine content; (ii) Limiting the amount of chlorine and fluorine content for any waste that is to be used as fuel in a lime kiln","mg/Nm3","N/A","1","Green","Continuous",0,0,0.11,"daily average value or the average value over the sampling period (spot measurements, for at least half an hour",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Domestic glass","Nitrates in batch formulation","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","When nitrates are used in the batch formulation, BAT is to reduce NO X emissions by minimising the use of these raw materials, in combination with primary or secondary techniques.","mg/Nm3","500","1500","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","BAT-AELs for NO X emissions from the melting furnace in the domestic glass sector, when nitrates are used in the batch formulation for a limited number of short campaigns or for melting furnaces with a capacity < 100 t/day producing special types of soda-lime glasses (clear/ultra-clear glass or coloured glass using selenium) and other special glasses (i.e. borosilicate, glass ceramics, opal glass, crystal and lead crystal\n\nThis BAT-AEL is for the fuel/ar conventional furnaces"]
["Cement lime and MgO","3. Mineral Industry ","Cement","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Kiln firing process","Air","Metals (Cd, Tl) ","In order to minimise the emissions of metals from the flue-gases of the kiln firing processes, BAT is to use one or a combination of the following techniques: (i) Selecting materials with a low content of relevant metals and limiting the content of relevant metals in materials, especially mercury; (ii) Using a quality assurance system to guarantee the characteristics of the waste materials used; (iii) Using effective dust removal techniques as set out in BAT 17","mg/Nm3","N/A","0.05","Green","Periodic",0,0,0.1,"average over the sampling period (spot measurements, for at least half an hour)","Low levels have been reported based on the quality of the raw materials and the fuels.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Domestic glass","Nitrates in batch formulation","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","When nitrates are used in the batch formulation, BAT is to reduce NO X emissions by minimising the use of these raw materials, in combination with primary or secondary techniques.","kg/tonne melted glass","1.25","3.75","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","BAT-AELs for NO X emissions from the melting furnace in the domestic glass sector, when nitrates are used in the batch formulation for a limited number of short campaigns or for melting furnaces with a capacity < 100 t/day producing special types of soda-lime glasses (clear/ultra-clear glass or coloured glass using selenium) and other special glasses (i.e. borosilicate, glass ceramics, opal glass, crystal and lead crystal\n\nThis BAT-AEL is for the fuel/ar conventional furnaces\n\nThe conversion factor reported in Table 2 for soda-lime glass (2,5 × 10 –3 ) has been applied."]
["Cement lime and MgO","3. Mineral Industry ","Lime","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Kiln firing process","Air","Metals (Cd, Tl) ","In order to minimise the emissions of metals from the flue-gases of kiln firing processes, BAT is to use one or a combination of the following techniques: (i) Selecting fuels with a low content of metals; (ii) Using a quality assurance system to guarantee the characteristics of the waste fuels used; (iii) Limiting the content of relevant metals in materials, especially mercury; (iv) Using one or a combination of dust removal techniques as set out in BAT 43","mg/Nm3","N/A","0.05","Green","Periodic",0,0,0.11,"average over the sampling period (spot measurements for at least half an hour)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Domestic glass","Nitrates in batch formulation","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","When nitrates are used in the batch formulation, BAT is to reduce NO X emissions by minimising the use of these raw materials, in combination with primary or secondary techniques.","mg/Nm3","300","500","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","BAT-AELs for NO X emissions from the melting furnace in the domestic glass sector, when nitrates are used in the batch formulation for a limited number of short campaigns or for melting furnaces with a capacity < 100 t/day producing special types of soda-lime glasses (clear/ultra-clear glass or coloured glass using selenium) and other special glasses (i.e. borosilicate, glass ceramics, opal glass, crystal and lead crystal\n\nThis BAT-AEL is for the electric melting furnace"]
["Cement lime and MgO","3. Mineral Industry ","Cement","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Kiln firing process","Air","Metals( As, Sb, Pb, Cr, Co, Cu, Mn, Ni, V)","In order to minimise the emissions of metals from the flue-gases of the kiln firing processes, BAT is to use one or a combination of the following techniques: (i) Selecting materials with a low content of relevant metals and limiting the content of relevant metals in materials, especially mercury; (ii) Using a quality assurance system to guarantee the characteristics of the waste materials used; (iii) Using effective dust removal techniques as set out in BAT 17","mg/Nm3","N/A","0.5","Green","Periodic",0,0,0.1,"average over the sampling period (spot measurements, for at least half an hour)","Low levels have been reported based on the quality of the raw materials and the fuels.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Domestic glass","Nitrates in batch formulation","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","When nitrates are used in the batch formulation, BAT is to reduce NO X emissions by minimising the use of these raw materials, in combination with primary or secondary techniques.","kg/tonne melted glass","8","10","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","BAT-AELs for NO X emissions from the melting furnace in the domestic glass sector, when nitrates are used in the batch formulation for a limited number of short campaigns or for melting furnaces with a capacity < 100 t/day producing special types of soda-lime glasses (clear/ultra-clear glass or coloured glass using selenium) and other special glasses (i.e. borosilicate, glass ceramics, opal glass, crystal and lead crystal\n\nThis BAT-AEL is for the electric melting furnace"]
["Cement lime and MgO","3. Mineral Industry ","Lime","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Kiln firing process","Air","Metals( As, Sb, Pb, Cr, Co, Cu, Mn, Ni, V)","In order to minimise the emissions of metals from the flue-gases of kiln firing processes, BAT is to use one or a combination of the following techniques: (i) Selecting fuels with a low content of metals; (ii) Using a quality assurance system to guarantee the characteristics of the waste fuels used; (iii) Limiting the content of relevant metals in materials, especially mercury; (iv) Using one or a combination of dust removal techniques as set out in BAT 43","mg/Nm3","N/A","0.5","Green","Periodic",0,0,0.11,"average over the sampling period (spot measurements for at least half an hour)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Domestic glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Combustion modifications, special furnace designs","mg/Nm3","500","1000","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)",0]
["Cement lime and MgO","3. Mineral Industry ","Cement","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Air","NH3 slip ","When SNCR is used, BAT is to achieve efficient NO x reduction, while keeping the ammonia slip as low as possible, by using the following technique: (i) To apply an appropriate and sufficient NO x reduction efficiency along with a stable operating process; (ii) To apply a good stoichiometric distribution of ammonia in order to achieve the highest efficiency of NO x reduction and to reduce the NH 3 slip; (iii) To keep the emissions of NH 3 slip (due to unreacted ammonia) from the flue-gases as low as possible taking into account the correlation between the NO x abatement efficiency and the NH 3 slip","mg/Nm3",30,"50","Green","Continuous",0,0,"Unspecified","Daily ","The ammonia slip depends on the initial NO x level and on the NO x abatement efficiency. For Lepol and long rotary kilns, the level may be even higher.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Domestic glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Combustion modifications, special furnace designs","kg/tonne melted glass","1.25","2.5","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","A conversion factor of 2,5 × 10 –3 has been applied for combustion modifications and special furnace designs and a conversion factor of 3 × 10 –3 has been applied for electric melting (see Table 2). However, a case-by-case conversion factor may have to be applied for specific productions."]
["Cement lime and MgO","3. Mineral Industry ","Cement","Unspecified","Lepol and long rotary kilns","Unspecified","Unspecified","Unspecified","Kiln firing proceeses","Air","Nitrogen dioxide","In order to reduce the emissions of NO x from the flue-gases of kiln firing and/or preheating/precalcining processes, BAT is to use one or a combination of the following techniques: (i) Primary techniques; (ii) Staged combustion (conventional or waste fuels), also in combination with a precalciner and the use of optimised fuel mix; (iii) Selective non-catalytic reduction (SNCR); (iv) Selective catalytic reduction (SCR)","mg/Nm3",400,"800","Green","Continuous",0,0,0.1,"Daily ","Depending on initial levels and NH 3 slip.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Domestic glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Electric melting","mg/Nm3","N/A","100","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)",0]
["Cement lime and MgO","3. Mineral Industry ","Cement","Unspecified","Preheater kilns","Unspecified","Unspecified","Unspecified","Kiln firing processes","Air","Nitrogen dioxide","In order to reduce the emissions of NO x from the flue-gases of kiln firing and/or preheating/precalcining processes, BAT is to use one or a combination of the following techniques: (i) Primary techniques; (ii) Staged combustion (conventional or waste fuels), also in combination with a precalciner and the use of optimised fuel mix; (iii) Selective non-catalytic reduction (SNCR); (iv) Selective catalytic reduction (SCR)","mg/Nm3",200,"450","Green","Continuous",0,0,0.1,"Daily ","The upper level of the BAT-AEL range is 500 mg/Nm 3 , if the initial NO x level after primary techniques is > 1 000 mg/Nm 3.\n\nExisting kiln system design, fuel mix properties including waste and raw material burnability (e.g. special cement or white cement clinker) can influence the ability to be within the range. Levels below 350 mg/Nm 3 are achieved at kilns with favourable conditions when using SNCR. In 2008, the lower value of 200 mg/Nm 3 has been reported as a monthly average for three plants (easy burning mix used) using SNCR.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Domestic glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Electric melting","kg/tonne melted glass","N/A","0.3","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","A conversion factor of 2,5 × 10 –3 has been applied for combustion modifications and special furnace designs and a conversion factor of 3 × 10 –3 has been applied for electric melting (see Table 2). However, a case-by-case conversion factor may have to be applied for specific productions."]
["Cement lime and MgO","3. Mineral Industry ","Lime","Unspecified","LRK, PRK","Unspecified","Unspecified","Unspecified","Kiln firing process","Air","Nitrogen dioxide","In order to reduce the emissions of NO X from the flue-gases of kiln firing processes, BAT is to use one or a combination of the following techniques:(i) Primary techniques; (ii) SNCR","mg/Nm3",200,"500","Green","Continuous",0,0,0.11,"daily average value or average over the sampling period (spot measurements for at least half an hour), stated as NO 2","The higher ends of the ranges are related to the production of dolime and hard burned lime. Higher levels than the upper end of the range may be associated with the production of sintered dolime.\n\nWhere primary techniques as indicated in BAT 45 (a)I are not sufficient to reach this level and where secondary techniques are not applicable to reduce the NO x emissions to 350 mg/Nm 3 , the upper level is 500 mg/Nm 3 , especially for hard burned lime and for the use of biomass as fuel.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Domestic glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Oxy-fuel melting","mg/Nm3","N/A","N/A","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The achievable levels depend on the quality of the natural gas and oxygen available (nitrogen content)."]
["Cement lime and MgO","3. Mineral Industry ","Lime","Unspecified","PFRK, ASK, MFSK, OSK","Unspecified","Unspecified","Unspecified","Kiln firing process","Air","Nitrogen dioxide","In order to reduce the emissions of NO X from the flue-gases of kiln firing processes, BAT is to use one or a combination of the following techniques:(i) Primary techniques; (ii) SNCR","mg/Nm3",100,"350","Green","Continuous",0,0,0.11,"daily average value or average over the sampling period (spot measurements for at least half an hour), stated as NO 2","The higher ends of the ranges are related to the production of dolime and hard burned lime. Higher levels than the upper end of the range may be associated with the production of sintered dolime.\n\nWhere primary techniques as indicated in BAT 45 (a)I are not sufficient to reach this level and where secondary techniques are not applicable to reduce the NO x emissions to 350 mg/Nm 3 , the upper level is 500 mg/Nm 3 , especially for hard burned lime and for the use of biomass as fuel.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Domestic glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Oxy-fuel melting","kg/tonne melted glass","0.5","1.5","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","A conversion factor of 2,5 × 10 –3 has been applied for combustion modifications and special furnace designs and a conversion factor of 3 × 10 –3 has been applied for electric melting (see Table 2). However, a case-by-case conversion factor may have to be applied for specific productions.\n\nThe achievable levels depend on the quality of the natural gas and oxygen available (nitrogen content)."]
["Cement lime and MgO","3. Mineral Industry ","Magnesium oxide","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Kiln firing process","Air","Nitrogen dioxide","In order to reduce the emissions of NO x from the flue-gases of kiln firing processes, BAT is to use a combination of the following techniques: (i) Appropriate fuel selection along with a limited nitrogen content in the fuel; (ii) Process optimisation and improved firing technique","mg/Nm3",500,"1500","Green","Continuous",0,0,0.1,"Daily","The higher values are related to the high temperature DBM process.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Filament glass fibre","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Combustion modifications","mg/Nm3","600","1000","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)",0]
["Cement lime and MgO","3. Mineral Industry ","Cement","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Kiln firing process","Air","PCDD/F","In order to prevent emissions of PCDD/F or to keep the emissions of PCDD/F from the flue-gases of the kiln firing processes low, BAT is to use one or a combination of the following techniques: (i) Carefully selecting and controlling of kiln inputs (raw materials), i.e. chlorine, copper and volatile organic compounds; (ii) Carefully selecting and controlling kiln inputs (fuels), i.e. chlorine and copper; (iii) Limiting/avoiding the use of wastes which contain chlorinated organic materials; (iv) Avoid feeding fuels with a high content of halogens (e.g. chlorine) in secondary firing; (v) Quick cooling of kiln flue-gases to lower than 200 °C and minimising residence time of flue-gases and oxygen content in zones where the temperatures range between 300 and 450 °C; (vi) Stop co-incinerating waste for operations such as start-ups and/or shutdowns","ng PCDD/F I-TEQ/Nm 3",0.05,"0.1","Green","Periodic",0,0,0.1,"average over the sampling period (6 – 8 hours)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Filament glass fibre","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Combustion modifications","kg/tonne melted glass","2.7","4.5","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The conversion factor reported in Table 2 (4,5 × 10 –3 ) has been applied."]
["Cement lime and MgO","3. Mineral Industry ","Lime","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Kiln firing process","Air","PCDD/F","In order to prevent or reduce the emissions of PCDD/F from the flue-gas of kiln firing processes, BAT is to use one or a combination of the following primary techniques: (i) Selecting fuels with a low chlorine content; (ii) limiting the copper input through the fuel; (iii) Minimsing the residence time of the flue gases and the oxygen content in zones where the termperatures range between 300-450oC","ng PCDD/F I-TEQ/Nm 3",0.05,"0.1","Green","Periodic",0,0,0.11,"average over the sampling period (6 – 8 hours)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Filament glass fibre","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Oxy-fuel melting","mg/Nm3","N/A","N/A","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The achievable levels depend on the quality of the natural gas and oxygen available (nitrogen content)."]
["Cement lime and MgO","3. Mineral Industry ","Cement","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to reduce/minimise the emissions of SO x from the flue-gases of kiln firing and/or preheating/precalcining processes, BAT is to use one of the following techniques: (i) Absorbent addition; (ii) Wet scrubber","mg/Nm3",50,"400","Green","Continuous",0,0,"Unspecified","Daily ","The range takes into account the sulphur content in the raw materials.\n\nFor white cement and special cement clinker production, the ability of clinker to retain fuel sulphur might be significantly lower leading to higher SO X emissions.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Filament glass fibre","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Oxy-fuel melting","kg/tonne melted glass","0.5","1.5","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The achievable levels depend on the quality of the natural gas and oxygen available (nitrogen content)."]
["Cement lime and MgO","3. Mineral Industry ","Lime","Unspecified","LRK, PRK","Unspecified","Unspecified","Unspecified","Kiln firing process","Air","Sulphur Dioxide (24 Hour Mean)","In order to reduce the emissions of SO x from the flue-gases of kiln firing processes, BAT is to use one or a combination of the following techniques: (i) Process optimisation to ensure an efficient absorption of sulphur dioxide (e.g. efficient contact between the kiln gases and the quicklime); (ii) Selecting fuels with a low sulphur content; (iii) Using absorbent addition techniques (e.g. absorbent addition, dry flue-gas cleaning with a filter, wet scrubber, or activated carbon injection)","mg/Nm3",50,"400","Green","Continuous",0,0,0.11,"daily average value or average over the sampling period (spot measurements for at least half an hour), SO x expressed as SO 2","The level depends on the initial SO x level in the flue-gas and on the reduction technique used.\n\nFor the production of sintered dolime using the ‘double- pass process’, SO x emissions might be higher than the upper end of the range.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Flat glass","Nitrates in batch formulation","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Primary techniques ","mg/Nm3","N/A",1200,"Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","BAT-AEL for NO X emissions from the melting furnace in the flat glass sector, when nitrates are used in the batch formulation for the production of special glasses in a limited number of short campaigns"]
["Cement lime and MgO","3. Mineral Industry ","Lime","Unspecified","PFRK, ASK, MFSK, OSK","Unspecified","Unspecified","Unspecified","Kiln firing process","Air","Sulphur Dioxide (24 Hour Mean)","In order to reduce the emissions of SO x from the flue-gases of kiln firing processes, BAT is to use one or a combination of the following techniques: (i) Process optimisation to ensure an efficient absorption of sulphur dioxide (e.g. efficient contact between the kiln gases and the quicklime); (ii) Selecting fuels with a low sulphur content; (iii) Using absorbent addition techniques (e.g. absorbent addition, dry flue-gas cleaning with a filter, wet scrubber, or activated carbon injection)","mg/Nm3",50,"200","Green","Continuous",0,0,0.11,"daily average value or average over the sampling period (spot measurements for at least half an hour), SO x expressed as SO 2","The level depends on the initial SO x level in the flue-gas and on the reduction technique used.\n\nFor the production of sintered dolime using the ‘double- pass process’, SO x emissions might be higher than the upper end of the range.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Flat glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Combustion modifications, Fenix process","mg/Nm3",700,800,"Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","Higher emission levels are expected when nitrates are used occasionally for the production of special glasses.\n\nThe lower levels of the range are associated with the application of the Fenix process"]
["Cement lime and MgO","3. Mineral Industry ","Magnesium oxide","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Kiln firing process","Air","Sulphur Dioxide (24 Hour Mean)","In order to reduce the emissions of SO x from the flue-gases of kiln firing processes, BAT is to use a combination of the following primary and secondary techniques: (i) Process optimisation techniques; (ii) Selecting fuels with a low sulphur content; (iii) A dry absorbent addition technique (sorbent addition into the flue gas stream such as reactive MgO grades, hydrated lime, activated carbon, etc.), in combination with a filter; (iv) Wet scrubber","mg/Nm3",50,"400","Green","Continuous",0,0,0.1,"daily average value or average over the sampling period (spot measurements for at least half an hour","The BAT-AELs depend on the content of sulphur in the raw materials and fuels. The lower end of the range is associated with the use of raw materials with low sulphur content and the use of natural gas; the upper end of the range is associated with the use of raw materials with higher sulphur content and/or the use of sulphur-containing fuels.\n\nCross-media effects should be taken into account to assess the best combination of BAT to reduce SO x emissions.\n\nWhen a wet scrubber is not applicable, BAT-AELs depend on the sulphur content of raw materials and fuels. In this case, the BAT-AEL is < 1 500 mg/Nm 3 while ensuring a SO X emissions removal efficiency of at least 60 %.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Flat glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Combustion modifications, Fenix process","kg/tonne melted glass",1.75,2,"Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","Higher emission levels are expected when nitrates are used occasionally for the production of special glasses.\n\nThe lower levels of the range are associated with the application of the Fenix process\n\nThe conversion factor reported in Table 2 (2,5 × 10 –3 ) has been applied"]
["Cement lime and MgO","3. Mineral Industry ","Lime","Unspecified","ASK, MFSK, PFRK","Unspecified","Unspecified","Unspecified","Kiln firing process","Air","Total organic compounds","In order to reduce the emissions of TOC from the flue-gases of kiln firing processes, BAT is to use one or a combination of the following techniques: (i) Applying general primary techniques and monitoring (see also BAT 30 and 31 in Section 1.3.1, and BAT 32 in Section 1.3.2); (ii) Avoid feeding raw materials with a high content of volatile organic compounds into the kiln system (except for hydraulic lime production)","mg/Nm3","N/A","30","Green","Continuous",0,0,0.11,"daily average value or average over the sampling period (spot measurements for at least half an hour)","Level can be higher depending on the content of organic matter of raw materials used and/or the type of lime produced, in particular for the production of natural hydraulic lime.\n\nIn exceptional cases, the level can be higher.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Flat glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Oxy-fuel melting","mg/Nm3","N/A","N/A","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","Higher emission levels are expected when nitrates are used occasionally for the production of special glasses.\n\nThe achievable levels depend on the quality of the natural gas and oxygen available (nitrogen content)."]
["Cement lime and MgO","3. Mineral Industry ","Lime","Unspecified","LRK, PRK","Unspecified","Unspecified","Unspecified","Kiln firing process","Air","Total organic compounds","In order to reduce the emissions of TOC from the flue-gases of kiln firing processes, BAT is to use one or a combination of the following techniques: (i) Applying general primary techniques and monitoring (see also BAT 30 and 31 in Section 1.3.1, and BAT 32 in Section 1.3.2); (ii) Avoid feeding raw materials with a high content of volatile organic compounds into the kiln system (except for hydraulic lime production)","mg/Nm3","N/A","10","Green","Continuous",0,0,0.11,"daily average value or average over the sampling period (spot measurements for at least half an hour)","Level can be higher depending on the content of organic matter of raw materials used and/or the type of lime produced, in particular for the production of natural hydraulic lime",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Flat glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Oxy-fuel melting","kg/tonne melted glass","1.25","2.0","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","Higher emission levels are expected when nitrates are used occasionally for the production of special glasses.\n\nThe achievable levels depend on the quality of the natural gas and oxygen available (nitrogen content).\n\nThe conversion factor reported in Table 2 (2,5 × 10 –3 ) has been applied."]
["Chlor Alkali","4. Chemical industry","Chloralkali industry","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Processing of chlorine","Air","Chlorine","In order to reduce channelled emissions of chlorine and chlorine dioxide to air from the processing of chlorine, BAT is to design, maintain and operate a chlorine absorption unit that incorporates an appropriate combination of the following features:\n(i) absorption unit based on packed columns and/or ejectors with an alkaline solution (e.g. sodium hydroxide solution) as scrubbing liquid;\n(ii) hydrogen peroxide dosing equipment or a separate wet scrubber with hydrogen peroxide if necessary to reduce chlorine dioxide concentrations;\n(iii) size suitable for the worst case scenario (derived from a risk assessment), in terms of produced chlorine quantity and flowrate (absorption of the full cell room production for a sufficient duration until the plant is shut down);\n(iv) size of the scrubbing liquid supply and storage capacity suitable to ensure an excess at all times;\n(v) in the case of packed columns, their size should be suitable to prevent flooding at all times;\n(vi) prevention of ingress of liquid chlorine into the absorption unit;\n(vii) prevention of backflow of scrubbing liquid into the chlorine system;\n(viii) prevention of solids precipitation in the absorption unit;\n(ix) use of heat exchangers to limit the temperature in the absorption unit below 55 °C at all times;\n(x) supply of dilution air after chlorine absorption to prevent the formation of explosive gas mixtures;\n(xi) use of construction materials which withstand the extremely corrosive conditions at all times;\n(xii) use of backup equipment, such as an additional scrubber in series with the one in operation, an emergency tank with scrubbing liquid feeding the scrubber by gravity, stand-by and spare fans, stand-by and spare pumps;\n(xiii) provision of an independent backup system for critical electrical equipment;\n(xiv) provision of an automatic switch to the backup system in case of emergencies, including periodic tests on this system and the switch;\n(xv) provision of a monitoring and alarm system for the following parameters:\n(a) chlorine in the outlet of the absorption unit and the surrounding area;\n(b) temperature of the scrubbing liquids;\n(c) reduction potential and alkalinity of the scrubbing liquids;\n(d) suction pressure;\n(e) flowrate of scrubbing liquids.","mg/m3",0.2,1,"Green","Continous with electrochemical cells\n\nYearly with absorption in a solution with subsequent analysis",0,0,"Unspecified","average value of at least three consecutive hourly measurements performed at least once every year at the outlet of the chlorine absorption unit.",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Flat glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Secondary techniques","mg/Nm3",400,700,"Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","Higher emission levels are expected when nitrates are used occasionally for the production of special glasses.\n\nThe higher levels of the range are associated with existing plants until a normal or complete rebuild of the melting furnace. The lower levels are associated with newer/retrofitted plants.\n"]
["Chlor Alkali","4. Chemical industry","Chloralkali industry","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Water","Chlorine (95%ile)","In order to reduce emissions of free chlorine to water from the chlor-alkali plant, BAT is to treat waste water streams containing free chlorine as close as possible to the source, to prevent stripping of chlorine and/or the formation of halogenated organic compounds, by using one or a combination of the techniques given below: (i) Chemical reduction; (ii) Catalytic decomposition; (iii) Thermal decomposition; (iv) Acidic decomposition; (v) Waste water recycling","mg/l",0.05,0.2,"Green","Continouos ",0,0,"Unspecified",0,0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Flat glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Secondary techniques","kg/tonne melted glass",1,1.75,"Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","Higher emission levels are expected when nitrates are used occasionally for the production of special glasses.\n\nThe higher levels of the range are associated with existing plants until a normal or complete rebuild of the melting furnace. The lower levels are associated with newer/retrofitted plants.\n"]
["Common Waste Water and Waste Gas Treatment","4. Chemical industry","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Whole plant","Water","Adsorbable organically bound halogens (AOX)","Appropriate final waste water treatment techniques, depending on the pollutant, include:\n\nPreliminary and primary treatment:(i) Equalisation; (ii) Neutralisation; (iii) Physical separation, e.g.\nscreens, sieves, grit separators,\ngrease separators or\nprimary settlement tanks \n\nBiological treatment: (i) Activated sludge process; (ii) Membrane bioreactor\n\nNitrogen removal: (i) Nitrification/denitrification\n\nPhosphorus removal: (i) Chemical precipitation\n\nFinal solids removal: (i) Coagulation and flocculation; (ii) Sedimentation; (iii) Filtration (e.g. sand filtration,\nmicrofiltration, ultrafiltration); (iv) Flotation\n","mg/l",0.2,1,"Green","Monthly",0,0,"N/A","Yearly","The lower end of the range is typically achieved when few halogenated organic compounds are used or produced by the installation\n\nThis BAT-AEL may not apply when the main pollutant load originates from the production of iodinated X-ray contrast agents due\nto the high refractory loads. This BAT-AEL may also not apply when the main pollutant load originates from the production of propylene\noxide or epichlorohydrin via the chlorohydrin process due to the high loads. ",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Frits ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Primary techniques: Fuel/air, fuel/oxygen-enriched air combustion, with nitrates ","mg/Nm3","N/A","1600","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The ranges take into account the combination of flue-gases from furnaces applying different melting techniques and producing a variety of frit types, with or without nitrates in the batch formulations, which may be conveyed to a single stack, precluding the possibility of characterising each applied melting technique and the different products."]
["Common Waste Water and Waste Gas Treatment","4. Chemical industry","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Whole plant","Water","COD","Appropriate final waste water treatment techniques, depending on the pollutant, include:\n\nPreliminary and primary treatment:(i) Equalisation; (ii) Neutralisation; (iii) Physical separation, e.g.\nscreens, sieves, grit separators,\ngrease separators or\nprimary settlement tanks \n\nBiological treatment: (i) Activated sludge process; (ii) Membrane bioreactor\n\nNitrogen removal: (i) Nitrification/denitrification\n\nPhosphorus removal: (i) Chemical precipitation\n\nFinal solids removal: (i) Coagulation and flocculation; (ii) Sedimentation; (iii) Filtration (e.g. sand filtration,\nmicrofiltration, ultrafiltration); (iv) Flotation\n","mg/l",30,100,"Green","Daily",0,0,"N/A","Yearly","No BAT-AEL applies for Biochemical oxygen demand (BOD). As an indication, the yearly average BOD5 level in the effluent from a biological waste water treatment plant will generally be ≤ 20 mg/l.\n\nEither the BAT-AEL for TOC or the BAT-AEL for COD applies. TOC is the preferred option because its monitoring does not rely on\nthe use of very toxic compounds. \n\nThe lower end of the range is typically achieved when few tributary waste water streams contain organic compounds and/or the\nwaste water mostly contains easily biodegradable organic compounds. \n\nThe upper end of the range may be up to 100 mg/l for TOC or up to 300 mg/l for COD, both as yearly averages, if both of the following\nconditions are fulfilled:\n— Condition A: Abatement efficiency ≥ 90 % as a yearly average (including both pretreatment and final treatment).\n— Condition B: If a biological treatment is used, at least one of the following criteria is met:\n— A low-loaded biological treatment step is used (i.e. ≤ 0,25 kg COD/kg of organic dry matter of sludge). This implies that the\nBOD5 level in the effluent is ≤ 20 mg/l.\n— Nitrification is used. \n\nThe upper end of the range may not apply if all of the following conditions are fulfilled:\n— Condition A: Abatement efficiency ≥ 95 % as a yearly average (including both pretreatment and final treatment).\n— Condition B: same as Condition B in footnote (4).\n— Condition C: The influent to the final waste water treatment shows the following characteristics: TOC > 2 g/l (or COD > 6 g/l)\nas a yearly average and a high proportion of refractory organic compounds. \n\nThe upper end of the range may not apply when the main pollutant load originates from the production of methylcellulose. \n\nThe BAT-AEL applies if the emission exceeds\n10 t/yr. ",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Frits ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Primary techniques: Fuel/air, fuel/oxygen-enriched air combustion, with nitrates ","kg/tonne melted glass","N/A","12","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The ranges take into account the combination of flue-gases from furnaces applying different melting techniques and producing a variety of frit types, with or without nitrates in the batch formulations, which may be conveyed to a single stack, precluding the possibility of characterising each applied melting technique and the different products.\n\nThe conversion factors of 5 × 10 –3 and 7,5 × 10 –3 have been used for the determination of the lower and higher values of the range. However, a case-by-case conversion factor may have to be applied based on the type of combustion"]
["Common Waste Water and Waste Gas Treatment","4. Chemical industry","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Whole plant","Water","Chromium VI (95%ile) (dissolved)","Appropriate final waste water treatment techniques, depending on the pollutant, include:\n\nPreliminary and primary treatment:(i) Equalisation; (ii) Neutralisation; (iii) Physical separation, e.g.\nscreens, sieves, grit separators,\ngrease separators or\nprimary settlement tanks \n\nBiological treatment: (i) Activated sludge process; (ii) Membrane bioreactor\n\nNitrogen removal: (i) Nitrification/denitrification\n\nPhosphorus removal: (i) Chemical precipitation\n\nFinal solids removal: (i) Coagulation and flocculation; (ii) Sedimentation; (iii) Filtration (e.g. sand filtration,\nmicrofiltration, ultrafiltration); (iv) Flotation\n","mg/l",5,25,"Green","Monthly",0,0,"N/A","Yearly","The lower end of the range is typically achieved when few of the corresponding metal (compounds) are used or produced by the installation\n\nThis BAT-AEL may not apply to inorganic effluents when the main pollutant load originates from the production of inorganic\nheavy metal compounds.\n\nThis BAT-AEL may not apply when the main pollutant load originates from the processing of large volumes of solid inorganic raw\nmaterials that are contaminated with metals (e.g. soda ash from the Solvay process, titanium dioxide).       \n\nThis BAT-AEL may not apply when the main pollutant load originates from the production of chromium-organic compounds.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Frits ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Primary techniques: Fuel/air, fuel/oxygen-enriched air combustion, without nitrates ","mg/Nm3","500","1000","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The ranges take into account the combination of flue-gases from furnaces applying different melting techniques and producing a variety of frit types, with or without nitrates in the batch formulations, which may be conveyed to a single stack, precluding the possibility of characterising each applied melting technique and the different products."]
["Common Waste Water and Waste Gas Treatment","4. Chemical industry","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Whole plant","Water","Copper (expressed as Cu)","Appropriate final waste water treatment techniques, depending on the pollutant, include:\n\nPreliminary and primary treatment:(i) Equalisation; (ii) Neutralisation; (iii) Physical separation, e.g.\nscreens, sieves, grit separators,\ngrease separators or\nprimary settlement tanks \n\nBiological treatment: (i) Activated sludge process; (ii) Membrane bioreactor\n\nNitrogen removal: (i) Nitrification/denitrification\n\nPhosphorus removal: (i) Chemical precipitation\n\nFinal solids removal: (i) Coagulation and flocculation; (ii) Sedimentation; (iii) Filtration (e.g. sand filtration,\nmicrofiltration, ultrafiltration); (iv) Flotation\n","mg/l",5,50,"Green","Monthly",0,0,"N/A","Yearly","The lower end of the range is typically achieved when few of the corresponding metal (compounds) are used or produced by the installation\n\nThis BAT-AEL may not apply to inorganic effluents when the main pollutant load originates from the production of inorganic\nheavy metal compounds.\n\nThis BAT-AEL may not apply when the main pollutant load originates from the processing of large volumes of solid inorganic raw\nmaterials that are contaminated with metals (e.g. soda ash from the Solvay process, titanium dioxide).       \n\nThis BAT-AEL may not apply when the main pollutant load originates from the production of chromium-organic compounds.\n\nThis BAT-AEL may not apply when the main pollutant load originates from the production of copper-organic compounds or the\nproduction of vinyl chloride monomer/ethylene dichloride via the oxychlorination process. ",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Frits ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Primary techniques: Fuel/air, fuel/oxygen-enriched air combustion, without nitrates ","kg/tonne melted glass","2.5","7.5","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The ranges take into account the combination of flue-gases from furnaces applying different melting techniques and producing a variety of frit types, with or without nitrates in the batch formulations, which may be conveyed to a single stack, precluding the possibility of characterising each applied melting technique and the different products.\n\nThe conversion factors of 5 × 10 –3 and 7,5 × 10 –3 have been used for the determination of the lower and higher values of the range. However, a case-by-case conversion factor may have to be applied based on the type of combustion"]
["Common Waste Water and Waste Gas Treatment","4. Chemical industry","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Whole plant","Water","Nickel and its compounds","Appropriate final waste water treatment techniques, depending on the pollutant, include:\n\nPreliminary and primary treatment:(i) Equalisation; (ii) Neutralisation; (iii) Physical separation, e.g.\nscreens, sieves, grit separators,\ngrease separators or\nprimary settlement tanks \n\nBiological treatment: (i) Activated sludge process; (ii) Membrane bioreactor\n\nNitrogen removal: (i) Nitrification/denitrification\n\nPhosphorus removal: (i) Chemical precipitation\n\nFinal solids removal: (i) Coagulation and flocculation; (ii) Sedimentation; (iii) Filtration (e.g. sand filtration,\nmicrofiltration, ultrafiltration); (iv) Flotation\n","mg/l",5,50,"Green","Monthly",0,0,"N/A","Yearly","The lower end of the range is typically achieved when few of the corresponding metal (compounds) are used or produced by the installation\n\nThis BAT-AEL may not apply to inorganic effluents when the main pollutant load originates from the production of inorganic\nheavy metal compounds.\n\nThis BAT-AEL may not apply when the main pollutant load originates from the processing of large volumes of solid inorganic raw\nmaterials that are contaminated with metals (e.g. soda ash from the Solvay process, titanium dioxide).   ",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Frits ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Primary techniques: Oxy fuel firing, with use nitrates","kg/tonne melted glass","5","10","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The ranges take into account the combination of flue-gases from furnaces applying different melting techniques and producing a variety of frit types, with or without nitrates in the batch formulations, which may be conveyed to a single stack, precluding the possibility of characterising each applied melting technique and the different products.\n\nThe conversion factors of 5 × 10 –3 and 7,5 × 10 –3 have been used for the determination of the lower and higher values of the range. However, a case-by-case conversion factor may have to be applied based on the type of combustion"]
["Common Waste Water and Waste Gas Treatment","4. Chemical industry","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Whole plant","Water","Total inorganic nitrogen (Ninorg)","Appropriate final waste water treatment techniques, depending on the pollutant, include:\n\nPreliminary and primary treatment:(i) Equalisation; (ii) Neutralisation; (iii) Physical separation, e.g.\nscreens, sieves, grit separators,\ngrease separators or\nprimary settlement tanks \n\nBiological treatment: (i) Activated sludge process; (ii) Membrane bioreactor\n\nNitrogen removal: (i) Nitrification/denitrification\n\nPhosphorus removal: (i) Chemical precipitation\n\nFinal solids removal: (i) Coagulation and flocculation; (ii) Sedimentation; (iii) Filtration (e.g. sand filtration,\nmicrofiltration, ultrafiltration); (iv) Flotation\n","mg/l",5,20,"Green","Daily",0,0,"N/A","Yearly","Either the BAT-AEL for total nitrogen or the BAT-AEL for total inorganic nitrogen applies. \n\nThe BAT-AELs for TN and Ninorg do not apply to installations without biological waste water treatment. The lower end of the range\nis typically achieved when the influent to the biological waste water treatment plant contains low levels of nitrogen and/or when nitrification/denitrification\ncan be operated under optimum conditions. \n\nThe upper end of the range may be higher and up to 40 mg/l for TN or 35 mg/l for Ninorg, both as yearly averages, if the abatement\nefficiency is ≥ 70 % as a yearly average (including both pretreatment and final treatment). ",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Frits ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Primary techniques: Oxy fuel firing, without nitrates","kg/tonne melted glass","2.5","5","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The ranges take into account the combination of flue-gases from furnaces applying different melting techniques and producing a variety of frit types, with or without nitrates in the batch formulations, which may be conveyed to a single stack, precluding the possibility of characterising each applied melting technique and the different products.\n\nThe conversion factors of 5 × 10 –3 and 7,5 × 10 –3 have been used for the determination of the lower and higher values of the range. However, a case-by-case conversion factor may have to be applied based on the type of combustion"]
["Common Waste Water and Waste Gas Treatment","4. Chemical industry","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Whole plant","Water","Total Nitrogen (TN)","Appropriate final waste water treatment techniques, depending on the pollutant, include:\n\nPreliminary and primary treatment:(i) Equalisation; (ii) Neutralisation; (iii) Physical separation, e.g.\nscreens, sieves, grit separators,\ngrease separators or\nprimary settlement tanks \n\nBiological treatment: (i) Activated sludge process; (ii) Membrane bioreactor\n\nNitrogen removal: (i) Nitrification/denitrification\n\nPhosphorus removal: (i) Chemical precipitation\n\nFinal solids removal: (i) Coagulation and flocculation; (ii) Sedimentation; (iii) Filtration (e.g. sand filtration,\nmicrofiltration, ultrafiltration); (iv) Flotation\n","mg/l",5,25,"Green","Daily",0,0,"N/A","Yearly","Either the BAT-AEL for total nitrogen or the BAT-AEL for total inorganic nitrogen applies. \n\nThe BAT-AELs for TN and Ninorg do not apply to installations without biological waste water treatment. The lower end of the range\nis typically achieved when the influent to the biological waste water treatment plant contains low levels of nitrogen and/or when nitrification/denitrification\ncan be operated under optimum conditions. \n\nThe upper end of the range may be higher and up to 40 mg/l for TN or 35 mg/l for Ninorg, both as yearly averages, if the abatement\nefficiency is ≥ 70 % as a yearly average (including both pretreatment and final treatment). ",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","HTIW wools","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Lubricant burn-off oven ","Air","Nitrogen dioxide","BAT is to reduce NO X emissions from the lubricant burn-off oven by applying combustion control and/or modifications","mg/Nm3","100","200","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3","N/A","Daily average (continuous)",0]
["Common Waste Water and Waste Gas Treatment","4. Chemical industry","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Whole plant","Water","Total Organic Carbon (TOC)","Appropriate final waste water treatment techniques, depending on the pollutant, include:\n\nPreliminary and primary treatment:(i) Equalisation; (ii) Neutralisation; (iii) Physical separation, e.g.\nscreens, sieves, grit separators,\ngrease separators or\nprimary settlement tanks \n\nBiological treatment: (i) Activated sludge process; (ii) Membrane bioreactor\n\nNitrogen removal: (i) Nitrification/denitrification\n\nPhosphorus removal: (i) Chemical precipitation\n\nFinal solids removal: (i) Coagulation and flocculation; (ii) Sedimentation; (iii) Filtration (e.g. sand filtration,\nmicrofiltration, ultrafiltration); (iv) Flotation\n","mg/l",10,33,"Green","Daily",0,0,"N/A","Yearly","No BAT-AEL applies for Biochemical oxygen demand (BOD). As an indication, the yearly average BOD5 level in the effluent from a biological waste water treatment plant will generally be ≤ 20 mg/l.\n\nEither the BAT-AEL for TOC or the BAT-AEL for COD applies. TOC is the preferred option because its monitoring does not rely on\nthe use of very toxic compounds. \n\nThe lower end of the range is typically achieved when few tributary waste water streams contain organic compounds and/or the\nwaste water mostly contains easily biodegradable organic compounds. \n\nThe upper end of the range may be up to 100 mg/l for TOC or up to 300 mg/l for COD, both as yearly averages, if both of the following\nconditions are fulfilled:\n— Condition A: Abatement efficiency ≥ 90 % as a yearly average (including both pretreatment and final treatment).\n— Condition B: If a biological treatment is used, at least one of the following criteria is met:\n— A low-loaded biological treatment step is used (i.e. ≤ 0,25 kg COD/kg of organic dry matter of sludge). This implies that the\nBOD5 level in the effluent is ≤ 20 mg/l.\n— Nitrification is used. \n\nThe upper end of the range may not apply if all of the following conditions are fulfilled:\n— Condition A: Abatement efficiency ≥ 95 % as a yearly average (including both pretreatment and final treatment).\n— Condition B: same as Condition B in footnote (4).\n— Condition C: The influent to the final waste water treatment shows the following characteristics: TOC > 2 g/l (or COD > 6 g/l)\nas a yearly average and a high proportion of refractory organic compounds. \n\nThe upper end of the range may not apply when the main pollutant load originates from the production of methylcellulose. \n\nThe BAT-AEL applies if the emission exceeds\n3,3 t/yr. ",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Mineral wool","Glass wool","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","All types of furnaces","kg/tonne melted glass","1.0","1.25","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The conversion factors of 2 × 10 –3 for glass wool and 2,5 × 10 –3 for stone wool have been used (see Table 2)."]
["Common Waste Water and Waste Gas Treatment","4. Chemical industry","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Whole plant","Water","Total phosphorous","Appropriate final waste water treatment techniques, depending on the pollutant, include:\n\nPreliminary and primary treatment:(i) Equalisation; (ii) Neutralisation; (iii) Physical separation, e.g.\nscreens, sieves, grit separators,\ngrease separators or\nprimary settlement tanks \n\nBiological treatment: (i) Activated sludge process; (ii) Membrane bioreactor\n\nNitrogen removal: (i) Nitrification/denitrification\n\nPhosphorus removal: (i) Chemical precipitation\n\nFinal solids removal: (i) Coagulation and flocculation; (ii) Sedimentation; (iii) Filtration (e.g. sand filtration,\nmicrofiltration, ultrafiltration); (iv) Flotation\n","mg/l",0.5,3,"Green","Daily",0,0,"N/A","Yearly","The lower end of the range is typically achieved when phosphorus is added for the proper operation of the biological waste water treatment plant or when phosphorus mainly originates from heating or cooling systems. The upper end of the range is typically achieved when phosphorus-containing compounds are produced by the installation.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Mineral wool","Glass wool","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Fuel/air and Electric furnaces","mg/Nm3","200","500","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)",0]
["Common Waste Water and Waste Gas Treatment","4. Chemical industry","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Whole plant","Water","Total Suspended Solids (TSS) ","Appropriate final waste water treatment techniques, depending on the pollutant, include:\n\nPreliminary and primary treatment:(i) Equalisation; (ii) Neutralisation; (iii) Physical separation, e.g.\nscreens, sieves, grit separators,\ngrease separators or\nprimary settlement tanks \n\nBiological treatment: (i) Activated sludge process; (ii) Membrane bioreactor\n\nNitrogen removal: (i) Nitrification/denitrification\n\nPhosphorus removal: (i) Chemical precipitation\n\nFinal solids removal: (i) Coagulation and flocculation; (ii) Sedimentation; (iii) Filtration (e.g. sand filtration,\nmicrofiltration, ultrafiltration); (iv) Flotation\n","mg/l",5,35,"Green","Daily",0,0,"N/A","Yearly","The lower end of the range is typically achieved when using filtration (e.g. sand filtration, microfiltration, ultrafiltration, membrane bioreactor), while the upper end of the range is typically achieved when using sedimentation only.\n\nThis BAT-AEL may not apply when the main pollutant load originates from the production of soda ash via the Solvay process or\nfrom the production of titanium dioxide. \n\nThe BAT-AEL applies if the emission exceeds\n3,5 t/yr. ",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Mineral wool","Glass wool","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Fuel/air and Electric furnaces","kg/tonne melted glass","0.4","1.0","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The conversion factors of 2 × 10 –3 for glass wool and 2,5 × 10 –3 for stone wool have been used"]
["Common Waste Water and Waste Gas Treatment","4. Chemical industry","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Whole plant","Water","Zinc (expressed as Zn)","Appropriate final waste water treatment techniques, depending on the pollutant, include:\n\nPreliminary and primary treatment:(i) Equalisation; (ii) Neutralisation; (iii) Physical separation, e.g.\nscreens, sieves, grit separators,\ngrease separators or\nprimary settlement tanks \n\nBiological treatment: (i) Activated sludge process; (ii) Membrane bioreactor\n\nNitrogen removal: (i) Nitrification/denitrification\n\nPhosphorus removal: (i) Chemical precipitation\n\nFinal solids removal: (i) Coagulation and flocculation; (ii) Sedimentation; (iii) Filtration (e.g. sand filtration,\nmicrofiltration, ultrafiltration); (iv) Flotation\n","mg/l",20,300,"Green","Monthly",0,0,"N/A","Yearly","The lower end of the range is typically achieved when few of the corresponding metal (compounds) are used or produced by the installation\n\nThis BAT-AEL may not apply to inorganic effluents when the main pollutant load originates from the production of inorganic\nheavy metal compounds.\n\nThis BAT-AEL may not apply when the main pollutant load originates from the processing of large volumes of solid inorganic raw\nmaterials that are contaminated with metals (e.g. soda ash from the Solvay process, titanium dioxide).   \n\nThis BAT-AEL may not apply when the main pollutant load originates from the production of viscose fibres. ",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Mineral wool","Glass wool","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Oxy-fuel melting","mg/Nm3","N/A","N/A","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The achievable levels depend on the quality of the natural gas and oxygen available (nitrogen content)."]
["Glass","3. Mineral industry","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes- Curing oven emissions ","Air","Amines","BAT is to reduce emissions from downstream processes by using one or a combination of the following techniques: (i) Impact jets and cyclones; (ii) Wet scrubbers; (iii) Wet electrostatic precipitators; (iv) Stone wool filters; (v) Waste gas incineration","mg/Nm3","N/A","2","Amber",0,"273.15","101.3","N/A","Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Mineral wool","Glass wool","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Oxy-fuel melting","kg/tonne melted glass","N/A","N/A","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The conversion factors of 2 × 10 –3 for glass wool and 2,5 × 10 –3 for stone wool have been used\n\nThe achievable levels depend on the quality of the natural gas and oxygen available (nitrogen content)."]
["Glass","3. Mineral industry","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes- Curing oven emissions ","Air","Amines","BAT is to reduce emissions from downstream processes by using one or a combination of the following techniques: (i) Impact jets and cyclones; (ii) Wet scrubbers; (iii) Wet electrostatic precipitators; (iv) Stone wool filters; (v) Waste gas incineration","kg/tonne melted glass","N/A","0.01","Amber",0,"273.15","101.3","N/A","Daily average (continuous)","The specific mass emissions refer to 1 tonne of produced glass",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Mineral wool","Nitrates in batch formulation","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Minimisation of nitrate input in the batch formulation, combined with primary techniques","mg/Nm3","500","700","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)",0]
["Glass","3. Mineral industry","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes- Forming area ","Air","Amines","BAT is to reduce emissions from downstream processes by using one or a combination of the following techniques: (i) Impact jets and cyclones; (ii) Wet scrubbers; (iii) Wet electrostatic precipitators; (iv) Stone wool filters; (v) Waste gas incineration","mg/Nm3","N/A","3","Amber",0,"273.15","101.3","N/A","Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Mineral wool","Nitrates in batch formulation","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Minimisation of nitrate input in the batch formulation, combined with primary techniques","kg/tonne melted glass","1.0","1.4","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The conversion factor of 2 × 10 –3 has been used\n\nThe lower levels of the ranges are associated with the application of oxy-fuel melting."]
["Glass","3. Mineral industry","Filament glass fibre","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes (forming and coating)","Air","Ammonia (ecological receptor - Sensitive Lichens)","BAT is to reduce emissions from downstream processes by using one or a combination of the following techniques: (i) Wet scrubbing systems; (ii) Wet electrostatic precipitator; (iii) Filtration system (bag filter)","mg/Nm3","N/A","20","Amber",0,"273.15","101.3","N/A","Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Mineral wool","Stone wool","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","All types of furnaces","mg/Nm3","400","500","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)",0]
["Glass","3. Mineral industry","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes- Curing oven emissions ","Air","Ammonia (ecological receptor - Sensitive Lichens)","BAT is to reduce emissions from downstream processes by using one or a combination of the following techniques: (i) Impact jets and cyclones; (ii) Wet scrubbers; (iii) Wet electrostatic precipitators; (iv) Stone wool filters; (v) Waste gas incineration","mg/Nm3","20","60","Green","Continuous or regular periodic measurements of NH 3 emissions, when selective catalytic reduction (SCR) or selective non-catalytic reduction (SNCR) techniques are applied","273.15","101.3","N/A","Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes- Curing oven emissions ","Air","Nitrogen dioxide","BAT is to reduce emissions from downstream processes by using one or a combination of the following techniques: (i) Impact jets and cyclones; (ii) Wet scrubbers; (iii) Wet electrostatic precipitators; (iv) Stone wool filters; (v) Waste gas incineration","mg/Nm3","100","200","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3","N/A","Daily average (continuous)",0]
["Glass","3. Mineral industry","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes- Curing oven emissions ","Air","Ammonia (ecological receptor - Sensitive Lichens)","BAT is to reduce emissions from downstream processes by using one or a combination of the following techniques: (i) Impact jets and cyclones; (ii) Wet scrubbers; (iii) Wet electrostatic precipitators; (iv) Stone wool filters; (v) Waste gas incineration","kg/tonne melted glass","N/A","0.4","Amber",0,"273.15","101.3","N/A","Daily average (continuous)","The specific mass emissions refer to 1 tonne of produced glass",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes- Curing oven emissions ","Air","Nitrogen dioxide","BAT is to reduce emissions from downstream processes by using one or a combination of the following techniques: (i) Impact jets and cyclones; (ii) Wet scrubbers; (iii) Wet electrostatic precipitators; (iv) Stone wool filters; (v) Waste gas incineration","kg/tonne melted glass","N/A","1","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3","N/A","Daily average (continuous)","The specific mass emissions refer to 1 tonne of produced glass"]
["Glass","3. Mineral industry","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes- Forming area ","Air","Ammonia (ecological receptor - Sensitive Lichens)","BAT is to reduce emissions from downstream processes by using one or a combination of the following techniques: (i) Impact jets and cyclones; (ii) Wet scrubbers; (iii) Wet electrostatic precipitators; (iv) Stone wool filters; (v) Waste gas incineration","mg/Nm3","30","60","Green","Continuous or regular periodic measurements of NH 3 emissions, when selective catalytic reduction (SCR) or selective non-catalytic reduction (SNCR) techniques are applied","273.15","101.3","N/A","Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Special glass ","Nitrates in batch formulation","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Minimisation of nitrate input in the batch formulation combined with primary or secondary techniques","mg/Nm3","500","1000","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The lower levels are associated with the use of electric melting."]
["Glass","3. Mineral industry","Container glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes","Air","Particulates (PM10) (24 hr Mean)","When tin, organotin or titanium compounds are used for hot-end coating operations, BAT is to reduce emissions by using one or a combination of the following techniques: (i) Minimising the losses of the coating product by ensuring a good sealing of the application system and applying an effective extracting hood; (ii) Combining the flue-gas from the coating operations with the waste gas from the melting furnace or with the combustion air of the furnace, when a secondary treatment system is applied (filter and dry or semi-dry scrubber); (iii) Applying a secondary technique, e.g. wet scrubbing, dry scrubbing plus filtration","mg/Nm3","N/A",10,"Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3","N/A","Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Special glass ","Nitrates in batch formulation","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Minimisation of nitrate input in the batch formulation combined with primary or secondary techniques","kg/tonne melted glass","1","6","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The lower levels are associated with the use of electric melting.\n\nThe conversion factors of 2,5 × 10 –3 and 6,5 × 10 –3 have been used for the determination of the lower and upper value of the BAT- AEL range respectively, with values being approximated. A case-by-case conversion factor may have to be applied based on the type of production."]
["Glass","3. Mineral industry","Container glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Particulates (PM10) (24 hr Mean)","Flue-gas cleaning system such as an electrostatic precipitator or a bag filter","mg/Nm3","10","20","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Special glass ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Combustion modifications","mg/Nm3","600","800","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)",0]
["Glass","3. Mineral industry","Container glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Particulates (PM10) (24 hr Mean)","Flue-gas cleaning system such as an electrostatic precipitator or a bag filter","kg/tonne melted glass","0.015","0.06","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The conversion factors of 1,5 × 10 –3 and 3 × 10 –3 have been used for the determination of the lower and higher value of the range respectively.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Special glass ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Combustion modifications","kg/tonne melted glass","1.5","3.2","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The conversion factors of 2,5 × 10 –3 and 4 × 10 –3 have been used for the determination of the lower and upper value of the BAT-AEL range (see Table 2), with some values being approximated. However, a case-by-case conversion factor needs to be applied based on the type of production."]
["Glass","3. Mineral industry","Domestic glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Dusty downstreatm processes ","Air","Particulates (PM10) (24 hr Mean)","For downstream dusty processes, BAT is to reduce emissions of dust and metals by using one or a combination of the following techniques: (i) Performing dusty operations (e.g. cutting, grinding, polishing) under liquid; (ii) Applying a bag filter system","mg/Nm3","1","10","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3","N/A","Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Special glass ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Electric melting","mg/Nm3","N/A","100","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)",0]
["Glass","3. Mineral industry","Domestic glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Particulates (PM10) (24 hr Mean)","BAT is to reduce dust emissions from the waste gases of the melting furnace by using one or a combination of the following techniques: (i) Reduction of the volatile components by raw material; (ii) electric melting; (iii) Oxy-fuel melting; (iv) Filtration system: electrostatic precipator or bag filter; (v) Wet scrubbing system ","mg/Nm3","10","20","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","Considerations concerning the economic viability for achieving the BAT-AELs in the case of furnaces with a capacity of < 80 t/d, producing soda-lime glass, are reported.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Special glass ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Electric melting","kg/tonne melted glass","0.25","0.4","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The conversion factors of 2,5 × 10 –3 and 4 × 10 –3 have been used for the determination of the lower and upper value of the BAT-AEL range (see Table 2), with some values being approximated. However, a case-by-case conversion factor needs to be applied based on the type of production."]
["Glass","3. Mineral industry","Domestic glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Particulates (PM10) (24 hr Mean)","BAT is to reduce dust emissions from the waste gases of the melting furnace by using one or a combination of the following techniques: (i) Reduction of the volatile components by raw material; (ii) electric melting; (iii) Oxy-fuel melting; (iv) Filtration system: electrostatic precipator or bag filter; (v) Wet scrubbing system ","kg/tonne melted glass","0.03","0.06","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","A conversion factor of 3 × 10 –3 has been applied (see Table 2). However, a case by case conversion factor may have to be applied for specific productions",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Special glass ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Oxy-fuel melting","mg/Nm3","N/A","N/A","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The higher values are related to a special production of borosilicate glass tubes for pharmaceutical use.\n\nThe achievable levels depend on the quality of the natural gas and oxygen available (nitrogen content)."]
["Glass","3. Mineral industry","Domestic glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Particulates (PM10) (24 hr Mean)","BAT is to reduce dust emissions from the waste gases of the melting furnace by using one or a combination of the following techniques: (i) Reduction of the volatile components by raw material; (ii) electric melting; (iii) Oxy-fuel melting; (iv) Filtration system: electrostatic precipator or bag filter; (v) Wet scrubbing system ","mg/Nm3","1","10","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","This BAT-AEL applies to batch formulations containing significant amounts of constituents meeting the criteria as dangerous substances, in accordance with Regulation (EC) No 1272/2008 of the European Parliament and of the Council.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Special glass ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Oxy-fuel melting","kg/tonne melted glass","1","3","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The conversion factors of 2,5 × 10 –3 and 4 × 10 –3 have been used for the determination of the lower and upper value of the BAT-AEL range (see Table 2), with some values being approximated. However, a case-by-case conversion factor needs to be applied based on the type of production.\n\nThe higher values are related to a special production of borosilicate glass tubes for pharmaceutical use.\n\nThe achievable levels depend on the quality of the natural gas and oxygen available (nitrogen content)."]
["Glass","3. Mineral industry","Domestic glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Particulates (PM10) (24 hr Mean)","BAT is to reduce dust emissions from the waste gases of the melting furnace by using one or a combination of the following techniques: (i) Reduction of the volatile components by raw material; (ii) electric melting; (iii) Oxy-fuel melting; (iv) Filtration system: electrostatic precipator or bag filter; (v) Wet scrubbing system ","kg/tonne melted glass","0.003","0.03","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","This BAT-AEL applies to batch formulations containing significant amounts of constituents meeting the criteria as dangerous substances, in accordance with Regulation (EC) No 1272/2008 of the European Parliament and of the Council.\n\nA conversion factor of 3 × 10 –3 has been applied (see Table 2). However, a case by case conversion factor may have to be applied for specific productions.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Special glass ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Secondary techniques","mg/Nm3","N/A","500","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)",0]
["Glass","3. Mineral industry","Filament glass fibre","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes (cutting and milling)","Air","Particulates (PM10) (24 hr Mean)","BAT is to reduce emissions from downstream processes by using one or a combination of the following techniques: (i) Wet scrubbing systems; (ii) Wet electrostatic precipitator; (iii) Filtration system (bag filter)","mg/Nm3","5","20","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3","N/A","Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Special glass ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Secondary techniques","kg/tonne melted glass","1","3","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The conversion factors of 2,5 × 10 –3 and 4 × 10 –3 have been used for the determination of the lower and upper value of the BAT-AEL range (see Table 2), with some values being approximated. However, a case-by-case conversion factor needs to be applied based on the type of production."]
["Glass","3. Mineral industry","Filament glass fibre","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes (forming and coating)","Air","Particulates (PM10) (24 hr Mean)","BAT is to reduce emissions from downstream processes by using one or a combination of the following techniques: (i) Wet scrubbing systems; (ii) Wet electrostatic precipitator; (iii) Filtration system (bag filter)","mg/Nm3","5","20","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3","N/A","Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Coke Oven Plants","Unspecified","Unspecified","Newor substantially revamped","Unspecified","Unspecified","Unspecified","Air","Nitrogen dioxide","BAT for the coke oven underfiring is to reduce the emissions by using the following techniques: (i) preventing leakage between the oven chamber and the heating chamber by means of regular coke oven operation; (ii) repairing leakage between the oven chamber and the heating chamber (only applicable to existing plants); (iii) incorporating low-nitrogen oxides (NOX) techniques in the construction of new batteries, such as staged combustion\nand the use of thinner bricks and refractory with a better thermal conductivity (only applicable to new plants); (iv) using desulphurised coke oven gas (COG) process gases ","mg/Nm3",350,500,"Green","Discontinuous ",0,0,0.05,"Daily mean average","This BAT is for new or substantially revamped\nplants (less than 10 years old)"]
["Glass","3. Mineral industry","Filament glass fibre","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Particulates (PM10) (24 hr Mean)","BAT is to reduce dust emissions from the waste gases of the melting furnace by using one or a combination of the following techniques: (i) Reduction of the volatile components by raw material; (ii) Filtration system: electrostatic precipitator or bag filter; (iii) Wet scrubbing system ","mg/Nm3","10","20","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","Values at levels of < 30 mg/Nm 3 (< 0,14 kg/tonne melted glass) have been reported for boron-free formulations, with the application of primary techniques.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Coke Oven Plants","Unspecified","Unspecified","Existing","Unspecified","Unspecified","Unspecified","Air","Nitrogen dioxide","BAT for the coke oven underfiring is to reduce the emissions by using the following techniques: (i) preventing leakage between the oven chamber and the heating chamber by means of regular coke oven operation; (ii) repairing leakage between the oven chamber and the heating chamber (only applicable to existing plants); (iii) incorporating low-nitrogen oxides (NOX) techniques in the construction of new batteries, such as staged combustion\nand the use of thinner bricks and refractory with a better thermal conductivity (only applicable to new plants); (iv) using desulphurised coke oven gas (COG) process gases ","mg/Nm3",500,650,"Green","Discontinuous ",0,0,0.05,"Daily mean average","This BAT is for older plants with well maintained batteries and incorporated low- nitrogen oxides (NOX) techniques."]
["Glass","3. Mineral industry","Flat glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes","Air","Particulates (PM10) (24 hr Mean)","BAT is to reduce emissions to air from the downstream processes by using one or a combination of the following techniques: (i) Minimising the losses of coating products applied to the flat glass by ensuring a good sealing of the application system; (ii) Minimising the losses of SO2 from the annealing ler, by operating the control system in an optimum manner; (iii) Combining the SO2 emissions from the lehr with the waste fas from the melting furnace, when technically feasible and where a secondary treatment system is applied (filter and dry or semi-dry scrubber); (iv) Applying a secondary technique, e.g. wet scrubbing, or dry scrubbing and filtration","mg/Nm3","15","20","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3","N/A","Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Sinter Plant","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Sinter strand","Air","Nitrogen dioxide","BAT for primary emissions from sinter strands is to reduce total nitrogen oxides (NOX) emissions by using one or\na combination of the following techniques:\n\nProcess integrated measures which can include: (i) waste gas recirculation; (ii) other primary measures, such as the use of anthracite or the use of low-NOX burners for ignition\n\n","mg/Nm3","N/A",500,"Green","Continuous",0,0,"Unspecified ","Daily mean value",0]
["Glass","3. Mineral industry","Flat glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Particulates (PM10) (24 hr Mean)","BAT is to reduce dust emissions from the waste gases of the melting furnace by applying an electrostatic precipitator or a bag filter system","mg/Nm3","10","20","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Sinter Plant","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Sinter strand","Air","Nitrogen dioxide","End-of-pipe techniques which can include:  selective catalytic reduction (SCR)","mg/Nm3","N/A",120,"Green","Continuous",0,0,0.15,"Daily mean value",0]
["Glass","3. Mineral industry","Flat glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Particulates (PM10) (24 hr Mean)","BAT is to reduce dust emissions from the waste gases of the melting furnace by applying an electrostatic precipitator or a bag filter system","kg/tonne melted glass","0.025","0.05","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Sinter Plant","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Sinter strand","Air","Nitrogen dioxide","End-of-pipe techniques which can include: the regenerative activated carbon (RAC) process","mg/Nm3","N/A",250,"Green","Continuous",0,0,0.15,"Daily mean value",0]
["Glass","3. Mineral industry","Frits ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes ","Air","Particulates (PM10) (24 hr Mean)","For downstream dusty processes, BAT is to reduce emissions by using one or a combination of the following techniques: (i) Applying wet milling techniques; (ii) Operating dry milling and dry product packaging under an efficient extraction system in conjunction with a fabric filter; (iii) Applying a filtration system","mg/Nm3","5","10","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3","N/A","Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Other","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Blast Furnaces: Hot blast stoves","Air","Nitrogen dioxide","BAT for hot blast stoves is to reduce emissions by using desulphurised and dedusted surplus coke oven gas, dedusted blast furnace gas, dedusted basic oxygen furnace gas and natural gas, individually or in combination.","mg/Nm3","N/A",100,"Green","Discontinuous ",0,0,0.03,"Daily mean values",0]
["Glass","3. Mineral industry","Frits ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Particulates (PM10) (24 hr Mean)","BAT is to reduce dust emissions from the waste gases of the melting furnace by means of an electrostatic precipitator or a bag filter system.","mg/Nm3","10","20","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","CCGT with a net total fuel utilisation of < 75 %","Existing","Natural gas ","50-600 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",10,"45","Green","Continuous ",0,0,0.15,"Yearly","These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines\n\nIn the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective.\n\nThese BAT-AELs do not apply to existing plants operated < 1 500 h/yr.\n\nOptimising the functioning of an existing technique to reduce NOX emissions further may lead to levels of CO emissions at the higher end of the indicative range for CO emissions given after this table.\n\nThese BAT-AELs do not apply to existing turbines for mechanical drive applications or to plants operated < 500 h/yr.\n\nFor plants with a net electrical efficiency (EE) greater than 55 %, a correction factor may be applied to the higher end of the BAT-AEL range, corresponding to [higher end] × EE/55, where EE is the net electrical efficiency of the plant determined at ISO baseload conditions."]
["Glass","3. Mineral industry","Frits ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Particulates (PM10) (24 hr Mean)","BAT is to reduce dust emissions from the waste gases of the melting furnace by means of an electrostatic precipitator or a bag filter system.","kg/tonne melted glass","0.05","0.15","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The conversion factors of 5 × 10 –3 and 7,5 × 10 –3 have been used for the determination of the lower and upper value of the BAT-AELs range (see Table 2). However, a case-by-case conversion factor may have to be applied based on the type of combustion.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","CCGT with a net total fuel utilisation of < 75 %","Existing","Natural gas ","50-600 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",35,"55","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period ","These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines\n\nIn the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective.\n\nThese BAT-AELs do not apply to existing turbines for mechanical drive applications or to plants operated < 500 h/yr.\n\nFor plants with a net electrical efficiency (EE) greater than 55 %, a correction factor may be applied to the higher end of the BAT-AEL range, corresponding to [higher end] × EE/55, where EE is the net electrical efficiency of the plant determined at ISO baseload conditions."]
["Glass","3. Mineral industry","HTIW wools","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes","Air","Particulates (PM10) (24 hr Mean)","BAT is to reduce dust emissions from the waste gases of the melting furnace by applying a filtration system.","mg/Nm3","5","20","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3","N/A","Daily average (continuous)","The values are associated with the use of a bag filter system.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","CCGT with a net total fuel utilisation of ≥ 75 %","Existing","Natural gas ","50-600 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",25,"50","Green","Continuous ",0,0,0.15,"Yearly","These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines\n\nIn the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective.\n\nThese BAT-AELs do not apply to existing plants operated < 1 500 h/yr.\n\nOptimising the functioning of an existing technique to reduce NOX emissions further may lead to levels of CO emissions at the higher end of the indicative range for CO emissions given after this table.\n\nThese BAT-AELs do not apply to existing turbines for mechanical drive applications or to plants operated < 500 h/yr.\n\nFor plants with a net electrical efficiency (EE) greater than 55 %, a correction factor may be applied to the higher end of the BAT-AEL range, corresponding to [higher end] × EE/55, where EE is the net electrical efficiency of the plant determined at ISO baseload conditions.\n\nFor existing plants put into operation no later than 7 January 2014, the higher end of the BAT-AEL range is 55 mg/Nm3."]
["Glass","3. Mineral industry","HTIW wools","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes","Air","Particulates (PM10) (24 hr Mean)","For downstream dusty processes, BAT is to reduce emissions using one or a combination of the following techniques: (i) Minimising the losses of product by ensuring a good sealing of the production line, where technically applicable; (ii) Cutting, trimming and packaging under vacuum, by applying an efficient extraction system in conjunction with a fabric filter; (iii) Applying a fabric filter system","mg/Nm3","1","5","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3","N/A","Daily average (continuous)","BAT-AELs from dusty downstream processes in the HTIW sector, when treated separately\n\nThe lower level of the range is associated with emissions of aluminium silicate glass wool/refractory ceramic fibres",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","CCGT with a net total fuel utilisation of ≥ 75 %","Existing","Natural gas ","50-600 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",35,"55","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period ","These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines\n\nIn the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective.\n\nThese BAT-AELs do not apply to existing turbines for mechanical drive applications or to plants operated < 500 h/yr.\n\nFor plants with a net electrical efficiency (EE) greater than 55 %, a correction factor may be applied to the higher end of the BAT-AEL range, corresponding to [higher end] × EE/55, where EE is the net electrical efficiency of the plant determined at ISO baseload conditions.\n\nFor existing plants put into operation no later than 7 January 2014, the higher end of the BAT-AEL range is 80 mg/Nm3."]
["Glass","3. Mineral industry","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Particulates (PM10) (24 hr Mean)","BAT is to reduce dust emissions from the waste gases of the melting furnace by applying an electrostatic precipitator or a bag filter system","mg/Nm3","10","20","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Coal and/or lignite ","< 100 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Combination of other primary techniques for NOX reduction (e.g. air staging, fuel staging, flue-gas recirculation, low- NOX burners (LNB)); (iii) Selective non- catalytic reduction (SNCR); (iv) Selective catalytic reduction (SCR); (v) Combined techniques for NOX and SOX reduction","mg/Nm3",165,330,"Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ","In the case of coal-fired PC boiler plants put into operation no later than 1 July 1987, which are operated < 1 500 h/yr and for which SCR and/or SNCR is not applicable, the higher end of the range is 340 mg/Nm3.\n\nFor plants operated < 500 h/yr, these levels are indicative."]
["Glass","3. Mineral industry","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Particulates (PM10) (24 hr Mean)","BAT is to reduce dust emissions from the waste gases of the melting furnace by applying an electrostatic precipitator or a bag filter system","kg/tonne melted glass","0.02","0.050","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The conversion factors of 2 × 10 –3 and 2,5 × 10 –3 have been used for the determination of the lower and upper value of the BAT-AELs range (see Table 2), in order to cover both the production of glass wool and stone wool.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Coal and/or lignite ","100-300 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Combination of other primary techniques for NOX reduction (e.g. air staging, fuel staging, flue-gas recirculation, low- NOX burners (LNB)); (iii) Selective non- catalytic reduction (SNCR); (iv) Selective catalytic reduction (SCR); (v) Combined techniques for NOX and SOX reduction","mg/Nm3",155,210,"Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ",0]
["Glass","3. Mineral industry","Special glass ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes","Air","Particulates (PM10) (24 hr Mean)","For downstream dusty processes, BAT is to reduce emissions of dust and metals by using one or a combination of the following techniques: (i) Performing dusty operations (e.g. cutting, grinding, polishing) under liquid; (ii) Applying a bag filter system","mg/Nm3","1","10","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3","N/A","Daily average (continuous)","BAT-AELs for dust and metal emissions from downstream processes in the special glass sector, when treated separately",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Coal and/or lignite ","< 100 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Combination of other primary techniques for NOX reduction (e.g. air staging, fuel staging, flue-gas recirculation, low- NOX burners (LNB)); (iii) Selective non- catalytic reduction (SNCR); (iv) Selective catalytic reduction (SCR); (v) Combined techniques for NOX and SOX reduction","mg/Nm3",100,270,"Green","Continuous ",0,0,0.06,"Yearly","These BAT-AELs do not apply to plants operated < 1 500 h/yr."]
["Glass","3. Mineral industry","Special glass ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Particulates (PM10) (24 hr Mean)","BAT is to reduce dust emissions from the waste gases of the melting furnace by using one or a combination of the following techniques: (i) Reduction of the volatile components by raw material modifications; (ii) Electric melting","mg/Nm3","10","20","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Coal and/or lignite ","100-300 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Combination of other primary techniques for NOX reduction (e.g. air staging, fuel staging, flue-gas recirculation, low- NOX burners (LNB)); (iii) Selective non- catalytic reduction (SNCR); (iv) Selective catalytic reduction (SCR); (v) Combined techniques for NOX and SOX reduction","mg/Nm3",100,180,"Green","Continuous ",0,0,0.06,"Yearly",0]
["Glass","3. Mineral industry","Special glass ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Particulates (PM10) (24 hr Mean)","BAT is to reduce dust emissions from the waste gases of the melting furnace by using one or a combination of the following techniques: (i) Reduction of the volatile components by raw material modifications; (ii) Electric melting","kg/tonne melted glass","0.03","0.13","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The conversions factors of 2,5 × 10 –3 and 6,5 × 10 –3 have been used for the determination of the lower and upper value of the BAT-AELs range (see Table 2), with some values being approximated. However, a-case-by-case conversion factor needs to be applied, depending on the type of glass produced.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Solid biomass and/or peat","≥ 300 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Low-NOX burners (LNB); (iii) Air staging; (iv) Fuel staging, (v) Flue-gas recirculation; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR)","mg/Nm3",40,"150","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ","The higher end of the BAT-AEL range is 160 mg/Nm3 for plants put into operation no later than 7 January 2014."]
["Glass","3. Mineral industry","Special glass ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Particulates (PM10) (24 hr Mean)","BAT is to reduce dust emissions from the waste gases of the melting furnace by using one or a combination of the following techniques: (i) Reduction of the volatile components by raw material modifications; (ii) Electric melting","mg/Nm3","1","10","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The BAT-AELs apply to batch formulations containing significant amounts of constituents meeting the criteria as dangerous substances, in accordance with Regulation (EC) No 1272/2008.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Solid biomass and/or peat","≥ 300 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Low-NOX burners (LNB); (iii) Air staging; (iv) Fuel staging, (v) Flue-gas recirculation; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR)","mg/Nm3",95,"165","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ","The higher end of the BAT-AEL range is 200 mg/Nm3 for plants put into operation no later than 7 January 2014."]
["Glass","3. Mineral industry","Special glass ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Particulates (PM10) (24 hr Mean)","BAT is to reduce dust emissions from the waste gases of the melting furnace by using one or a combination of the following techniques: (i) Reduction of the volatile components by raw material modifications; (ii) Electric melting","kg/tonne melted glass","0.003","0.065","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The BAT-AELs apply to batch formulations containing significant amounts of constituents meeting the criteria as dangerous substances, in accordance with Regulation (EC) No 1272/2008.\n\nThe conversions factors of 2,5 × 10 –3 and 6,5 × 10 –3 have been used for the determination of the lower and upper value of the BAT-AELs range (see Table 2), with some values being approximated. However, a-case-by-case conversion factor needs to be applied, depending on the type of glass produced.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Solid biomass and/or peat","100-300 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Low-NOX burners (LNB); (iii) Air staging; (iv) Fuel staging, (v) Flue-gas recirculation; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR)","mg/Nm3",50,"180","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ",0]
["Glass","3. Mineral industry","Filament glass fibre","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes (forming and coating)","Air","Formaldehyde","BAT is to reduce emissions from downstream processes by using one or a combination of the following techniques: (i) Wet scrubbing systems; (ii) Wet electrostatic precipitator; (iii) Filtration system (bag filter)","mg/Nm3","N/A","10","Amber",0,"273.15","101.3","N/A","Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Solid biomass and/or peat","100-300 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Low-NOX burners (LNB); (iii) Air staging; (iv) Fuel staging, (v) Flue-gas recirculation; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR)","mg/Nm3",100,"220","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ",0]
["Glass","3. Mineral industry","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes- Curing oven emissions ","Air","Formaldehyde","BAT is to reduce emissions from downstream processes by using one or a combination of the following techniques: (i) Impact jets and cyclones; (ii) Wet scrubbers; (iii) Wet electrostatic precipitators; (iv) Stone wool filters; (v) Waste gas incineration","mg/Nm3","2","5","Amber",0,"273.15","101.3","N/A","Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Solid biomass and/or peat","50-100 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Low-NOX burners (LNB); (iii) Air staging; (iv) Fuel staging, (v) Flue-gas recirculation; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR)","mg/Nm3",70,"225","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ","For plants burning fuels where the average potassium content is 2 000 mg/kg (dry) or higher, and/or the average sodium content is 300 mg/kg or higher, the higher end of the BAT-AEL range is 250 mg/Nm3."]
["Glass","3. Mineral industry","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes- Curing oven emissions ","Air","Formaldehyde","BAT is to reduce emissions from downstream processes by using one or a combination of the following techniques: (i) Impact jets and cyclones; (ii) Wet scrubbers; (iii) Wet electrostatic precipitators; (iv) Stone wool filters; (v) Waste gas incineration","kg/tonne melted glass","N/A","0.03","Amber",0,"273.15","101.3","N/A","Daily average (continuous)","The specific mass emissions refer to 1 tonne of produced glass",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Solid biomass and/or peat","50-100 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Low-NOX burners (LNB); (iii) Air staging; (iv) Fuel staging, (v) Flue-gas recirculation; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR)","mg/Nm3",120,"275","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ","For plants put into operation no later than 7 January 2014 and burning fuels where the average potassium content is 2 000 mg/kg (dry) or higher, and/or the average sodium content is 300 mg/kg or higher, the higher end of the BAT-AEL range is 310 mg/Nm3."]
["Glass","3. Mineral industry","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes- Forming area ","Air","Formaldehyde","BAT is to reduce emissions from downstream processes by using one or a combination of the following techniques: (i) Impact jets and cyclones; (ii) Wet scrubbers; (iii) Wet electrostatic precipitators; (iv) Stone wool filters; (v) Waste gas incineration","mg/Nm3","2","5","Amber",0,"273.15","101.3","N/A","Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","New","Coal and/or lignite ","< 100 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Combination of other primary techniques for NOX reduction (e.g. air staging, fuel staging, flue-gas recirculation, low- NOX burners (LNB)); (iii) Selective non- catalytic reduction (SNCR); (iv) Selective catalytic reduction (SCR); (v) Combined techniques for NOX and SOX reduction","mg/Nm3",100,150,"Green","Continuous ",0,0,0.06,"Yearly",0]
["Glass","3. Mineral industry","Container glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes","Air","Hydrogen chloride","When tin, organotin or titanium compounds are used for hot-end coating operations, BAT is to reduce emissions by using one or a combination of the following techniques: (i) Minimising the losses of the coating product by ensuring a good sealing of the application system and applying an effective extracting hood; (ii) Combining the flue-gas from the coating operations with the waste gas from the melting furnace or with the combustion air of the furnace, when a secondary treatment system is applied (filter and dry or semi-dry scrubber); (iii) Applying a secondary technique, e.g. wet scrubbing, dry scrubbing plus filtration","mg/Nm3","N/A",30,"Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3","N/A","Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","New","Coal and/or lignite ","< 100 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Combination of other primary techniques for NOX reduction (e.g. air staging, fuel staging, flue-gas recirculation, low- NOX burners (LNB)); (iii) Selective non- catalytic reduction (SNCR); (iv) Selective catalytic reduction (SCR); (v) Combined techniques for NOX and SOX reduction","mg/Nm3",155,200,"Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ",0]
["Glass","3. Mineral industry","Container glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Hydrogen chloride","BAT is to reduce HCl and HF emissions from the melting furnace (possibly combined with flue-gases from hot-end coating activities) by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of chlorine and fluorine; (ii) Dry or semi-dry scrubbing, in a combination with filtration system","mg/Nm3","10","20","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The higher levels are associated with the simultaneous treatment of flue-gases from hot-end coating operations.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","New","Coal and/or lignite ","100-300 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Combination of other primary techniques for NOX reduction (e.g. air staging, fuel staging, flue-gas recirculation, low- NOX burners (LNB)); (iii) Selective non- catalytic reduction (SNCR); (iv) Selective catalytic reduction (SCR); (v) Combined techniques for NOX and SOX reduction","mg/Nm3",50,100,"Green","Continuous ",0,0,0.06,"Yearly",0]
["Glass","3. Mineral industry","Container glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Hydrogen chloride","BAT is to reduce HCl and HF emissions from the melting furnace (possibly combined with flue-gases from hot-end coating activities) by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of chlorine and fluorine; (ii) Dry or semi-dry scrubbing, in a combination with filtration system","kg/tonne melted glass","0.02","0.03","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The higher levels are associated with the simultaneous treatment of flue-gases from hot-end coating operations.\n\nThe conversion factor for general cases, reported in Table 2 (1,5 × 10 –3 ) has been applied",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","New","Coal and/or lignite ","100-300 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Combination of other primary techniques for NOX reduction (e.g. air staging, fuel staging, flue-gas recirculation, low- NOX burners (LNB)); (iii) Selective non- catalytic reduction (SNCR); (iv) Selective catalytic reduction (SCR); (v) Combined techniques for NOX and SOX reduction","mg/Nm3",80,130,"Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ",0]
["Glass","3. Mineral industry","Domestic glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Hydrogen chloride","BAT is to reduce HCl and HF emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of chlorine and fluorine; (ii) Minimisation of the flourine content in the batch formulation and optimisation of the flourine mass balance; (iii) Dry or semi-dry scrubbing, in combination with a filtration system; (iv) Wet scrubbing ","mg/Nm3","10","20","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The lower levels are associated with the use of electric melting.\n\nIn cases where KCl or NaCl are used as a refining agents, the BAT-AEL is < 30 mg/Nm 3 or < 0,09 kg/tonne melted glass.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","New","Solid biomass and/or peat","≥ 300 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Low-NOX burners (LNB); (iii) Air staging; (iv) Fuel staging, (v) Flue-gas recirculation; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR)","mg/Nm3",40,"140","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ",0]
["Glass","3. Mineral industry","Domestic glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Hydrogen chloride","BAT is to reduce HCl and HF emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of chlorine and fluorine; (ii) Minimisation of the flourine content in the batch formulation and optimisation of the flourine mass balance; (iii) Dry or semi-dry scrubbing, in combination with a filtration system; (iv) Wet scrubbing ","kg/tonne melted glass","0.03","0.06","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The lower levels are associated with the use of electric melting.\n\nIn cases where KCl or NaCl are used as a refining agents, the BAT-AEL is < 30 mg/Nm 3 or < 0,09 kg/tonne melted glass.\n\nA conversion factor of 3 × 10 –3 has been applied (see Table 2). However, a case-by-case conversion factor may have to be applied for specific productions.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","New","Solid biomass and/or peat","≥ 300 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Low-NOX burners (LNB); (iii) Air staging; (iv) Fuel staging, (v) Flue-gas recirculation; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR)","mg/Nm3",65,"150","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ",0]
["Glass","3. Mineral industry","Filament glass fibre","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Hydrogen chloride","BAT is to reduce HCl and HF emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of chlorine and flourine; (ii) Minimisation of the flourine content in the batch formulation ","mg/Nm3","N/A","10","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","New","Solid biomass and/or peat","100-300 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Low-NOX burners (LNB); (iii) Air staging; (iv) Fuel staging, (v) Flue-gas recirculation; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR)","mg/Nm3",50,"140","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ",0]
["Glass","3. Mineral industry","Filament glass fibre","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Hydrogen chloride","BAT is to reduce HCl and HF emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of chlorine and flourine; (ii) Minimisation of the flourine content in the batch formulation ","kg/tonne melted glass","N/A","0.05","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The conversion factor reported in Table 2 (4,5 × 10 –3 ) has been applied.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","New","Solid biomass and/or peat","100-300 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Low-NOX burners (LNB); (iii) Air staging; (iv) Fuel staging, (v) Flue-gas recirculation; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR)","mg/Nm3",100,"200","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ",0]
["Glass","3. Mineral industry","Flat glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes","Air","Hydrogen chloride","BAT is to reduce emissions to air from the downstream processes by using one or a combination of the following techniques: (i) Minimising the losses of coating products applied to the flat glass by ensuring a good sealing of the application system; (ii) Minimising the losses of SO2 from the annealing ler, by operating the control system in an optimum manner; (iii) Combining the SO2 emissions from the lehr with the waste fas from the melting furnace, when technically feasible and where a secondary treatment system is applied (filter and dry or semi-dry scrubber); (iv) Applying a secondary technique, e.g. wet scrubbing, or dry scrubbing and filtration","mg/Nm3","N/A","10","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3","N/A","Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","New","Solid biomass and/or peat","50-100 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Low-NOX burners (LNB); (iii) Air staging; (iv) Fuel staging, (v) Flue-gas recirculation; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR)","mg/Nm3",70,"150","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ","For plants burning fuels where the average potassium content is 2 000 mg/kg (dry) or higher, and/or the average sodium content is 300 mg/kg or higher, the higher end of the BAT-AEL range is 200 mg/Nm3."]
["Glass","3. Mineral industry","Flat glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Hydrogen chloride","BAT is to reduce HCl and HF emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of chlorine and flourine; (ii) Dry or semi-dry scrubbing in combination with a filtration system ","mg/Nm3","10","25","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The higher levels of the range are associated with the recycling of filter dust in the batch formulation",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","New","Solid biomass and/or peat","50-100 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Low-NOX burners (LNB); (iii) Air staging; (iv) Fuel staging, (v) Flue-gas recirculation; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR)","mg/Nm3",120,"200","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ","For plants burning fuels where the average potassium content is 2 000 mg/kg (dry) or higher, and/or the average sodium content is 300 mg/kg or higher, the higher end of the BAT-AEL range is 260 mg/Nm3."]
["Glass","3. Mineral industry","Flat glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Hydrogen chloride","BAT is to reduce HCl and HF emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of chlorine and flourine; (ii) Dry or semi-dry scrubbing in combination with a filtration system ","kg/tonne melted glass","0.025","0.0625","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The conversion factor reported in Table 2 (2,5 × 10 –3 ) has been applied.\n\nThe higher levels of the range are associated with the recycling of filter dust in the batch formulation",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Existing","100% iron and steel process gases ","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of iron and steel process gases in CCGTs, BAT is to use one or a combination of the techniques given below: (i) Process gas management system; (ii) Advanced control system; (iii) Water/steam addition; (iv) Dry low-NOX burners(DLN); (v) Low-NOX burners (LNB); (vi) Selective catalytic reduction (SCR)","mg/Nm3",20,"100","Green","Continuous ",0,0,0.03,"Yearly","Plants combusting a mixture of gases with an equivalent LHV of > 20 MJ/Nm3 are expected to emit at the higher end of the BAT-AEL ranges.\n\nThe lower end of the BAT-AEL range can be achieved when using SCR.\n\nFor plants operated < 1 500 h/yr, these BAT AELs do not apply."]
["Glass","3. Mineral industry","Frits ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Hydrogen chloride","BAT is to reduce HCl and HF emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of chlorine and fluorine; (ii) Minimisation of the fluorine compounds in the batch formulation when used to ensure the quality of the final product; (iii) Dry or semi-dry scrubbing, in combination with a filtration system","mg/Nm3","N/A","10","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Existing","100% iron and steel process gases ","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of iron and steel process gases in CCGTs, BAT is to use one or a combination of the techniques given below: (i) Process gas management system; (ii) Advanced control system; (iii) Water/steam addition; (iv) Dry low-NOX burners(DLN); (v) Low-NOX burners (LNB); (vi) Selective catalytic reduction (SCR)","mg/Nm3",22,"110","Green","Continuous ",0,0,0.03,"Daily average or average over sampling period ","Plants combusting a mixture of gases with an equivalent LHV of > 20 MJ/Nm3 are expected to emit at the higher end of the BAT-AEL ranges.\n\nThe lower end of the BAT-AEL range can be achieved when using SCR.\n\nIn the case of plants put into operation no later than 7 January 2014, the higher end of the BAT-AEL range is 160 mg/Nm3. Furthermore, the higher end of the BAT-AEL range may be exceeded when SCR cannot be used and when using a high share of COG (e.g. > 50 %) and/or when combusting COG with a relatively high level of H2. In this case, the higher end of the BAT-AEL range is 220 mg/Nm3.\n\nFor plants operated < 500 h/yr, these levels are indicative."]
["Glass","3. Mineral industry","Frits ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Hydrogen chloride","BAT is to reduce HCl and HF emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of chlorine and fluorine; (ii) Minimisation of the fluorine compounds in the batch formulation when used to ensure the quality of the final product; (iii) Dry or semi-dry scrubbing, in combination with a filtration system","kg/tonne melted glass","N/A","0.05","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The conversion factor of 5 × 10 –3 has been used with some values being approximated. A case-by-case conversion factor may have to be applied based on the type of combustion",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","New","100% iron and steel process gases ","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of iron and steel process gases in CCGTs, BAT is to use one or a combination of the techniques given below: (i) Process gas management system; (ii) Advanced control system; (iii) Water/steam addition; (iv) Dry low-NOX burners(DLN); (v) Low-NOX burners (LNB); (vi) Selective catalytic reduction (SCR)","mg/Nm3",15,"65","Green","Continuous ",0,0,0.03,"Yearly","Plants combusting a mixture of gases with an equivalent LHV of > 20 MJ/Nm3 are expected to emit at the higher end of the BAT-AEL ranges."]
["Glass","3. Mineral industry","HTIW wools","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Hydrogen chloride","BAT is to reduce SO X emissions from the melting furnaces and downstream processes by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of sulphur; (ii) Use of low sulphur content fuel","mg/Nm3","N/A","10","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","New","100% iron and steel process gases ","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of iron and steel process gases in CCGTs, BAT is to use one or a combination of the techniques given below: (i) Process gas management system; (ii) Advanced control system; (iii) Water/steam addition; (iv) Dry low-NOX burners(DLN); (v) Low-NOX burners (LNB); (vi) Selective catalytic reduction (SCR)","mg/Nm3",22,"100","Green","Continuous ",0,0,0.03,"Daily average or average over sampling period ","Plants combusting a mixture of gases with an equivalent LHV of > 20 MJ/Nm3 are expected to emit at the higher end of the BAT-AEL ranges."]
["Glass","3. Mineral industry","Mineral wool","Glass wool ","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Hydrogen chloride","BAT is to reduce HCl and HF emissions from the melting furnace by using one or a combination of the following techniques:(i) Selection of raw materials for the batch formulation with a low content of chlorine and fluorine; (ii) Dry or semi-dry scrubbing, in combination with a filtration system","mg/Nm3","5","10","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Existing","Gases only ","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO emissions to air from the combustion of process fuels from the chemical industry, BAT is to use one or a combination of the techniques given below: (i) Low-NOX burners (LNB); (ii) Air staging; (iii) Fuel staging; (iv) Flue-gas recirculation; (v) Water/steam addition; (vi) Fuel choice; (vii) Advanced control system; (viii) Selective non-catalytic reduction (SNCR); (ix) Selective catalytic reduction (SCR)","mg/Nm3",70,"100","Green","Continuous ",0,0,0.03,"Yearly","For plants operated < 1 500 h/yr, these BAT AELs do not apply.  \n\nFor existing plants put into operation no later than 7 January 2014, the higher end of the BAT-AEL range is 180 mg/Nm3."]
["Glass","3. Mineral industry","Mineral wool","Glass wool ","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Hydrogen chloride","BAT is to reduce HCl and HF emissions from the melting furnace by using one or a combination of the following techniques:(i) Selection of raw materials for the batch formulation with a low content of chlorine and fluorine; (ii) Dry or semi-dry scrubbing, in combination with a filtration system","kg/tonne melted glass","0.01","0.02","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The conversion factors of 2 × 10 –3 for glass wool and 2,5 × 10 –3 for stone wool have been used (",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Existing","Gases only ","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO emissions to air from the combustion of process fuels from the chemical industry, BAT is to use one or a combination of the techniques given below: (i) Low-NOX burners (LNB); (ii) Air staging; (iii) Fuel staging; (iv) Flue-gas recirculation; (v) Water/steam addition; (vi) Fuel choice; (vii) Advanced control system; (viii) Selective non-catalytic reduction (SNCR); (ix) Selective catalytic reduction (SCR)","mg/Nm3",85,"110","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ","For plants operated < 500 h/yr, these levels are indicative.\n\nFor existing plants put into operation no later than 7 January 2014, the higher end of the BAT-AEL range is 210 mg/Nm3."]
["Glass","3. Mineral industry","Mineral wool","Stone wool","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Hydrogen chloride","BAT is to reduce HCl and HF emissions from the melting furnace by using one or a combination of the following techniques:(i) Selection of raw materials for the batch formulation with a low content of chlorine and fluorine; (ii) Dry or semi-dry scrubbing, in combination with a filtration system","mg/Nm3","10","30","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Existing","HFO and/or gas oil in boilers","< 100 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Air staging; (ii) Fuel staging; (iii) Flue-gas recirculation; (iv) Low-NOX burners (LNB); (v) Water/steam addition; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR); (viii) Advanced control systeml (ix) Fuel choice","mg/Nm3",150,"270","Green","Continuous ",0,0,0.03,"Yearly","These BAT-AELs do not apply to plants operated < 1 500 h/yr."]
["Glass","3. Mineral industry","Mineral wool","Stone wool","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Hydrogen chloride","BAT is to reduce HCl and HF emissions from the melting furnace by using one or a combination of the following techniques:(i) Selection of raw materials for the batch formulation with a low content of chlorine and fluorine; (ii) Dry or semi-dry scrubbing, in combination with a filtration system","kg/tonne melted glass","0.025","0.075","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The conversion factors of 2 × 10 –3 for glass wool and 2,5 × 10 –3 for stone wool have been used",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Existing","HFO and/or gas oil in boilers","< 100 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Air staging; (ii) Fuel staging; (iii) Flue-gas recirculation; (iv) Low-NOX burners (LNB); (v) Water/steam addition; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR); (viii) Advanced control systeml (ix) Fuel choice","mg/Nm3",210,"330","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ","For plants operated < 500 h/yr, these levels are indicative.\n\nFor industrial boilers and district heating plants put into operation no later than 27 November 2003, which are operated < 1 500 h/yr and for which SCR and/or SNCR is not applicable, the higher end of the BAT-AEL range is 450 mg/Nm3."]
["Glass","3. Mineral industry","Special glass ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Hydrogen chloride","BAT is to reduce HCl and HF emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of chlorine and fluorine; (ii) Minimisation of the fluorine and/or chlorine compounds in the batch formulation and optimisation of the fluorine and/or chlorine mass balance; (iii) Dry or semi-dry scrubbing, in combination with a filtration system","mg/Nm3","10","20","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The higher levels are associated with the use of materials containing chlorine in the batch formulation.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Existing","HFO and/or gas oil in boilers","≥ 100 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Air staging; (ii) Fuel staging; (iii) Flue-gas recirculation; (iv) Low-NOX burners (LNB); (v) Water/steam addition; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR); (viii) Advanced control systeml (ix) Fuel choice","mg/Nm3",45,"100","Green","Continuous ",0,0,0.03,"Yearly","The higher end of the BAT-AEL range is 110 mg/Nm3 for plants of 100–300 MWth and plants of ≥ 300 MWth that were put into operation no later than 7 January 2014."]
["Glass","3. Mineral industry","Special glass ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Hydrogen chloride","BAT is to reduce HCl and HF emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of chlorine and fluorine; (ii) Minimisation of the fluorine and/or chlorine compounds in the batch formulation and optimisation of the fluorine and/or chlorine mass balance; (iii) Dry or semi-dry scrubbing, in combination with a filtration system","kg/tonne melted glass","0.03","0.05","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The higher levels are associated with the use of materials containing chlorine in the batch formulation.\n\nThe conversion factor of 2,5 × 10 –3 (see Table 2) has been used; with some values being approximated. A case-by-case conversion factor may have to be applied based on the type of production.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Existing","HFO and/or gas oil in boilers","≥ 100 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Air staging; (ii) Fuel staging; (iii) Flue-gas recirculation; (iv) Low-NOX burners (LNB); (v) Water/steam addition; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR); (viii) Advanced control systeml (ix) Fuel choice","mg/Nm3",85,"110","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ","For industrial boilers and district heating plants of > 100 MWth put into operation no later than 27 November 2003, which are operated < 1 500 h/yr and for which SCR and/or SNCR is not applicable, the higher end of the BAT-AEL range is 365 mg/Nm3."]
["Glass","3. Mineral industry","Domestic glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Acid polishing processes","Air","Hydrogen fluoride (as F) (Ecological - Daily Mean)","For acid polishing processes, BAT is to reduce HF emissions by using one or a combination of the following techniques: (i) Minimising the losses of polishing product by ensuring a good sealing of the application system; (ii) Applying a secondary technique, e.g. wet scrubbing","mg/Nm3","N/A","5","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3","N/A","Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Existing","Mixture of gases and liquids","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO emissions to air from the combustion of process fuels from the chemical industry, BAT is to use one or a combination of the techniques given below: (i) Low-NOX burners (LNB); (ii) Air staging; (iii) Fuel staging; (iv) Flue-gas recirculation; (v) Water/steam addition; (vi) Fuel choice; (vii) Advanced control system; (viii) Selective non-catalytic reduction (SNCR); (ix) Selective catalytic reduction (SCR)","mg/Nm3",80,"290","Green","Continuous ",0,0,0.03,"Yearly","For plants operated < 1 500 h/yr, these BAT AELs do not apply.\n\nFor existing plants of ≤ 500 MWth put into operation no later than 27 November 2003 using liquid fuels with a nitrogen content higher than 0,6 wt-%, the higher end of the BAT-AEL range is 380 mg/Nm3."]
["Glass","3. Mineral industry","Domestic glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Hydrogen fluoride (as F) (Ecological - Daily Mean)","BAT is to reduce HCl and HF emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of chlorine and fluorine; (ii) Minimisation of the flourine content in the batch formulation and optimisation of the flourine mass balance; (iii) Dry or semi-dry scrubbing, in combination with a filtration system; (iv) Wet scrubbing ","mg/Nm3","1","5","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The lower levels are associated with the use of electric melting. The higher levels are associated with the production of opal glass, the recycling of filter dust or where high levels of external cullet are used in the batch formulation.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Existing","Mixture of gases and liquids","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO emissions to air from the combustion of process fuels from the chemical industry, BAT is to use one or a combination of the techniques given below: (i) Low-NOX burners (LNB); (ii) Air staging; (iii) Fuel staging; (iv) Flue-gas recirculation; (v) Water/steam addition; (vi) Fuel choice; (vii) Advanced control system; (viii) Selective non-catalytic reduction (SNCR); (ix) Selective catalytic reduction (SCR)","mg/Nm3",100,"330","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ","For plants operated < 500 h/yr, these levels are indicative. \n\nFor existing plants of ≤ 500 MWth put into operation no later than 27 November 2003 using liquid fuels with a nitrogen content higher than 0,6 wt-%, the higher end of the BAT-AEL range is 380 mg/Nm3."]
["Glass","3. Mineral industry","Domestic glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Hydrogen fluoride (as F) (Ecological - Daily Mean)","BAT is to reduce HCl and HF emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of chlorine and fluorine; (ii) Minimisation of the flourine content in the batch formulation and optimisation of the flourine mass balance; (iii) Dry or semi-dry scrubbing, in combination with a filtration system; (iv) Wet scrubbing ","kg/tonne melted glass","0.003","0.015","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The lower levels are associated with the use of electric melting. The higher levels are associated with the production of opal glass, the recycling of filter dust or where high levels of external cullet are used in the batch formulation.\n\nA conversion factor of 3 × 10 –3 has been applied (see Table 2). However, a case-by-case conversion factor may have to be applied for specific productions.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Existing","Natural gas ","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",50,"100","Green","Continuous ",0,0,0.15,"Yearly","Optimising the functioning of an existing technique to reduce NOX emissions further may lead to levels of CO emissions at the higher end of the indicative range for CO emissions given after this table.\n\nThese BAT-AELs do not apply to plants operated < 1 500 h/yr."]
["Glass","3. Mineral industry","Filament glass fibre","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Hydrogen fluoride (as F) (Ecological - Daily Mean)","BAT is to reduce HCl and HF emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of chlorine and flourine; (ii) Minimisation of the flourine content in the batch formulation ","mg/Nm3","5","15","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The higher levels of the range are associated with the use of fluorine compounds in the batch formulation.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Existing","Natural gas ","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",85,"110","Green","Continuous ",0,0,0.15,"Daily average or average over sampling period ","For plants operated < 500 h/yr, these levels are indicative."]
["Glass","3. Mineral industry","Filament glass fibre","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Hydrogen fluoride (as F) (Ecological - Daily Mean)","BAT is to reduce HCl and HF emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of chlorine and flourine; (ii) Minimisation of the flourine content in the batch formulation ","kg/tonne melted glass","0.02","0.07","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The conversion factor reported in Table 2 (4,5 × 10 –3 ) has been applied.\n\nThe higher levels of the range are associated with the use of fluorine compounds in the batch formulation.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","New","Gases only ","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO emissions to air from the combustion of process fuels from the chemical industry, BAT is to use one or a combination of the techniques given below: (i) Low-NOX burners (LNB); (ii) Air staging; (iii) Fuel staging; (iv) Flue-gas recirculation; (v) Water/steam addition; (vi) Fuel choice; (vii) Advanced control system; (viii) Selective non-catalytic reduction (SNCR); (ix) Selective catalytic reduction (SCR)","mg/Nm3",20,"80","Green","Continuous ",0,0,0.03,"Yearly",0]
["Glass","3. Mineral industry","Flat glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes","Air","Hydrogen fluoride (as F) (Ecological - Daily Mean)","BAT is to reduce emissions to air from the downstream processes by using one or a combination of the following techniques: (i) Minimising the losses of coating products applied to the flat glass by ensuring a good sealing of the application system; (ii) Minimising the losses of SO2 from the annealing ler, by operating the control system in an optimum manner; (iii) Combining the SO2 emissions from the lehr with the waste fas from the melting furnace, when technically feasible and where a secondary treatment system is applied (filter and dry or semi-dry scrubber); (iv) Applying a secondary technique, e.g. wet scrubbing, or dry scrubbing and filtration","mg/Nm3","1","5","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3","N/A","Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","New","Gases only ","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO emissions to air from the combustion of process fuels from the chemical industry, BAT is to use one or a combination of the techniques given below: (i) Low-NOX burners (LNB); (ii) Air staging; (iii) Fuel staging; (iv) Flue-gas recirculation; (v) Water/steam addition; (vi) Fuel choice; (vii) Advanced control system; (viii) Selective non-catalytic reduction (SNCR); (ix) Selective catalytic reduction (SCR)","mg/Nm3",30,"100","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ",0]
["Glass","3. Mineral industry","Flat glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Hydrogen fluoride (as F) (Ecological - Daily Mean)","BAT is to reduce HCl and HF emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of chlorine and flourine; (ii) Dry or semi-dry scrubbing in combination with a filtration system ","mg/Nm3","1","4","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","New","HFO and/or gas oil in boilers","< 100 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Air staging; (ii) Fuel staging; (iii) Flue-gas recirculation; (iv) Low-NOX burners (LNB); (v) Water/steam addition; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR); (viii) Advanced control systeml (ix) Fuel choice","mg/Nm3",75,"200","Green","Continuous ",0,0,0.03,"Yearly",0]
["Glass","3. Mineral industry","Flat glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Hydrogen fluoride (as F) (Ecological - Daily Mean)","BAT is to reduce HCl and HF emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of chlorine and flourine; (ii) Dry or semi-dry scrubbing in combination with a filtration system ","kg/tonne melted glass","0.0025","0.010","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The conversion factor reported in Table 2 (2,5 × 10 –3 ) has been applied.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","New","HFO and/or gas oil in boilers","≥ 100 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Air staging; (ii) Fuel staging; (iii) Flue-gas recirculation; (iv) Low-NOX burners (LNB); (v) Water/steam addition; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR); (viii) Advanced control systeml (ix) Fuel choice","mg/Nm3",45,"75","Green","Continuous ",0,0,0.03,"Yearly",0]
["Glass","3. Mineral industry","Frits ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Hydrogen fluoride (as F) (Ecological - Daily Mean)","BAT is to reduce HCl and HF emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of chlorine and fluorine; (ii) Minimisation of the fluorine compounds in the batch formulation when used to ensure the quality of the final product; (iii) Dry or semi-dry scrubbing, in combination with a filtration system","mg/Nm3","N/A","5","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","New","Mixture of gases and liquids","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO emissions to air from the combustion of process fuels from the chemical industry, BAT is to use one or a combination of the techniques given below: (i) Low-NOX burners (LNB); (ii) Air staging; (iii) Fuel staging; (iv) Flue-gas recirculation; (v) Water/steam addition; (vi) Fuel choice; (vii) Advanced control system; (viii) Selective non-catalytic reduction (SNCR); (ix) Selective catalytic reduction (SCR)","mg/Nm3",30,"85","Green","Continuous ",0,0,0.03,"Yearly",0]
["Glass","3. Mineral industry","Frits ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Hydrogen fluoride (as F) (Ecological - Daily Mean)","BAT is to reduce HCl and HF emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of chlorine and fluorine; (ii) Minimisation of the fluorine compounds in the batch formulation when used to ensure the quality of the final product; (iii) Dry or semi-dry scrubbing, in combination with a filtration system","kg/tonne melted glass","N/A","0.03","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The conversion factor of 5 × 10 –3 has been used with some values being approximated. A case-by-case conversion factor may have to be applied based on the type of combustion",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","New","Mixture of gases and liquids","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO emissions to air from the combustion of process fuels from the chemical industry, BAT is to use one or a combination of the techniques given below: (i) Low-NOX burners (LNB); (ii) Air staging; (iii) Fuel staging; (iv) Flue-gas recirculation; (v) Water/steam addition; (vi) Fuel choice; (vii) Advanced control system; (viii) Selective non-catalytic reduction (SNCR); (ix) Selective catalytic reduction (SCR)","mg/Nm3",50,"110","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ",0]
["Glass","3. Mineral industry","HTIW wools","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Hydrogen fluoride (as F) (Ecological - Daily Mean)","BAT is to reduce SO X emissions from the melting furnaces and downstream processes by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of sulphur; (ii) Use of low sulphur content fuel","mg/Nm3","N/A","5","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","New","Natural gas ","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",10,"60","Green","Continuous ",0,0,0.15,"Yearly","Optimising the functioning of an existing technique to reduce NOX emissions further may lead to levels of CO emissions at the higher end of the indicative range for CO emissions given after this table."]
["Glass","3. Mineral industry","Mineral wool","All products","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Hydrogen fluoride (as F) (Ecological - Daily Mean)","BAT is to reduce HCl and HF emissions from the melting furnace by using one or a combination of the following techniques:(i) Selection of raw materials for the batch formulation with a low content of chlorine and fluorine; (ii) Dry or semi-dry scrubbing, in combination with a filtration system","kg/tonne melted glass","0.002","0.013","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The conversion factors of 2 × 10 –3 and 2,5 × 10 –3 have been used for the determination of the lower and upper values of the BAT-AELs range\n\nThe conversion factors of 2 × 10 –3 for glass wool and 2,5 × 10 –3 for stone wool have been used",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","New","Natural gas ","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",30,"85","Green","Continuous ",0,0,0.15,"Daily average or average over sampling period ",0]
["Glass","3. Mineral industry","Mineral wool","Glass wool ","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Hydrogen fluoride (as F) (Ecological - Daily Mean)","BAT is to reduce HCl and HF emissions from the melting furnace by using one or a combination of the following techniques:(i) Selection of raw materials for the batch formulation with a low content of chlorine and fluorine; (ii) Dry or semi-dry scrubbing, in combination with a filtration system","mg/Nm3","1","5","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","New","HFO and/or gas oil in boilers","< 100 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Air staging; (ii) Fuel staging; (iii) Flue-gas recirculation; (iv) Low-NOX burners (LNB); (v) Water/steam addition; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR); (viii) Advanced control systeml (ix) Fuel choice","mg/Nm3",100,"215","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ",0]
["Glass","3. Mineral industry","Special glass ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Acid polishing processes","Air","Hydrogen fluoride (as F) (Ecological - Daily Mean)","For acid polishing processes, BAT is to reduce HF emissions by using one or a combination of the following techniques: (i) Minimising the losses of polishing product by ensuring a good sealing of the application system; (ii) Applying a secondary technique, e.g. wet scrubbing","mg/Nm3","N/A","5","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3","N/A","Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","New","HFO and/or gas oil in boilers","≥ 100 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Air staging; (ii) Fuel staging; (iii) Flue-gas recirculation; (iv) Low-NOX burners (LNB); (v) Water/steam addition; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR); (viii) Advanced control systeml (ix) Fuel choice","mg/Nm3",85,"100","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ","The higher end of the BAT-AEL range is 145 mg/Nm3 for plants of 100–300 MWth and plants of ≥ 300 MWth that were put into operation no later than 7 January 2014."]
["Glass","3. Mineral industry","Special glass ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Hydrogen fluoride (as F) (Ecological - Daily Mean)","BAT is to reduce HCl and HF emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of chlorine and fluorine; (ii) Minimisation of the fluorine and/or chlorine compounds in the batch formulation and optimisation of the fluorine and/or chlorine mass balance; (iii) Dry or semi-dry scrubbing, in combination with a filtration system","mg/Nm3","1","5","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","CCGT","Existing","100% iron and steel process gases ","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of iron and steel process gases in CCGTs, BAT is to use one or a combination of the techniques given below: (i) Process gas management system; (ii) Advanced control system; (iii) Water/steam addition; (iv) Dry low-NOX burners(DLN); (v) Low-NOX burners (LNB); (vi) Selective catalytic reduction (SCR)","mg/Nm3",20,"50","Green","Continuous ",0,0,0.15,"Yearly","Plants combusting a mixture of gases with an equivalent LHV of > 20 MJ/Nm3 are expected to emit at the higher end of the BAT-AEL ranges.\n\nThe lower end of the BAT-AEL range can be achieved when using SCR.\n\nFor plants operated < 1 500 h/yr, these BAT AELs do not apply."]
["Glass","3. Mineral industry","Special glass ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Hydrogen fluoride (as F) (Ecological - Daily Mean)","BAT is to reduce HCl and HF emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of chlorine and fluorine; (ii) Minimisation of the fluorine and/or chlorine compounds in the batch formulation and optimisation of the fluorine and/or chlorine mass balance; (iii) Dry or semi-dry scrubbing, in combination with a filtration system","kg/tonne melted glass","0.003","0.04","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The upper value of the range has been derived from specific reported data.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","CCGT","Existing","100% iron and steel process gases ","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of iron and steel process gases in CCGTs, BAT is to use one or a combination of the techniques given below: (i) Process gas management system; (ii) Advanced control system; (iii) Water/steam addition; (iv) Dry low-NOX burners(DLN); (v) Low-NOX burners (LNB); (vi) Selective catalytic reduction (SCR)","mg/Nm3",30,"55","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period ","Plants combusting a mixture of gases with an equivalent LHV of > 20 MJ/Nm3 are expected to emit at the higher end of the BAT-AEL ranges.\n\nFor plants operated < 500 h/yr, these levels are indicative.\n\nIn the case of plants put into operation no later than 7 January 2014, the higher end of the BAT-AEL range is 70 mg/Nm3."]
["Glass","3. Mineral industry","Container glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Hydrogen fluoride (as F) (Ecological - Daily Mean)","BAT is to reduce HCl and HF emissions from the melting furnace (possibly combined with flue-gases from hot-end coating activities) by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of chlorine and fluorine; (ii) Dry or semi-dry scrubbing, in a combination with filtration system","mg/Nm3","1","5","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","CCGT","New","100% iron and steel process gases ","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of iron and steel process gases in CCGTs, BAT is to use one or a combination of the techniques given below: (i) Process gas management system; (ii) Advanced control system; (iii) Water/steam addition; (iv) Dry low-NOX burners(DLN); (v) Low-NOX burners (LNB); (vi) Selective catalytic reduction (SCR)","mg/Nm3",20,"35","Green","Continuous ",0,0,0.15,"Yearly","Plants combusting a mixture of gases with an equivalent LHV of > 20 MJ/Nm3 are expected to emit at the higher end of the BAT-AEL ranges."]
["Glass","3. Mineral industry","Container glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Hydrogen fluoride (as F) (Ecological - Daily Mean)","BAT is to reduce HCl and HF emissions from the melting furnace (possibly combined with flue-gases from hot-end coating activities) by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of chlorine and fluorine; (ii) Dry or semi-dry scrubbing, in a combination with filtration system","kg/tonne melted glass","0.001","0.008","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The conversion factor for general cases, reported in Table 2 (1,5 × 10 –3 ) has been applied.\n\nThe higher levels are associated with the simultaneous treatment of flue-gases from hot-end coating operations",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","CCGT","New","100% iron and steel process gases ","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of iron and steel process gases in CCGTs, BAT is to use one or a combination of the techniques given below: (i) Process gas management system; (ii) Advanced control system; (iii) Water/steam addition; (iv) Dry low-NOX burners(DLN); (v) Low-NOX burners (LNB); (vi) Selective catalytic reduction (SCR)","mg/Nm3",30,"50","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period ","Plants combusting a mixture of gases with an equivalent LHV of > 20 MJ/Nm3 are expected to emit at the higher end of the BAT-AEL ranges."]
["Glass","3. Mineral industry","Mineral wool","Stone wool","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Hydrogen sulphide","BAT is to reduce H 2 S emissions from the melting furnace by applying a waste gas incineration system to oxidise hydrogen sulphide to SO 2","mg/Nm3","N/A","2","Amber",0,"273.15","101.3",0.08,"Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","CCGT","New","Natural gas ","≥ 50 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",10,"30","Green","Continuous ",0,0,0.15,"Yearly","These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines\n\nIn the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective.\n\nThese BAT-AELs do not apply to existing plants operated < 1 500 h/yr.\n\nOptimising the functioning of an existing technique to reduce NOX emissions further may lead to levels of CO emissions at the higher end of the indicative range for CO emissions given after this table.\n\nThese BAT-AELs do not apply to existing turbines for mechanical drive applications or to plants operated < 500 h/yr.\n\nFor plants with a net electrical efficiency (EE) greater than 55 %, a correction factor may be applied to the higher end of the BAT-AEL range, corresponding to [higher end] × EE/55, where EE is the net electrical efficiency of the plant determined at ISO baseload conditions."]
["Glass","3. Mineral industry","Mineral wool","Stone wool","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Hydrogen sulphide","BAT is to reduce H 2 S emissions from the melting furnace by applying a waste gas incineration system to oxidise hydrogen sulphide to SO 2","kg/tonne melted glass","N/A","0.005","Amber",0,"273.15","101.3",0.08,"Daily average (continuous)","The conversion factor of 2,5 × 10 –3 for stone wool has been applied",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","CCGT","New","Natural gas ","≥ 50 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",15,"40","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period ","These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines\n\nIn the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective."]
["Glass","3. Mineral industry","Domestic glass","Lead crystal glass","Unspecified","Unspecified","Unspecified","Unspecified","Dusty downstreatm processes ","Air","Lead","For downstream dusty processes, BAT is to reduce emissions of dust and metals by using one or a combination of the following techniques: (i) Performing dusty operations (e.g. cutting, grinding, polishing) under liquid; (ii) Applying a bag filter system","mg/Nm3","1","1.5","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3","N/A","Daily average (continuous)","The levels refer to downstream operations on lead crystal glass.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","CCGT with a net total fuel utilisation of < 75 %","Existing","Natural gas ","≥ 600 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",10,"40","Green","Continuous ",0,0,0.15,"Yearly","These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines\n\nIn the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective.\n\nThese BAT-AELs do not apply to existing plants operated < 1 500 h/yr.\n\nOptimising the functioning of an existing technique to reduce NOX emissions further may lead to levels of CO emissions at the higher end of the indicative range for CO emissions given after this table.\n\nThese BAT-AELs do not apply to existing turbines for mechanical drive applications or to plants operated < 500 h/yr.\n\nFor plants with a net electrical efficiency (EE) greater than 55 %, a correction factor may be applied to the higher end of the BAT-AEL range, corresponding to [higher end] × EE/55, where EE is the net electrical efficiency of the plant determined at ISO baseload conditions."]
["Glass","3. Mineral industry","Domestic glass","Lead crystal glass","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Lead","When lead compounds are used for the manufacturing of lead crystal glass, BAT is to reduce lead emissions from the melting furnace by using one or a combination of the following techniques: (i) Electric melting; (ii) Bag filter; (iii) Electrostatic precipitator; (iv) Dry or semi-dry scrubbing in combination with a filtration system","mg/Nm3","0.5","1","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The values refer to the sum of lead present in the flue-gases in both solid and gaseous phases.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","CCGT with a net total fuel utilisation of < 75 %","Existing","Natural gas ","≥ 600 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",18,"50","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period ","These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines\n\nIn the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective.\n\nThese BAT-AELs do not apply to existing turbines for mechanical drive applications or to plants operated < 500 h/yr.\n\nFor plants with a net electrical efficiency (EE) greater than 55 %, a correction factor may be applied to the higher end of the BAT-AEL range, corresponding to [higher end] × EE/55, where EE is the net electrical efficiency of the plant determined at ISO baseload conditions."]
["Glass","3. Mineral industry","Domestic glass","Lead crystal glass","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Lead","When lead compounds are used for the manufacturing of lead crystal glass, BAT is to reduce lead emissions from the melting furnace by using one or a combination of the following techniques: (i) Electric melting; (ii) Bag filter; (iii) Electrostatic precipitator; (iv) Dry or semi-dry scrubbing in combination with a filtration system","kg/tonne melted glass",1E-3,3.0000000000000001E-3,"Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The values refer to the sum of lead present in the flue-gases in both solid and gaseous phases.\n\nA conversion factor of 3 × 10 –3 has been applied (see Table 2). However, a case-by-case conversion factor may have to be applied for specific productions.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","CCGT with a net total fuel utilisation of ≥ 75 %","Existing","Natural gas ","≥ 600 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",10,"50","Green","Continuous ",0,0,0.15,"Yearly","These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines\n\nIn the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective.\n\nThese BAT-AELs do not apply to existing plants operated < 1 500 h/yr.\n\nOptimising the functioning of an existing technique to reduce NOX emissions further may lead to levels of CO emissions at the higher end of the indicative range for CO emissions given after this table.\n\nThese BAT-AELs do not apply to existing turbines for mechanical drive applications or to plants operated < 500 h/yr.\n\nFor plants with a net electrical efficiency (EE) greater than 55 %, a correction factor may be applied to the higher end of the BAT-AEL range, corresponding to [higher end] × EE/55, where EE is the net electrical efficiency of the plant determined at ISO baseload conditions."]
["Glass","3. Mineral industry","Filament glass fibre","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Metals (Group 1 + Group 2)","BAT is to reduce metal emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of metals; (ii) Applying a dry or semi-dry scrubbing in combination with filtration system; (iii) Applying wet scrubbing","mg/Nm3","1","3","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The levels refer to the sum of metals present in the flue-gases in both solid and gaseous phases",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","CCGT with a net total fuel utilisation of ≥ 75 %","Existing","Natural gas ","≥ 600 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",18,"55","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period ","These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines\n\nIn the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective.\n\nThese BAT-AELs do not apply to existing turbines for mechanical drive applications or to plants operated < 500 h/yr.\n\nFor plants with a net electrical efficiency (EE) greater than 55 %, a correction factor may be applied to the higher end of the BAT-AEL range, corresponding to [higher end] × EE/55, where EE is the net electrical efficiency of the plant determined at ISO baseload conditions.\n\nFor existing plants put into operation no later than 7 January 2014, the higher end of the BAT-AEL range is 65 mg/Nm3."]
["Glass","3. Mineral industry","Filament glass fibre","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Metals (Group 1 + Group 2)","BAT is to reduce metal emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of metals; (ii) Applying a dry or semi-dry scrubbing in combination with filtration system; (iii) Applying wet scrubbing","kg/tonne melted glass",4.5000000000000005E-3,1.35E-4,"Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The levels refer to the sum of metals present in the flue-gases in both solid and gaseous phases.\n\nThe conversion factor reported in Table 2 (4,5 × 10 –3 ) has been applied.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Coal-fired PC boiler","Existing","Coal and/or lignite ","≥ 300 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Combination of other primary techniques for NOX reduction (e.g. air staging, fuel staging, flue-gas recirculation, low- NOX burners (LNB)); (iii) Selective non- catalytic reduction (SNCR); (iv) Selective catalytic reduction (SCR); (v) Combined techniques for NOX and SOX reduction","mg/Nm3",85,"165","Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ","In the case of plants put into operation no later than 7 January 2014, the higher end of the range is 200 mg/Nm3 for plants operated ≥ 1 500 h/yr, and 220 mg/Nm3 for plants operated < 1 500 h/yr."]
["Glass","3. Mineral industry","Flat glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes","Air","Metals (Group 1 + Group 2)","BAT is to reduce emissions to air from the downstream processes by using one or a combination of the following techniques: (i) Minimising the losses of coating products applied to the flat glass by ensuring a good sealing of the application system; (ii) Minimising the losses of SO2 from the annealing ler, by operating the control system in an optimum manner; (iii) Combining the SO2 emissions from the lehr with the waste fas from the melting furnace, when technically feasible and where a secondary treatment system is applied (filter and dry or semi-dry scrubber); (iv) Applying a secondary technique, e.g. wet scrubbing, or dry scrubbing and filtration","mg/Nm3","N/A","5","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3","N/A","Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Coal-fired PC boiler","Existing","Coal and/or lignite ","≥ 300 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Combination of other primary techniques for NOX reduction (e.g. air staging, fuel staging, flue-gas recirculation, low- NOX burners (LNB)); (iii) Selective non- catalytic reduction (SNCR); (iv) Selective catalytic reduction (SCR); (v) Combined techniques for NOX and SOX reduction","mg/Nm3",65,150,"Green","Continuous ",0,0,0.06,"Yearly",0]
["Glass","3. Mineral industry","Container glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Metals (Group 1 + Group 2)","BAT is to reduce metal emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of metals; (ii) Minimising the use of metal compounds in the batch formulation, where colouring and decolourising of glass is needed, subject to consumer glass quality requirements; (iii) Applying a filtration system (bag filter or electrostatic precipitator); (iv) Applying a dry or semi-dry scrubbing, in combination with a filtration system","mg/Nm3","1","5","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The levels refer to the sum of metals present in the flue-gases in both solid and gaseous phases.\n\nThe lower levels are BAT-AELs when metal compounds are not intentionally used in the batch formulation.\n\nThe upper levels are associated with the use of metals for colouring or decolourising the glass, or when the flue-gases from the hot-end coating operations are treated together with the melting furnace emissions",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Coal-fired PC boiler","New","Coal and/or lignite ","≥ 300 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Combination of other primary techniques for NOX reduction (e.g. air staging, fuel staging, flue-gas recirculation, low- NOX burners (LNB)); (iii) Selective non- catalytic reduction (SNCR); (iv) Selective catalytic reduction (SCR); (v) Combined techniques for NOX and SOX reduction","mg/Nm3",65,85,"Green","Continuous ",0,0,0.06,"Yearly",0]
["Glass","3. Mineral industry","Container glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Metals (Group 1 + Group 2)","BAT is to reduce metal emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of metals; (ii) Minimising the use of metal compounds in the batch formulation, where colouring and decolourising of glass is needed, subject to consumer glass quality requirements; (iii) Applying a filtration system (bag filter or electrostatic precipitator); (iv) Applying a dry or semi-dry scrubbing, in combination with a filtration system","kg/tonne melted glass",1.5E-3,7.4999999999999997E-3,"Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The levels refer to the sum of metals present in the flue-gases in both solid and gaseous phases.\n\nThe lower levels are BAT-AELs when metal compounds are not intentionally used in the batch formulation.\n\nThe upper levels are associated with the use of metals for colouring or decolourising the glass, or when the flue-gases from the hot-end coating operations are treated together with the melting furnace emissions\n\nThe conversion factor for general cases, reported in Table 2 (1,5 × 10 –3 ) has been applied",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Coal-fired PC boiler","New","Coal and/or lignite ","≥ 300 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Combination of other primary techniques for NOX reduction (e.g. air staging, fuel staging, flue-gas recirculation, low- NOX burners (LNB)); (iii) Selective non- catalytic reduction (SNCR); (iv) Selective catalytic reduction (SCR); (v) Combined techniques for NOX and SOX reduction","mg/Nm3",80,125,"Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ",0]
["Glass","3. Mineral industry","Domestic glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Dusty downstreatm processes ","Air","Metals (Group 1 + Group 2)","For downstream dusty processes, BAT is to reduce emissions of dust and metals by using one or a combination of the following techniques: (i) Performing dusty operations (e.g. cutting, grinding, polishing) under liquid; (ii) Applying a bag filter system","mg/Nm3","1","5","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3","N/A","Daily average (continuous)","The levels refer to the sum of metals present in the waste gas.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Dual fuel gas turbines ","Unspecified","Gas oil ","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of gas oil in gas turbines, BAT is to use one or a combination of the techniques given below: (i) Water/steam addition; (ii) Low-NOX burners (LNB); (iii) Selective catalytic reduction (SCR)","mg/Nm3",145,"250","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period.","The emission level for NOX emissions to air from the combustion of gas oil in dual fuel gas turbines for emergency use operated < 500 h/yr"]
["Glass","3. Mineral industry","Frits ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Metals (Group 1 + Group 2)","BAT is to reduce metal emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of metals; (ii) Minimising of the use of metal compounds in the batch formulation, where colouring is required or other specific characteristics are conferred to the frit; (iii) Dry or semi-dry scrubbing, in combination with a filtration system","mg/Nm3","N/A","5","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The levels refer to the sum of metals present in the flue-gases in both solid and gaseous phases",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Engine","Existing","Natural gas ","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",20,"100","Green","Continuous ",0,0,0.15,"Yearly","Optimising the functioning of an existing technique to reduce NOX emissions further may lead to levels of CO emissions at the higher end of the indicative range for CO emissions given after this table.\n\nThese BAT-AELs do not apply to plants operated < 1 500 h/yr."]
["Glass","3. Mineral industry","Frits ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Metals (Group 1 + Group 2)","BAT is to reduce metal emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of metals; (ii) Minimising of the use of metal compounds in the batch formulation, where colouring is required or other specific characteristics are conferred to the frit; (iii) Dry or semi-dry scrubbing, in combination with a filtration system","kg/tonne melted glass","N/A",3.6999999999999998E-2,"Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The levels refer to the sum of metals present in the flue-gases in both solid and gaseous phases",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Engine","Existing","Natural gas ","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",55,"110","Green","Continuous ",0,0,0.15,"Daily average or average over sampling period ","For plants operated < 500 h/yr, these levels are indicative.\n\nIn the case of engines for emergency use operated < 500 h/yr that could not apply the lean-burn concept or use SCR, the higher end of the indicative range is 175 mg/Nm3."]
["Glass","3. Mineral industry","HTIW wools","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes ","Air","Metals (Group 1 + Group 2)","BAT is to reduce metal emissions from the melting furnace and/or downstream processes by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of metals; (ii) Applying a filtration system","mg/Nm3","N/A","5","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3","N/A","Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Engine","New","Natural gas ","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",20,"75","Green","Continuous ",0,0,0.15,"Yearly","Optimising the functioning of an existing technique to reduce NOX emissions further may lead to levels of CO emissions at the higher end of the indicative range for CO emissions given after this table."]
["Glass","3. Mineral industry","HTIW wools","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Metals (Group 1 + Group 2)","BAT is to reduce metal emissions from the melting furnace and/or downstream processes by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of metals; (ii) Applying a filtration system","mg/Nm3","N/A","5","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Engine","New","Natural gas ","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",55,"85","Green","Continuous ",0,0,0.15,"Daily average or average over sampling period ",0]
["Glass","3. Mineral industry","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Metals (Group 1 + Group 2)","BAT is to reduce metal emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of metals; (ii) Application of a filtration system","mg/Nm3","1","2","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The ranges refer to the sum of metals present in the flue-gases in both solid and gaseous phases\n\nThe conversion factors of 2 × 10 –3 and 2,5 × 10 –3 have been used for the determination of the lower and upper values of the BAT-AELs range\n\nHigher values are associated with the use of cupola furnaces for the production of stone wool.\nEN L 70/48 Official Journal of the European Union 8.3.2012",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","FBC boiler combusting coal and/or lignite and lignite-fired PC boiler","Existing","Coal and/or lignite ","≥ 300 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Combination of other primary techniques for NOX reduction (e.g. air staging, fuel staging, flue-gas recirculation, low- NOX burners (LNB)); (iii) Selective non- catalytic reduction (SNCR); (iv) Selective catalytic reduction (SCR); (v) Combined techniques for NOX and SOX reduction","mg/Nm3",140,165,"Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ","The higher end of the range is 220 mg/Nm3 for FBC boilers put into operation no later than 7 January 2014 and for lignite-fired PC boilers."]
["Glass","3. Mineral industry","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Metals (Group 1 + Group 2)","BAT is to reduce metal emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of metals; (ii) Application of a filtration system","kg/tonne melted glass",2E-3,5.0000000000000001E-3,"Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The ranges refer to the sum of metals present in the flue-gases in both solid and gaseous phases\n\nThe conversion factors of 2 × 10 –3 and 2,5 × 10 –3 have been used for the determination of the lower and upper values of the BAT-AELs range\n",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","FBC boiler combusting coal and/or lignite and lignite-fired PC boiler","Existing","Coal and/or lignite ","≥ 300 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Combination of other primary techniques for NOX reduction (e.g. air staging, fuel staging, flue-gas recirculation, low- NOX burners (LNB)); (iii) Selective non- catalytic reduction (SNCR); (iv) Selective catalytic reduction (SCR); (v) Combined techniques for NOX and SOX reduction","mg/Nm3",85,"150","Green","Continuous ",0,0,0.06,"Yearly","The lower end of the range is considered achievable when using SCR.\n\nThe higher end of the range is 175 mg/Nm3 for FBC boilers put into operation no later than 7 January 2014 and for lignite-fired PC boilers."]
["Glass","3. Mineral industry","Special glass ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes","Air","Metals (Group 1 + Group 2)","For downstream dusty processes, BAT is to reduce emissions of dust and metals by using one or a combination of the following techniques: (i) Performing dusty operations (e.g. cutting, grinding, polishing) under liquid; (ii) Applying a bag filter system","mg/Nm3","1","5","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3","N/A","Daily average (continuous)","\nBAT-AELs for dust and metal emissions from downstream processes in the special glass sector, when treated separately\n\nThe levels refer to the sum of metals present in the waste gas.\n55.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","FBC boiler combusting coal and/or lignite and lignite-fired PC boiler","New","Coal and/or lignite ","≥ 300 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Combination of other primary techniques for NOX reduction (e.g. air staging, fuel staging, flue-gas recirculation, low- NOX burners (LNB)); (iii) Selective non- catalytic reduction (SNCR); (iv) Selective catalytic reduction (SCR); (v) Combined techniques for NOX and SOX reduction","mg/Nm3",50,85,"Green","Continuous ",0,0,0.06,"Yearly",0]
["Glass","3. Mineral industry","Special glass ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Metals (Group 1 + Group 2)","BAT is to reduce metal emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of metals; (ii) Minimising the use of metal compounds in the batch formulation, through a suitable selection of the raw materials where colouring and decolourising of glass is needed or where specific characteristics are conferred to the glass; (iii) Dry or semi-dry scrubbing, in combination with a filtration system","mg/Nm3","1","5","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The levels refer to the sum of metals present in the flue-gases in both solid and gaseous phases.\n\nThe lower levels are BAT-AELs when metal compounds are not intentionally used in the batch formulation.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","FBC boiler combusting coal and/or lignite and lignite-fired PC boiler","New","Coal and/or lignite ","≥ 300 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Combination of other primary techniques for NOX reduction (e.g. air staging, fuel staging, flue-gas recirculation, low- NOX burners (LNB)); (iii) Selective non- catalytic reduction (SNCR); (iv) Selective catalytic reduction (SCR); (v) Combined techniques for NOX and SOX reduction","mg/Nm3",80,125,"Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ",0]
["Glass","3. Mineral industry","Special glass ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Metals (Group 1 + Group 2)","BAT is to reduce metal emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of metals; (ii) Minimising the use of metal compounds in the batch formulation, through a suitable selection of the raw materials where colouring and decolourising of glass is needed or where specific characteristics are conferred to the glass; (iii) Dry or semi-dry scrubbing, in combination with a filtration system","kg/tonne melted glass",3.0000000000000001E-3,1.4999999999999999E-2,"Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The levels refer to the sum of metals present in the flue-gases in both solid and gaseous phases.\n\nThe lower levels are BAT-AELs when metal compounds are not intentionally used in the batch formulation.\n\nThe conversion factor of 2,5 × 10 –3 (see Table 2) has been used, with some values indicated in the table having been approximated. A case-by-case conversion factor may have to be applied based on the type of production.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Fired engines ","Existing","HFO and/or gas oil in reciprocating engines","≥ 50 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of HFO and/or gas oil in reciprocating engines, BAT is to use one or a combination of the techniques given below: (i) Low-NOX combustion concept in diesel engines; (ii) Exhaust-gas recirculation (EGR); (iii) Water/steam addition; (iv) Selective catalytic reduction (SCR)","mg/Nm3",152,"625","Green","Continuous ",0,0,0.15,"Yearly","These BAT-AELs do not apply to plants operated < 1 500 h/yr or to plants that cannot be fitted with secondary abatement techniques."]
["Glass","3. Mineral industry","Frits ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes ","Air","Metals (Group 1)","For downstream dusty processes, BAT is to reduce emissions by using one or a combination of the following techniques: (i) Applying wet milling techniques; (ii) Operating dry milling and dry product packaging under an efficient extraction system in conjunction with a fabric filter; (iii) Applying a filtration system","mg/Nm3","N/A","1","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3","N/A","Daily average (continuous)","The levels refer to the sum of metals present in the waste gas.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Fired engines ","Existing","HFO and/or gas oil in reciprocating engines","≥ 50 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of HFO and/or gas oil in reciprocating engines, BAT is to use one or a combination of the techniques given below: (i) Low-NOX combustion concept in diesel engines; (ii) Exhaust-gas recirculation (EGR); (iii) Water/steam addition; (iv) Selective catalytic reduction (SCR)","mg/Nm3",150,"750","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period ","The BAT-AEL range is 1 150–1 900 mg/Nm3 for plants operated < 1 500 h/yr and for plants that cannot be fitted with secondary abatement techniques.\n\nFor plants operated < 500 h/yr, these levels are indicative."]
["Glass","3. Mineral industry","Container glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Metals (Group 1)","BAT is to reduce metal emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of metals; (ii) Minimising the use of metal compounds in the batch formulation, where colouring and decolourising of glass is needed, subject to consumer glass quality requirements; (iii) Applying a filtration system (bag filter or electrostatic precipitator); (iv) Applying a dry or semi-dry scrubbing, in combination with a filtration system","mg/Nm3","0.2","1","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The levels refer to the sum of metals present in the flue-gases in both solid and gaseous phases.\n\nThe lower levels are BAT-AELs when metal compounds are not intentionally used in the batch formulation.\n\nThe upper levels are associated with the use of metals for colouring or decolourising the glass, or when the flue-gases from the hot-end coating operations are treated together with the melting furnace emissions\n\nIn specific cases, when high quality flint glass is produced requiring higher amounts of selenium for decolourising (depending on the raw materials), higher values are reported, up to 3",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Fired engines ","New","HFO and/or gas oil in reciprocating engines","≥ 50 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of HFO and/or gas oil in reciprocating engines, BAT is to use one or a combination of the techniques given below: (i) Low-NOX combustion concept in diesel engines; (ii) Exhaust-gas recirculation (EGR); (iii) Water/steam addition; (iv) Selective catalytic reduction (SCR)","mg/Nm3",115,"190","Green","Continuous ",0,0,0.15,"Yearly","For plants including units of < 20 MWth combusting HFO, the higher end of the BAT-AEL range applying to those units is 225 mg/Nm3."]
["Glass","3. Mineral industry","Container glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Metals (Group 1)","BAT is to reduce metal emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of metals; (ii) Minimising the use of metal compounds in the batch formulation, where colouring and decolourising of glass is needed, subject to consumer glass quality requirements; (iii) Applying a filtration system (bag filter or electrostatic precipitator); (iv) Applying a dry or semi-dry scrubbing, in combination with a filtration system","kg/tonne melted glass",2.9999999999999997E-4,1.5E-3,"Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The levels refer to the sum of metals present in the flue-gases in both solid and gaseous phases.\n\nThe lower levels are BAT-AELs when metal compounds are not intentionally used in the batch formulation.\n\nThe upper levels are associated with the use of metals for colouring or decolourising the glass, or when the flue-gases from the hot-end coating operations are treated together with the melting furnace emissions\n\nThe conversion factor for general cases, reported in Table 2 (1,5 × 10 –3 ) has been applied",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Fired engines ","New","HFO and/or gas oil in reciprocating engines","≥ 50 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of HFO and/or gas oil in reciprocating engines, BAT is to use one or a combination of the techniques given below: (i) Low-NOX combustion concept in diesel engines; (ii) Exhaust-gas recirculation (EGR); (iii) Water/steam addition; (iv) Selective catalytic reduction (SCR)","mg/Nm3",145,"300","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period ",0]
["Glass","3. Mineral industry","Domestic glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Dusty downstreatm processes ","Air","Metals (Group 1)","For downstream dusty processes, BAT is to reduce emissions of dust and metals by using one or a combination of the following techniques: (i) Performing dusty operations (e.g. cutting, grinding, polishing) under liquid; (ii) Applying a bag filter system","mg/Nm3","N/A","1","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3","N/A","Daily average (continuous)","The levels refer to the sum of metals present in the waste gas.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Gas turbine for mechanical drive applications — All but plants operated < 500 h/yr","Existing","Natural gas ","≥ 50 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",25,"55","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period ","These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines\n\nIn the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective.\n\nFor existing plants put into operation no later than 7 January 2014, the higher end of the BAT-AEL range is 65 mg/Nm3.\n\nFor existing plants put into operation no later than 7 January 2014, the higher end of the BAT-AEL range is 65 mg/Nm3."]
["Glass","3. Mineral industry","Domestic glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Metals (Group 1)","BAT is to reduce metal emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of metals; (ii) Minimising the use of metal compounds in the batch formulation, through a suitable selection of the raw materials where colouring and decolourising of glass is needed or where specific characteristics are conferred to the glass; (iii) Dry or semi-dry scrubbing, in combination with a filtration system ","mg/Nm3","0.2","1","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","BAT-AELs for metal emissions from the melting furnace in the domestic glass sector with the exception of glasses where selenium is used for decolourising\n\nThe levels refer to the sum of metals present in the flue-gases in both solid and gaseous phases.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Gas turbine for mechanical drive applications — All but plants operated < 500 h/yr","Existing","Natural gas ","≥ 50 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",15,"50","Green","Continuous ",0,0,0.15,"Yearly","These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines\n\nIn the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective.\n\nThese BAT-AELs do not apply to existing plants operated < 1 500 h/yr.\n\nOptimising the functioning of an existing technique to reduce NOX emissions further may lead to levels of CO emissions at the higher end of the indicative range for CO emissions given after this table.\n\nFor existing plants put into operation no later than 7 January 2014, the higher end of the BAT-AEL range is 60 mg/Nm3.\n"]
["Glass","3. Mineral industry","Domestic glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Metals (Group 1)","BAT is to reduce metal emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of metals; (ii) Minimising the use of metal compounds in the batch formulation, through a suitable selection of the raw materials where colouring and decolourising of glass is needed or where specific characteristics are conferred to the glass; (iii) Dry or semi-dry scrubbing, in combination with a filtration system ","kg/tonne melted glass",5.9999999999999995E-4,3.0000000000000001E-3,"Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","BAT-AELs for metal emissions from the melting furnace in the domestic glass sector with the exception of glasses where selenium is used for decolourising\n\nThe levels refer to the sum of metals present in the flue-gases in both solid and gaseous phases.\n\nA conversion factor of 3 × 10 –3 has been applied (see Table 2). However, a case-by-case conversion factor may have to be applied for specific productions.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Gas turbine put into operation no later than 27 November 2003, or existing gas turbine for emergency use and operated < 500 h/yr","Existing","Natural gas ","≥ 50 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3","N/A","N/A","Green","Continuous ",0,0,0.15,"Yearly","These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines\n\nIn the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective.\n\nThese BAT-AELs do not apply to existing plants operated < 1 500 h/yr.\n\nOptimising the functioning of an existing technique to reduce NOX emissions further may lead to levels of CO emissions at the higher end of the indicative range for CO emissions given after this table."]
["Glass","3. Mineral industry","Filament glass fibre","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Metals (Group 1)","BAT is to reduce metal emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of metals; (ii) Applying a dry or semi-dry scrubbing in combination with filtration system; (iii) Applying wet scrubbing","mg/Nm3","0.2","1","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The levels refer to the sum of metals present in the flue-gases in both solid and gaseous phases",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Gas turbine put into operation no later than 27 November 2003, or existing gas turbine for emergency use and operated < 500 h/yr","Existing","Natural gas ","≥ 50 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",60,"140","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period ","These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines\n\nIn the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective.\n\nThe lower end of the BAT-AEL range for NOX can be achieved with DLN burners.\n\nThese levels are indicative."]
["Glass","3. Mineral industry","Filament glass fibre","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Metals (Group 1)","BAT is to reduce metal emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of metals; (ii) Applying a dry or semi-dry scrubbing in combination with filtration system; (iii) Applying wet scrubbing","kg/tonne melted glass",9.0000000000000008E-4,4.5000000000000005E-3,"Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The levels refer to the sum of metals present in the flue-gases in both solid and gaseous phases. \n\nThe conversion factor reported in Table 2 (4,5 × 10 –3 ) has been applied.\n",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","IGCC","Existing","Unspecified","≥ 100 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent and/or reduce NOX emissions to air while limiting CO emissions to air from IGCC plants, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Water/steam addition; (iii) Dry low-NOX burners (DLN); (iv) Syngas dilution with waste nitrogen from the air supply unit (ASU); (v) Selective catalytic reduction (SCR)","mg/Nm3",12,"45","Green","Continuous",0,0,0.15,"Yearly","As an indication, the yearly average CO emission levels for existing plants operated ≥ 1 500 h/yr and for new plants will generally be < 5–30 mg/Nm3."]
["Glass","3. Mineral industry","Flat glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes","Air","Metals (Group 1)","BAT is to reduce emissions to air from the downstream processes by using one or a combination of the following techniques: (i) Minimising the losses of coating products applied to the flat glass by ensuring a good sealing of the application system; (ii) Minimising the losses of SO2 from the annealing ler, by operating the control system in an optimum manner; (iii) Combining the SO2 emissions from the lehr with the waste fas from the melting furnace, when technically feasible and where a secondary treatment system is applied (filter and dry or semi-dry scrubber); (iv) Applying a secondary technique, e.g. wet scrubbing, or dry scrubbing and filtration","mg/Nm3","N/A","1","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3","N/A","Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","IGCC","Existing","Unspecified","≥ 100 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent and/or reduce NOX emissions to air while limiting CO emissions to air from IGCC plants, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Water/steam addition; (iii) Dry low-NOX burners (DLN); (iv) Syngas dilution with waste nitrogen from the air supply unit (ASU); (v) Selective catalytic reduction (SCR)","mg/Nm3",1,"60","Green","Continuous",0,0,0.15,"Daily average or average over the sampling period ","As an indication, the yearly average CO emission levels for existing plants operated ≥ 1 500 h/yr and for new plants will generally be < 5–30 mg/Nm3."]
["Glass","3. Mineral industry","Flat glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Metals (Group 1)","BAT is to reduce metal emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of metals; (ii) Applying a filtration system; (iii) Applying a dry or semi-dry scrubbing in combination with a filtration system ","mg/Nm3","0.2","1","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","BAT-AELs for metal emissions from the melting furnace in the flat glass sector, with the exception of selenium coloured glasses\n\nThe ranges refer to the sum of metals present in the flue-gases in both solid and gaseous phases.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","IGCC","New","Unspecified","≥ 100 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent and/or reduce NOX emissions to air while limiting CO emissions to air from IGCC plants, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Water/steam addition; (iii) Dry low-NOX burners (DLN); (iv) Syngas dilution with waste nitrogen from the air supply unit (ASU); (v) Selective catalytic reduction (SCR)","mg/Nm3",10,"25","Green","Continuous",0,0,0.15,"Yearly","As an indication, the yearly average CO emission levels for existing plants operated ≥ 1 500 h/yr and for new plants will generally be < 5–30 mg/Nm3."]
["Glass","3. Mineral industry","Flat glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Metals (Group 1)","BAT is to reduce metal emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of metals; (ii) Applying a filtration system; (iii) Applying a dry or semi-dry scrubbing in combination with a filtration system ","kg/tonne melted glass",5.0000000000000001E-4,2.5000000000000001E-3,"Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","BAT-AELs for metal emissions from the melting furnace in the flat glass sector, with the exception of selenium coloured glasses\n\nThe ranges refer to the sum of metals present in the flue-gases in both solid and gaseous phases.\n\nThe conversion factor reported in Table 2 (2,5 × 10 –3 ) has been applied",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","IGCC","New","Unspecified","≥ 100 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent and/or reduce NOX emissions to air while limiting CO emissions to air from IGCC plants, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Water/steam addition; (iii) Dry low-NOX burners (DLN); (iv) Syngas dilution with waste nitrogen from the air supply unit (ASU); (v) Selective catalytic reduction (SCR)","mg/Nm3",1,"35","Green","Continuous",0,0,0.15,"Daily average or average over the sampling period ","As an indication, the yearly average CO emission levels for existing plants operated ≥ 1 500 h/yr and for new plants will generally be < 5–30 mg/Nm3."]
["Glass","3. Mineral industry","Frits ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Metals (Group 1)","BAT is to reduce metal emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of metals; (ii) Minimising of the use of metal compounds in the batch formulation, where colouring is required or other specific characteristics are conferred to the frit; (iii) Dry or semi-dry scrubbing, in combination with a filtration system","mg/Nm3","N/A","1","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The levels refer to the sum of metals present in the flue-gases in both solid and gaseous phases",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","OCGT","New","Natural gas ","≥ 50 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",15,"35","Green","Continuous ",0,0,0.15,"Yearly","These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines\n\nIn the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective.\n\nThese BAT-AELs do not apply to existing plants operated < 1 500 h/yr.\n\nOptimising the functioning of an existing technique to reduce NOX emissions further may lead to levels of CO emissions at the higher end of the indicative range for CO emissions given after this table.\n\nThese BAT-AELs do not apply to existing turbines for mechanical drive applications or to plants operated < 500 h/yr.\n\nFor plants with a net electrical efficiency (EE) greater than 39 %, a correction factor may be applied to the higher end of the range, corresponding to [higher end] × EE/39, where EE is the net electrical energy efficiency or net mechanical energy efficiency of the plant determined at ISO baseload conditions."]
["Glass","3. Mineral industry","Frits ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Metals (Group 1)","BAT is to reduce metal emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of metals; (ii) Minimising of the use of metal compounds in the batch formulation, where colouring is required or other specific characteristics are conferred to the frit; (iii) Dry or semi-dry scrubbing, in combination with a filtration system","kg/tonne melted glass","N/A",7.4999999999999997E-3,"Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The levels refer to the sum of metals present in the flue-gases in both solid and gaseous phases\n\nThe conversion factor of 7,5 × 10 –3 has been used. A case-by-case conversion factor may have to be applied based on the type of combustion",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","OCGT","New","Natural gas ","≥ 50 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",25,"50","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period ","These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines\n\nIn the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective.\n\nThese BAT-AELs do not apply to existing turbines for mechanical drive applications or to plants operated < 500 h/yr.\n\nFor plants with a net electrical efficiency (EE) greater than 39 %, a correction factor may be applied to the higher end of the range, corresponding to [higher end] × EE/39, where EE is the net electrical energy efficiency or net mechanical energy efficiency of the plant determined at ISO baseload conditions."]
["Glass","3. Mineral industry","HTIW wools","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes ","Air","Metals (Group 1)","BAT is to reduce metal emissions from the melting furnace and/or downstream processes by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of metals; (ii) Applying a filtration system","mg/Nm3","N/A","1","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3","N/A","Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","OCGT (excluding turbines for mechanical drive applications) — All but plants operated < 500 h/yr","Existing","Natural gas ","≥ 50 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",15,"50","Green","Continuous ",0,0,0.15,"Yearly","These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines\n\nIn the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective.\n\nThese BAT-AELs do not apply to existing plants operated < 1 500 h/yr.\n\nOptimising the functioning of an existing technique to reduce NOX emissions further may lead to levels of CO emissions at the higher end of the indicative range for CO emissions given after this table.\n\nThese BAT-AELs do not apply to existing turbines for mechanical drive applications or to plants operated < 500 h/yr.\n\nFor plants with a net electrical efficiency (EE) greater than 39 %, a correction factor may be applied to the higher end of the range, corresponding to [higher end] × EE/39, where EE is the net electrical energy efficiency or net mechanical energy efficiency of the plant determined at ISO baseload conditions."]
["Glass","3. Mineral industry","HTIW wools","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Metals (Group 1)","BAT is to reduce metal emissions from the melting furnace and/or downstream processes by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of metals; (ii) Applying a filtration system","mg/Nm3","N/A","1","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","OCGT (excluding turbines for mechanical drive applications) — All but plants operated < 500 h/yr","Existing","Natural gas ","≥ 50 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",25,"55","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period ","These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines\n\nIn the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective.\n\nThe higher end of the range is 80 mg/Nm3 in the case of plants which were put into operation no later than 27 November 2003 and are operated between 500 h/yr and 1 500 h/yr.\n\n\nThese BAT-AELs do not apply to existing turbines for mechanical drive applications or to plants operated < 500 h/yr.\n\nFor plants with a net electrical efficiency (EE) greater than 39 %, a correction factor may be applied to the higher end of the range, corresponding to [higher end] × EE/39, where EE is the net electrical energy efficiency or net mechanical e"]
["Glass","3. Mineral industry","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Metals (Group 1)","BAT is to reduce metal emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of metals; (ii) Application of a filtration system","mg/Nm3","0.2","1","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The ranges refer to the sum of metals present in the flue-gases in both solid and gaseous phases\n\nHigher values are associated with the use of cupola furnaces for the production of stone wool",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Open-cycle gas turbines on offshore platforms","Existing","Gaseous fuels ","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of gaseous and/or liquid fuels on offshore platforms, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Dry low-NOX burners (DLN); (iii) Lean-burn concept; (iv) Low-NOX burners (LNB)","mg/Nm3",50,"350","Green","Continuous ",0,0,0.03,"Average over the sampling period","These BAT-AELs are based on > 70 % of baseload power available on the day.\n\nThis includes single fuel and dual fuel gas turbines.\n\nThe lower end of the BAT-AEL range can be achieved with DLN burners."]
["Glass","3. Mineral industry","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Metals (Group 1)","BAT is to reduce metal emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of metals; (ii) Application of a filtration system","kg/tonne melted glass",4.0000000000000002E-4,2.5000000000000001E-3,"Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The ranges refer to the sum of metals present in the flue-gases in both solid and gaseous phases",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Open-cycle gas turbines on offshore platforms","New","Gaseous fuels ","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of gaseous and/or liquid fuels on offshore platforms, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Dry low-NOX burners (DLN); (iii) Lean-burn concept; (iv) Low-NOX burners (LNB)","mg/Nm3",15,"50","Green","Continuous ",0,0,0.03,"Average over the sampling period","These BAT-AELs are based on > 70 % of baseload power available on the day. \n\nThis includes single fuel and dual fuel gas turbines.\n\nThe higher end of the BAT-AEL range is 250 mg/Nm3 if DLN burners are not applicable."]
["Glass","3. Mineral industry","Special glass ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes","Air","Metals (Group 1)","For downstream dusty processes, BAT is to reduce emissions of dust and metals by using one or a combination of the following techniques: (i) Performing dusty operations (e.g. cutting, grinding, polishing) under liquid; (ii) Applying a bag filter system","mg/Nm3","N/A","1","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3","N/A","Daily average (continuous)","BAT-AELs for dust and metal emissions from downstream processes in the special glass sector, when treated separately\n\nThe levels refer to the sum of metals present in the waste gas.\n55.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Metals Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Hydrometallurgical operation involving dissolving/leaching with nitric acid","Air","Nitrogen dioxide","In order to reduce NOX emissions to air from a hydrometallurgical operation involving dissolving/leaching with nitric acid, BAT is to use one or both of the techniques given below: (i)Alkaline scrubber with caustic soda; (ii) Scrubber with oxidation agents (e.g. oxygen, hydrogen peroxide) and reducing agents (e.g. nitric acid,\nurea) for those vessels in hydrometallurgical operations with the potential to generate high concentrations\nof NOX. It is often applied in combination with (i) \n","mg/Nm3",70,150,"Green","Continuous or once per year",0,0,0,"Hourly average or average over the sampling period ",0]
["Glass","3. Mineral industry","Special glass ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Metals (Group 1)","BAT is to reduce metal emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of metals; (ii) Minimising the use of metal compounds in the batch formulation, through a suitable selection of the raw materials where colouring and decolourising of glass is needed or where specific characteristics are conferred to the glass; (iii) Dry or semi-dry scrubbing, in combination with a filtration system","mg/Nm3","0.1","1","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The levels refer to the sum of metals present in the flue-gases in both solid and gaseous phases.\n\nThe lower levels are BAT-AELs when metal compounds are not intentionally used in the batch formulation.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Gaseous fuels ","Lime kilns","Air","Nitrogen dioxide","In order to reduce NOx emissions from a lime kiln, BAT is to apply a combination of the techniques given below: (i) Optimised combustion and combustion control; (ii) Good mixing of fuel and air; (iii) Low-NOx burner; (iv) Fuel selection/low-N fuel","mg /nm3",100,350,"Green","Continuous",0,0,0.06,"Yearly","When using gaseous fuels originating from vegetable matter (e.g. non-condensable gases), including those obtained as by-products of the pulping process, emission levels up to 450 mg/Nm3 (corresponding to 0,45 kg NOx/ADt) may occur."]
["Glass","3. Mineral industry","Special glass ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Metals (Group 1)","BAT is to reduce metal emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of metals; (ii) Minimising the use of metal compounds in the batch formulation, through a suitable selection of the raw materials where colouring and decolourising of glass is needed or where specific characteristics are conferred to the glass; (iii) Dry or semi-dry scrubbing, in combination with a filtration system","kg/tonne melted glass",2.9999999999999997E-4,3.0000000000000001E-3,"Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","The levels refer to the sum of metals present in the flue-gases in both solid and gaseous phases.\n\nThe lower levels are BAT-AELs when metal compounds are not intentionally used in the batch formulation.\n\nThe conversion factor of 2,5 × 10 –3 (see Table 2) has been used, with some values indicated in the table having been approximated. A case-by-case conversion factor may have to be applied based on the type of production.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Gaseous fuels ","Lime kilns","Air","Nitrogen dioxide","In order to reduce NOx emissions from a lime kiln, BAT is to apply a combination of the techniques given below: (i) Optimised combustion and combustion control; (ii) Good mixing of fuel and air; (iii) Low-NOx burner; (iv) Fuel selection/low-N fuel","kg NOx/Adt",0.1,0.3,"Green","Continuous",0,0,"Unspecified","Yearly","When using gaseous fuels originating from vegetable matter (e.g. non-condensable gases), including those obtained as by-products of the pulping process, emission levels up to 450 mg/Nm3 (corresponding to 0,45 kg NOx/ADt) may occur."]
["Glass","3. Mineral industry","Domestic glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Metals (Group 1+ Group 2) ","BAT is to reduce metal emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of metals; (ii) Minimising the use of metal compounds in the batch formulation, through a suitable selection of the raw materials where colouring and decolourising of glass is needed or where specific characteristics are conferred to the glass; (iii) Dry or semi-dry scrubbing, in combination with a filtration system ","mg/Nm3","1","5","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","BAT-AELs for metal emissions from the melting furnace in the domestic glass sector with the exception of glasses where selenium is used for decolourising\n\nThe levels refer to the sum of metals present in the flue-gases in both solid and gaseous phases.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Liquid fuels","Lime kilns","Air","Nitrogen dioxide","In order to reduce NOx emissions from a lime kiln, BAT is to apply a combination of the techniques given below: (i) Optimised combustion and combustion control; (ii) Good mixing of fuel and air; (iii) Low-NOx burner; (iv) Fuel selection/low-N fuel","mg /nm3",100,200,"Green","Continuous",0,0,0.06,"Yearly","When using liquid fuels originating from vegetable matter (e.g. turpentine, methanol, tall-oil), including those obtained as by-products of the pulping process, emission levels up to 350 mg/Nm3 (corresponding to 0,35 kg NOx/ADt) may occur."]
["Glass","3. Mineral industry","Domestic glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Metals (Group 1+ Group 2) ","BAT is to reduce metal emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of metals; (ii) Minimising the use of metal compounds in the batch formulation, through a suitable selection of the raw materials where colouring and decolourising of glass is needed or where specific characteristics are conferred to the glass; (iii) Dry or semi-dry scrubbing, in combination with a filtration system ","kg/tonne melted glass",3.0000000000000001E-3,1.4999999999999999E-2,"Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","BAT-AELs for metal emissions from the melting furnace in the domestic glass sector with the exception of glasses where selenium is used for decolourising \n\nThe levels refer to the sum of metals present in the flue-gases in both solid and gaseous phases.\n\nA conversion factor of 3 × 10 –3 has been applied (see Table 2). However, a case-by-case conversion factor may have to be applied for specific productions.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Liquid fuels","Lime kilns","Air","Nitrogen dioxide","In order to reduce NOx emissions from a lime kiln, BAT is to apply a combination of the techniques given below: (i) Optimised combustion and combustion control; (ii) Good mixing of fuel and air; (iii) Low-NOx burner; (iv) Fuel selection/low-N fuel","kg NOx/Adt",0.1,0.2,"Green","Continuous",0,0,"Unspecified","Yearly","When using liquid fuels originating from vegetable matter (e.g. turpentine, methanol, tall-oil), including those obtained as by-products of the pulping process, emission levels up to 350 mg/Nm3 (corresponding to 0,35 kg NOx/ADt) may occur."]
["Glass","3. Mineral industry","Flat glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Metals (Group 1+ Group 2) ","BAT is to reduce metal emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of metals; (ii) Applying a filtration system; (iii) Applying a dry or semi-dry scrubbing in combination with a filtration system ","mg/Nm3","1","5","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","BAT-AELs for metal emissions from the melting furnace in the flat glass sector, with the exception of selenium coloured glasses\n\nThe ranges refer to the sum of metals present in the flue-gases in both solid and gaseous phases.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","TRS burner for strong odorous gases ","Air","Nitrogen dioxide","In order to reduce NOx emissions from the incineration of strong odorous gases in a dedicated TRS burner, BAT is to use one or a combination of the techniques given below: (i) Burner/firing optimisation; (ii) Staged incineration","mg/Nm3",50,400,"Green","Continuous",0,0,0.09,"Yearly","Where at existing plants a switch to staged incineration is not feasible, emissions levels up to 1 000 mg/Nm3 (corresponding to 0,2 kg/ADt) may occur."]
["Glass","3. Mineral industry","Flat glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Metals (Group 1+ Group 2) ","BAT is to reduce metal emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of metals; (ii) Applying a filtration system; (iii) Applying a dry or semi-dry scrubbing in combination with a filtration system ","kg/tonne melted glass",2.5000000000000001E-3,1.2500000000000001E-2,"Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3",0.08,"Daily average (continuous)","BAT-AELs for metal emissions from the melting furnace in the flat glass sector, with the exception of selenium coloured glasses\n\nThe ranges refer to the sum of metals present in the flue-gases in both solid and gaseous phases.\n\nThe conversion factor reported in Table 2 (2,5 × 10 –3 ) has been applied",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","TRS burner for strong odorous gases ","Air","Nitrogen dioxide","In order to reduce NOx emissions from the incineration of strong odorous gases in a dedicated TRS burner, BAT is to use one or a combination of the techniques given below: (i) Burner/firing optimisation; (ii) Staged incineration","kg NOx/Adt",0.01,0.1,"Green","Continuous",0,0,"Unspecified","Yearly","Where at existing plants a switch to staged incineration is not feasible, emissions levels up to 1 000 mg/Nm3 (corresponding to 0,2 kg/ADt) may occur."]
["Glass","3. Mineral industry","Frits ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes ","Air","Metals (Group 1+ Group 2) ","For downstream dusty processes, BAT is to reduce emissions by using one or a combination of the following techniques: (i) Applying wet milling techniques; (ii) Operating dry milling and dry product packaging under an efficient extraction system in conjunction with a fabric filter; (iii) Applying a filtration system","mg/Nm3","N/A","5","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3","N/A","Daily average (continuous)","The levels refer to the sum of metals present in the waste gas.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Recovery boiler","Air","Nitrogen dioxide","In order to reduce NOx emissions from a recovery boiler, BAT is to use an optimised firing system including one or a combination of the techniques given below: (i) Optimising the recovery boiler by controlling the firing conditions; (ii) Staged injection of spent liquor; (iii) Selective non-catalytic reduction (SNCR)","mg/Nm3",100,350,"Green","Continuous",0,0,0.05,"Daily","For ammonium-based mills, higher emission levels of NOx may occur: up to 580 mg/Nm3 as daily average and up to 450 mg/Nm3 as yearly average."]
["Glass","3. Mineral industry","Container glass","Nitrates in batch formulation","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Primary techniques ","mg/Nm3","N/A",1000,"Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","If nitrates are used in the batch formulation for short campaigns or for melting furnaces with a capacity of < 100 t/day",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Recovery boiler","Air","Nitrogen dioxide","In order to reduce NOx emissions from a recovery boiler, BAT is to use an optimised firing system including one or a combination of the techniques given below: (i) Optimising the recovery boiler by controlling the firing conditions; (ii) Staged injection of spent liquor; (iii) Selective non-catalytic reduction (SNCR)","mg/Nm3",100,270,"Green","Continuous",0,0,0.05,"Yearly","For ammonium-based mills, higher emission levels of NOx may occur: up to 580 mg/Nm3 as daily average and up to 450 mg/Nm3 as yearly average."]
["Glass","3. Mineral industry","Container glass","Nitrates in batch formulation","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Primary techniques ","kg/tonne melted glass","N/A",3,"Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","If nitrates are used in the batch formulation for short campaigns or for melting furnaces with a capacity of < 100 t/day",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Refineries","1. Energy industries","Unspecified","Unspecified","All","Existing","All","Unspecified","Gas-fired combustion unit, with the exception of gas turbines","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion units, BAT is to use one or a combination of the techniques given below: \n\nPrimary techniques:\n(i) Selection or treatment of fuel; (ii) Combustion modifications\n\nSeconary techniques:\n(i) Selective catalytic reduction (SCR) ; (ii) Selective non-catalytic reduction (SNCR), (iii) Low temperature oxidation; (iv) SNOX combined technique\n\n\n","mg/Nm3",30,150,"Amber",0,0,0,0.03,"Monthly ","For an existing unit using high air pre-heat (i.e. > 200 °C) or with H2 content in the fuel gas higher than 50 %, the upper end of the BAT-AEL range is 200 mg/Nm3."]
["Glass","3. Mineral industry","Container glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Combustion modifications, special furnace designs","mg/Nm3","500","800","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The lower value refers to the use of special furnace designs, where applicable\n\nThese values should be reconsidered in the occasion of a normal or complete rebuild of the melting furnace",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Refineries","1. Energy industries","Unspecified","Unspecified","All","Existing","All","Unspecified","Multi-fuel fired combustion unit  with the exception\nof gas turbines","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion units, BAT is to use one or a combination of the techniques given below: \n\nPrimary techniques:\n(i) Selection or treatment of fuel; (ii) Combustion modifications\n\nSeconary techniques:\n(i) Selective catalytic reduction (SCR) ; (ii) Selective non-catalytic reduction (SNCR), (iii) Low temperature oxidation; (iv) SNOX combined technique\n\n\n","mg/Nm3",30,300,"Green","Continuous",0,0,0.03,"Monthly ","For existing units < 100 MW firing fuel oil with a nitrogen content higher than 0,5 % (w/w) or with liquid firing > 50 % or using air preheating, values up to 450 mg/Nm3 may occur\n\nThe lower end of the range can be achieved by using the SCR technique"]
["Glass","3. Mineral industry","Container glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Combustion modifications, special furnace designs","kg/tonne melted glass",0.75,1.2,"Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The conversion factor reported in Table 2 for general cases (1,5 × 10 –3 ) has been applied, with the exception of electric melting (specific cases: 3 × 10 –3 )\n\nThe lower value refers to the use of special furnace designs, where applicable\n\nThese values should be reconsidered in the occasion of a normal or complete rebuild of the melting furnace",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Refineries","1. Energy industries","Unspecified","Unspecified","All","New","All","Unspecified","Gas turbine","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion units, BAT is to use one or a combination of the techniques given below: \n\nPrimary techniques:\n(i) Selection or treatment of fuel; (ii) Combustion modifications\n\nSeconary techniques:\n(i) Selective catalytic reduction (SCR) ; (ii) Selective non-catalytic reduction (SNCR), (iii) Low temperature oxidation; (iv) SNOX combined technique\n\n\n","mg/Nm3",20,50,"Amber",0,0,0,0.15,"Monthly "," BAT-AEL refers to combined emissions from the gas turbine and the supplementary firing recovery boiler, where present.\n\nFor fuel with high H2 content (i.e. above 10 %), the upper end of the range is 75 mg/Nm3. \n\nGas turbine (including combined cycle gas\nturbine — CCGT) and integrated gasification\ncombined cycle turbine (IGCC)) "]
["Glass","3. Mineral industry","Container glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Electric melting","mg/Nm3","N/A",100,"Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Refineries","1. Energy industries","Unspecified","Unspecified","All","New","All","Unspecified","Gas-fired combustion unit, with the exception of gas turbines","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion units, BAT is to use one or a combination of the techniques given below: \n\nPrimary techniques:\n(i) Selection or treatment of fuel; (ii) Combustion modifications\n\nSeconary techniques:\n(i) Selective catalytic reduction (SCR) ; (ii) Selective non-catalytic reduction (SNCR), (iii) Low temperature oxidation; (iv) SNOX combined technique\n\n\n","mg/Nm3",30,100,"Amber",0,0,0,0.03,"Monthly ",0]
["Glass","3. Mineral industry","Container glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Electric melting","kg/tonne melted glass","N/A",0.3,"Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The conversion factor reported in Table 2 for general cases (1,5 × 10 –3 ) has been applied, with the exception of electric melting (specific cases: 3 × 10 –3 )",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Refineries","1. Energy industries","Unspecified","Unspecified","All","Unspecified","All","Unspecified","Gas turbine- Existing","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion units, BAT is to use one or a combination of the techniques given below: \n\nPrimary techniques:\n(i) Selection or treatment of fuel; (ii) Combustion modifications\n\nSeconary techniques:\n(i) Selective catalytic reduction (SCR) ; (ii) Selective non-catalytic reduction (SNCR), (iii) Low temperature oxidation; (iv) SNOX combined technique\n\n\n","mg/Nm3",40,120,"Amber",0,0,0,0.15,"Monthly ","\n\n BAT-AEL refers to combined emissions from the gas turbine and the supplementary firing recovery boiler, where present.\n\nGas turbine (including combined cycle gas\nturbine — CCGT) and integrated gasification\ncombined cycle turbine (IGCC)) "]
["Glass","3. Mineral industry","Container glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Oxy-fuel melting","mg/Nm3","N/A","N/A","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The achievable levels depend on the quality of the natural gas and oxygen available (nitrogen content).",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Woodbased Panels Production","6.   Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Dryer- Directly heated","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from directly heated dryers, BAT is to use technique (i) or technique (i) in combination with technique (ii): (i) Efficient operation of the combustion process using\nair- and fuel-staged combustion, while applying pulverised\ncombustion, fluidised bed boilers or moving\ngrate firing; (ii) Selective non-catalytic reduction (SNCR) by injection\nand reaction with urea or liquid ammonia","mg/Nm3",30,250,"Green","Periodic (at least once every 6 months)",0,0,"Unspecified ","Average over sampling period ",0]
["Glass","3. Mineral industry","Container glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Oxy-fuel melting","kg/tonne melted glass","0.5","0.8","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The achievable levels depend on the quality of the natural gas and oxygen available (nitrogen content)\n\nThe conversion factor reported in Table 2 for general cases (1,5 × 10 –3 ) has been applied, with the exception of electric melting (specific cases: 3 × 10 –3 )",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Container glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Oxy-fuel melting","kg/tonne melted glass","0.5","0.8","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The achievable levels depend on the quality of the natural gas and oxygen available (nitrogen content)\n\nThe conversion factor reported in Table 2 for general cases (1,5 × 10 –3 ) has been applied, with the exception of electric melting (specific cases: 3 × 10 –3 )"]
["Glass","3. Mineral industry","Container glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Secondary techniques","mg/Nm3","N/A",500,"Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Container glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Secondary techniques","mg/Nm3","N/A",500,"Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)",0]
["Glass","3. Mineral industry","Container glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Secondary techniques","kg/tonne melted glass","N/A",0.75,"Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The achievable levels depend on the quality of the natural gas and oxygen available (nitrogen content)",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Container glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Secondary techniques","kg/tonne melted glass","N/A",0.75,"Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The achievable levels depend on the quality of the natural gas and oxygen available (nitrogen content)"]
["Glass","3. Mineral industry","Domestic glass","Nitrates in batch formulation","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","When nitrates are used in the batch formulation, BAT is to reduce NO X emissions by minimising the use of these raw materials, in combination with primary or secondary techniques.","mg/Nm3","500","1500","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","BAT-AELs for NO X emissions from the melting furnace in the domestic glass sector, when nitrates are used in the batch formulation for a limited number of short campaigns or for melting furnaces with a capacity < 100 t/day producing special types of soda-lime glasses (clear/ultra-clear glass or coloured glass using selenium) and other special glasses (i.e. borosilicate, glass ceramics, opal glass, crystal and lead crystal\n\nThis BAT-AEL is for the fuel/ar conventional furnaces",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Domestic glass","Nitrates in batch formulation","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","When nitrates are used in the batch formulation, BAT is to reduce NO X emissions by minimising the use of these raw materials, in combination with primary or secondary techniques.","mg/Nm3","500","1500","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","BAT-AELs for NO X emissions from the melting furnace in the domestic glass sector, when nitrates are used in the batch formulation for a limited number of short campaigns or for melting furnaces with a capacity < 100 t/day producing special types of soda-lime glasses (clear/ultra-clear glass or coloured glass using selenium) and other special glasses (i.e. borosilicate, glass ceramics, opal glass, crystal and lead crystal\n\nThis BAT-AEL is for the fuel/ar conventional furnaces"]
["Glass","3. Mineral industry","Domestic glass","Nitrates in batch formulation","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","When nitrates are used in the batch formulation, BAT is to reduce NO X emissions by minimising the use of these raw materials, in combination with primary or secondary techniques.","kg/tonne melted glass","1.25","3.75","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","BAT-AELs for NO X emissions from the melting furnace in the domestic glass sector, when nitrates are used in the batch formulation for a limited number of short campaigns or for melting furnaces with a capacity < 100 t/day producing special types of soda-lime glasses (clear/ultra-clear glass or coloured glass using selenium) and other special glasses (i.e. borosilicate, glass ceramics, opal glass, crystal and lead crystal\n\nThis BAT-AEL is for the fuel/ar conventional furnaces\n\nThe conversion factor reported in Table 2 for soda-lime glass (2,5 × 10 –3 ) has been applied.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Domestic glass","Nitrates in batch formulation","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","When nitrates are used in the batch formulation, BAT is to reduce NO X emissions by minimising the use of these raw materials, in combination with primary or secondary techniques.","kg/tonne melted glass","1.25","3.75","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","BAT-AELs for NO X emissions from the melting furnace in the domestic glass sector, when nitrates are used in the batch formulation for a limited number of short campaigns or for melting furnaces with a capacity < 100 t/day producing special types of soda-lime glasses (clear/ultra-clear glass or coloured glass using selenium) and other special glasses (i.e. borosilicate, glass ceramics, opal glass, crystal and lead crystal\n\nThis BAT-AEL is for the fuel/ar conventional furnaces\n\nThe conversion factor reported in Table 2 for soda-lime glass (2,5 × 10 –3 ) has been applied."]
["Glass","3. Mineral industry","Domestic glass","Nitrates in batch formulation","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","When nitrates are used in the batch formulation, BAT is to reduce NO X emissions by minimising the use of these raw materials, in combination with primary or secondary techniques.","mg/Nm3","300","500","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","BAT-AELs for NO X emissions from the melting furnace in the domestic glass sector, when nitrates are used in the batch formulation for a limited number of short campaigns or for melting furnaces with a capacity < 100 t/day producing special types of soda-lime glasses (clear/ultra-clear glass or coloured glass using selenium) and other special glasses (i.e. borosilicate, glass ceramics, opal glass, crystal and lead crystal\n\nThis BAT-AEL is for the electric melting furnace",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Domestic glass","Nitrates in batch formulation","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","When nitrates are used in the batch formulation, BAT is to reduce NO X emissions by minimising the use of these raw materials, in combination with primary or secondary techniques.","mg/Nm3","300","500","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","BAT-AELs for NO X emissions from the melting furnace in the domestic glass sector, when nitrates are used in the batch formulation for a limited number of short campaigns or for melting furnaces with a capacity < 100 t/day producing special types of soda-lime glasses (clear/ultra-clear glass or coloured glass using selenium) and other special glasses (i.e. borosilicate, glass ceramics, opal glass, crystal and lead crystal\n\nThis BAT-AEL is for the electric melting furnace"]
["Glass","3. Mineral industry","Domestic glass","Nitrates in batch formulation","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","When nitrates are used in the batch formulation, BAT is to reduce NO X emissions by minimising the use of these raw materials, in combination with primary or secondary techniques.","kg/tonne melted glass","8","10","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","BAT-AELs for NO X emissions from the melting furnace in the domestic glass sector, when nitrates are used in the batch formulation for a limited number of short campaigns or for melting furnaces with a capacity < 100 t/day producing special types of soda-lime glasses (clear/ultra-clear glass or coloured glass using selenium) and other special glasses (i.e. borosilicate, glass ceramics, opal glass, crystal and lead crystal\n\nThis BAT-AEL is for the electric melting furnace",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Domestic glass","Nitrates in batch formulation","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","When nitrates are used in the batch formulation, BAT is to reduce NO X emissions by minimising the use of these raw materials, in combination with primary or secondary techniques.","kg/tonne melted glass","8","10","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","BAT-AELs for NO X emissions from the melting furnace in the domestic glass sector, when nitrates are used in the batch formulation for a limited number of short campaigns or for melting furnaces with a capacity < 100 t/day producing special types of soda-lime glasses (clear/ultra-clear glass or coloured glass using selenium) and other special glasses (i.e. borosilicate, glass ceramics, opal glass, crystal and lead crystal\n\nThis BAT-AEL is for the electric melting furnace"]
["Glass","3. Mineral industry","Domestic glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Combustion modifications, special furnace designs","mg/Nm3","500","1000","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Domestic glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Combustion modifications, special furnace designs","mg/Nm3","500","1000","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)",0]
["Glass","3. Mineral industry","Domestic glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Combustion modifications, special furnace designs","kg/tonne melted glass","1.25","2.5","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","A conversion factor of 2,5 × 10 –3 has been applied for combustion modifications and special furnace designs and a conversion factor of 3 × 10 –3 has been applied for electric melting (see Table 2). However, a case-by-case conversion factor may have to be applied for specific productions.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Domestic glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Combustion modifications, special furnace designs","kg/tonne melted glass","1.25","2.5","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","A conversion factor of 2,5 × 10 –3 has been applied for combustion modifications and special furnace designs and a conversion factor of 3 × 10 –3 has been applied for electric melting (see Table 2). However, a case-by-case conversion factor may have to be applied for specific productions."]
["Glass","3. Mineral industry","Domestic glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Electric melting","mg/Nm3","N/A","100","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Domestic glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Electric melting","mg/Nm3","N/A","100","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)",0]
["Glass","3. Mineral industry","Domestic glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Electric melting","kg/tonne melted glass","N/A","0.3","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","A conversion factor of 2,5 × 10 –3 has been applied for combustion modifications and special furnace designs and a conversion factor of 3 × 10 –3 has been applied for electric melting (see Table 2). However, a case-by-case conversion factor may have to be applied for specific productions.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Domestic glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Electric melting","kg/tonne melted glass","N/A","0.3","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","A conversion factor of 2,5 × 10 –3 has been applied for combustion modifications and special furnace designs and a conversion factor of 3 × 10 –3 has been applied for electric melting (see Table 2). However, a case-by-case conversion factor may have to be applied for specific productions."]
["Glass","3. Mineral industry","Domestic glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Oxy-fuel melting","mg/Nm3","N/A","N/A","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The achievable levels depend on the quality of the natural gas and oxygen available (nitrogen content).",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Domestic glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Oxy-fuel melting","mg/Nm3","N/A","N/A","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The achievable levels depend on the quality of the natural gas and oxygen available (nitrogen content)."]
["Glass","3. Mineral industry","Domestic glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Oxy-fuel melting","kg/tonne melted glass","0.5","1.5","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","A conversion factor of 2,5 × 10 –3 has been applied for combustion modifications and special furnace designs and a conversion factor of 3 × 10 –3 has been applied for electric melting (see Table 2). However, a case-by-case conversion factor may have to be applied for specific productions.\n\nThe achievable levels depend on the quality of the natural gas and oxygen available (nitrogen content).",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Domestic glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Oxy-fuel melting","kg/tonne melted glass","0.5","1.5","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","A conversion factor of 2,5 × 10 –3 has been applied for combustion modifications and special furnace designs and a conversion factor of 3 × 10 –3 has been applied for electric melting (see Table 2). However, a case-by-case conversion factor may have to be applied for specific productions.\n\nThe achievable levels depend on the quality of the natural gas and oxygen available (nitrogen content)."]
["Glass","3. Mineral industry","Filament glass fibre","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Combustion modifications","mg/Nm3","600","1000","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Filament glass fibre","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Combustion modifications","mg/Nm3","600","1000","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)",0]
["Glass","3. Mineral industry","Filament glass fibre","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Combustion modifications","kg/tonne melted glass","2.7","4.5","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The conversion factor reported in Table 2 (4,5 × 10 –3 ) has been applied.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Filament glass fibre","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Combustion modifications","kg/tonne melted glass","2.7","4.5","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The conversion factor reported in Table 2 (4,5 × 10 –3 ) has been applied."]
["Glass","3. Mineral industry","Filament glass fibre","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Oxy-fuel melting","mg/Nm3","N/A","N/A","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The achievable levels depend on the quality of the natural gas and oxygen available (nitrogen content).",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Filament glass fibre","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Oxy-fuel melting","mg/Nm3","N/A","N/A","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The achievable levels depend on the quality of the natural gas and oxygen available (nitrogen content)."]
["Glass","3. Mineral industry","Filament glass fibre","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Oxy-fuel melting","kg/tonne melted glass","0.5","1.5","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The achievable levels depend on the quality of the natural gas and oxygen available (nitrogen content).",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Filament glass fibre","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Oxy-fuel melting","kg/tonne melted glass","0.5","1.5","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The achievable levels depend on the quality of the natural gas and oxygen available (nitrogen content)."]
["Glass","3. Mineral industry","Flat glass","Nitrates in batch formulation","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Primary techniques ","mg/Nm3","N/A",1200,"Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","BAT-AEL for NO X emissions from the melting furnace in the flat glass sector, when nitrates are used in the batch formulation for the production of special glasses in a limited number of short campaigns",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Flat glass","Nitrates in batch formulation","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Primary techniques ","mg/Nm3","N/A",1200,"Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","BAT-AEL for NO X emissions from the melting furnace in the flat glass sector, when nitrates are used in the batch formulation for the production of special glasses in a limited number of short campaigns"]
["Glass","3. Mineral industry","Flat glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Combustion modifications, Fenix process","mg/Nm3",700,800,"Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","Higher emission levels are expected when nitrates are used occasionally for the production of special glasses.\n\nThe lower levels of the range are associated with the application of the Fenix process",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Flat glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Combustion modifications, Fenix process","mg/Nm3",700,800,"Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","Higher emission levels are expected when nitrates are used occasionally for the production of special glasses.\n\nThe lower levels of the range are associated with the application of the Fenix process"]
["Glass","3. Mineral industry","Flat glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Combustion modifications, Fenix process","kg/tonne melted glass",1.75,2,"Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","Higher emission levels are expected when nitrates are used occasionally for the production of special glasses.\n\nThe lower levels of the range are associated with the application of the Fenix process\n\nThe conversion factor reported in Table 2 (2,5 × 10 –3 ) has been applied",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Flat glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Combustion modifications, Fenix process","kg/tonne melted glass",1.75,2,"Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","Higher emission levels are expected when nitrates are used occasionally for the production of special glasses.\n\nThe lower levels of the range are associated with the application of the Fenix process\n\nThe conversion factor reported in Table 2 (2,5 × 10 –3 ) has been applied"]
["Glass","3. Mineral industry","Flat glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Oxy-fuel melting","mg/Nm3","N/A","N/A","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","Higher emission levels are expected when nitrates are used occasionally for the production of special glasses.\n\nThe achievable levels depend on the quality of the natural gas and oxygen available (nitrogen content).",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Flat glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Oxy-fuel melting","mg/Nm3","N/A","N/A","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","Higher emission levels are expected when nitrates are used occasionally for the production of special glasses.\n\nThe achievable levels depend on the quality of the natural gas and oxygen available (nitrogen content)."]
["Glass","3. Mineral industry","Flat glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Oxy-fuel melting","kg/tonne melted glass","1.25","2.0","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","Higher emission levels are expected when nitrates are used occasionally for the production of special glasses.\n\nThe achievable levels depend on the quality of the natural gas and oxygen available (nitrogen content).\n\nThe conversion factor reported in Table 2 (2,5 × 10 –3 ) has been applied.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Flat glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Oxy-fuel melting","kg/tonne melted glass","1.25","2.0","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","Higher emission levels are expected when nitrates are used occasionally for the production of special glasses.\n\nThe achievable levels depend on the quality of the natural gas and oxygen available (nitrogen content).\n\nThe conversion factor reported in Table 2 (2,5 × 10 –3 ) has been applied."]
["Glass","3. Mineral industry","Flat glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Secondary techniques","mg/Nm3",400,700,"Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","Higher emission levels are expected when nitrates are used occasionally for the production of special glasses.\n\nThe higher levels of the range are associated with existing plants until a normal or complete rebuild of the melting furnace. The lower levels are associated with newer/retrofitted plants.\n",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Flat glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Secondary techniques","mg/Nm3",400,700,"Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","Higher emission levels are expected when nitrates are used occasionally for the production of special glasses.\n\nThe higher levels of the range are associated with existing plants until a normal or complete rebuild of the melting furnace. The lower levels are associated with newer/retrofitted plants.\n"]
["Glass","3. Mineral industry","Flat glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Secondary techniques","kg/tonne melted glass",1,1.75,"Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","Higher emission levels are expected when nitrates are used occasionally for the production of special glasses.\n\nThe higher levels of the range are associated with existing plants until a normal or complete rebuild of the melting furnace. The lower levels are associated with newer/retrofitted plants.\n",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Flat glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Secondary techniques","kg/tonne melted glass",1,1.75,"Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","Higher emission levels are expected when nitrates are used occasionally for the production of special glasses.\n\nThe higher levels of the range are associated with existing plants until a normal or complete rebuild of the melting furnace. The lower levels are associated with newer/retrofitted plants.\n"]
["Glass","3. Mineral industry","Frits ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Primary techniques: Fuel/air, fuel/oxygen-enriched air combustion, with nitrates ","mg/Nm3","N/A","1600","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The ranges take into account the combination of flue-gases from furnaces applying different melting techniques and producing a variety of frit types, with or without nitrates in the batch formulations, which may be conveyed to a single stack, precluding the possibility of characterising each applied melting technique and the different products.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Frits ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Primary techniques: Fuel/air, fuel/oxygen-enriched air combustion, with nitrates ","mg/Nm3","N/A","1600","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The ranges take into account the combination of flue-gases from furnaces applying different melting techniques and producing a variety of frit types, with or without nitrates in the batch formulations, which may be conveyed to a single stack, precluding the possibility of characterising each applied melting technique and the different products."]
["Glass","3. Mineral industry","Frits ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Primary techniques: Fuel/air, fuel/oxygen-enriched air combustion, with nitrates ","kg/tonne melted glass","N/A","12","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The ranges take into account the combination of flue-gases from furnaces applying different melting techniques and producing a variety of frit types, with or without nitrates in the batch formulations, which may be conveyed to a single stack, precluding the possibility of characterising each applied melting technique and the different products.\n\nThe conversion factors of 5 × 10 –3 and 7,5 × 10 –3 have been used for the determination of the lower and higher values of the range. However, a case-by-case conversion factor may have to be applied based on the type of combustion",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Frits ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Primary techniques: Fuel/air, fuel/oxygen-enriched air combustion, with nitrates ","kg/tonne melted glass","N/A","12","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The ranges take into account the combination of flue-gases from furnaces applying different melting techniques and producing a variety of frit types, with or without nitrates in the batch formulations, which may be conveyed to a single stack, precluding the possibility of characterising each applied melting technique and the different products.\n\nThe conversion factors of 5 × 10 –3 and 7,5 × 10 –3 have been used for the determination of the lower and higher values of the range. However, a case-by-case conversion factor may have to be applied based on the type of combustion"]
["Glass","3. Mineral industry","Frits ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Primary techniques: Fuel/air, fuel/oxygen-enriched air combustion, without nitrates ","mg/Nm3","500","1000","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The ranges take into account the combination of flue-gases from furnaces applying different melting techniques and producing a variety of frit types, with or without nitrates in the batch formulations, which may be conveyed to a single stack, precluding the possibility of characterising each applied melting technique and the different products.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Frits ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Primary techniques: Fuel/air, fuel/oxygen-enriched air combustion, without nitrates ","mg/Nm3","500","1000","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The ranges take into account the combination of flue-gases from furnaces applying different melting techniques and producing a variety of frit types, with or without nitrates in the batch formulations, which may be conveyed to a single stack, precluding the possibility of characterising each applied melting technique and the different products."]
["Glass","3. Mineral industry","Frits ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Primary techniques: Fuel/air, fuel/oxygen-enriched air combustion, without nitrates ","kg/tonne melted glass","2.5","7.5","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The ranges take into account the combination of flue-gases from furnaces applying different melting techniques and producing a variety of frit types, with or without nitrates in the batch formulations, which may be conveyed to a single stack, precluding the possibility of characterising each applied melting technique and the different products.\n\nThe conversion factors of 5 × 10 –3 and 7,5 × 10 –3 have been used for the determination of the lower and higher values of the range. However, a case-by-case conversion factor may have to be applied based on the type of combustion",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Frits ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Primary techniques: Fuel/air, fuel/oxygen-enriched air combustion, without nitrates ","kg/tonne melted glass","2.5","7.5","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The ranges take into account the combination of flue-gases from furnaces applying different melting techniques and producing a variety of frit types, with or without nitrates in the batch formulations, which may be conveyed to a single stack, precluding the possibility of characterising each applied melting technique and the different products.\n\nThe conversion factors of 5 × 10 –3 and 7,5 × 10 –3 have been used for the determination of the lower and higher values of the range. However, a case-by-case conversion factor may have to be applied based on the type of combustion"]
["Glass","3. Mineral industry","Frits ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Primary techniques: Oxy fuel firing, with use nitrates","kg/tonne melted glass","5","10","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The ranges take into account the combination of flue-gases from furnaces applying different melting techniques and producing a variety of frit types, with or without nitrates in the batch formulations, which may be conveyed to a single stack, precluding the possibility of characterising each applied melting technique and the different products.\n\nThe conversion factors of 5 × 10 –3 and 7,5 × 10 –3 have been used for the determination of the lower and higher values of the range. However, a case-by-case conversion factor may have to be applied based on the type of combustion",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Frits ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Primary techniques: Oxy fuel firing, with use nitrates","kg/tonne melted glass","5","10","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The ranges take into account the combination of flue-gases from furnaces applying different melting techniques and producing a variety of frit types, with or without nitrates in the batch formulations, which may be conveyed to a single stack, precluding the possibility of characterising each applied melting technique and the different products.\n\nThe conversion factors of 5 × 10 –3 and 7,5 × 10 –3 have been used for the determination of the lower and higher values of the range. However, a case-by-case conversion factor may have to be applied based on the type of combustion"]
["Glass","3. Mineral industry","Frits ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Primary techniques: Oxy fuel firing, without nitrates","kg/tonne melted glass","2.5","5","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The ranges take into account the combination of flue-gases from furnaces applying different melting techniques and producing a variety of frit types, with or without nitrates in the batch formulations, which may be conveyed to a single stack, precluding the possibility of characterising each applied melting technique and the different products.\n\nThe conversion factors of 5 × 10 –3 and 7,5 × 10 –3 have been used for the determination of the lower and higher values of the range. However, a case-by-case conversion factor may have to be applied based on the type of combustion",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Frits ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Primary techniques: Oxy fuel firing, without nitrates","kg/tonne melted glass","2.5","5","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The ranges take into account the combination of flue-gases from furnaces applying different melting techniques and producing a variety of frit types, with or without nitrates in the batch formulations, which may be conveyed to a single stack, precluding the possibility of characterising each applied melting technique and the different products.\n\nThe conversion factors of 5 × 10 –3 and 7,5 × 10 –3 have been used for the determination of the lower and higher values of the range. However, a case-by-case conversion factor may have to be applied based on the type of combustion"]
["Glass","3. Mineral industry","HTIW wools","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Lubricant burn-off oven ","Air","Nitrogen dioxide","BAT is to reduce NO X emissions from the lubricant burn-off oven by applying combustion control and/or modifications","mg/Nm3","100","200","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3","N/A","Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","HTIW wools","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Lubricant burn-off oven ","Air","Nitrogen dioxide","BAT is to reduce NO X emissions from the lubricant burn-off oven by applying combustion control and/or modifications","mg/Nm3","100","200","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3","N/A","Daily average (continuous)",0]
["Glass","3. Mineral industry","Mineral wool","Glass wool","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","All types of furnaces","kg/tonne melted glass","1.0","1.25","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The conversion factors of 2 × 10 –3 for glass wool and 2,5 × 10 –3 for stone wool have been used (see Table 2).",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Mineral wool","Glass wool","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","All types of furnaces","kg/tonne melted glass","1.0","1.25","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The conversion factors of 2 × 10 –3 for glass wool and 2,5 × 10 –3 for stone wool have been used (see Table 2)."]
["Glass","3. Mineral industry","Mineral wool","Glass wool","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Fuel/air and Electric furnaces","mg/Nm3","200","500","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Mineral wool","Glass wool","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Fuel/air and Electric furnaces","mg/Nm3","200","500","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)",0]
["Glass","3. Mineral industry","Mineral wool","Glass wool","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Fuel/air and Electric furnaces","kg/tonne melted glass","0.4","1.0","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The conversion factors of 2 × 10 –3 for glass wool and 2,5 × 10 –3 for stone wool have been used",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Mineral wool","Glass wool","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Fuel/air and Electric furnaces","kg/tonne melted glass","0.4","1.0","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The conversion factors of 2 × 10 –3 for glass wool and 2,5 × 10 –3 for stone wool have been used"]
["Glass","3. Mineral industry","Mineral wool","Glass wool","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Oxy-fuel melting","mg/Nm3","N/A","N/A","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The achievable levels depend on the quality of the natural gas and oxygen available (nitrogen content).",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Mineral wool","Glass wool","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Oxy-fuel melting","mg/Nm3","N/A","N/A","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The achievable levels depend on the quality of the natural gas and oxygen available (nitrogen content)."]
["Glass","3. Mineral industry","Mineral wool","Glass wool","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Oxy-fuel melting","kg/tonne melted glass","N/A","N/A","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The conversion factors of 2 × 10 –3 for glass wool and 2,5 × 10 –3 for stone wool have been used\n\nThe achievable levels depend on the quality of the natural gas and oxygen available (nitrogen content).",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Mineral wool","Glass wool","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Oxy-fuel melting","kg/tonne melted glass","N/A","N/A","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The conversion factors of 2 × 10 –3 for glass wool and 2,5 × 10 –3 for stone wool have been used\n\nThe achievable levels depend on the quality of the natural gas and oxygen available (nitrogen content)."]
["Glass","3. Mineral industry","Mineral wool","Nitrates in batch formulation","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Minimisation of nitrate input in the batch formulation, combined with primary techniques","mg/Nm3","500","700","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Mineral wool","Nitrates in batch formulation","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Minimisation of nitrate input in the batch formulation, combined with primary techniques","mg/Nm3","500","700","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)",0]
["Glass","3. Mineral industry","Mineral wool","Nitrates in batch formulation","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Minimisation of nitrate input in the batch formulation, combined with primary techniques","kg/tonne melted glass","1.0","1.4","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The conversion factor of 2 × 10 –3 has been used\n\nThe lower levels of the ranges are associated with the application of oxy-fuel melting.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Mineral wool","Nitrates in batch formulation","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Minimisation of nitrate input in the batch formulation, combined with primary techniques","kg/tonne melted glass","1.0","1.4","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The conversion factor of 2 × 10 –3 has been used\n\nThe lower levels of the ranges are associated with the application of oxy-fuel melting."]
["Glass","3. Mineral industry","Mineral wool","Stone wool","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","All types of furnaces","mg/Nm3","400","500","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Mineral wool","Stone wool","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","All types of furnaces","mg/Nm3","400","500","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)",0]
["Glass","3. Mineral industry","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes- Curing oven emissions ","Air","Nitrogen dioxide","BAT is to reduce emissions from downstream processes by using one or a combination of the following techniques: (i) Impact jets and cyclones; (ii) Wet scrubbers; (iii) Wet electrostatic precipitators; (iv) Stone wool filters; (v) Waste gas incineration","mg/Nm3","100","200","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3","N/A","Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes- Curing oven emissions ","Air","Nitrogen dioxide","BAT is to reduce emissions from downstream processes by using one or a combination of the following techniques: (i) Impact jets and cyclones; (ii) Wet scrubbers; (iii) Wet electrostatic precipitators; (iv) Stone wool filters; (v) Waste gas incineration","mg/Nm3","100","200","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3","N/A","Daily average (continuous)",0]
["Glass","3. Mineral industry","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes- Curing oven emissions ","Air","Nitrogen dioxide","BAT is to reduce emissions from downstream processes by using one or a combination of the following techniques: (i) Impact jets and cyclones; (ii) Wet scrubbers; (iii) Wet electrostatic precipitators; (iv) Stone wool filters; (v) Waste gas incineration","kg/tonne melted glass","N/A","1","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3","N/A","Daily average (continuous)","The specific mass emissions refer to 1 tonne of produced glass",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes- Curing oven emissions ","Air","Nitrogen dioxide","BAT is to reduce emissions from downstream processes by using one or a combination of the following techniques: (i) Impact jets and cyclones; (ii) Wet scrubbers; (iii) Wet electrostatic precipitators; (iv) Stone wool filters; (v) Waste gas incineration","kg/tonne melted glass","N/A","1","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3","N/A","Daily average (continuous)","The specific mass emissions refer to 1 tonne of produced glass"]
["Glass","3. Mineral industry","Special glass ","Nitrates in batch formulation","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Minimisation of nitrate input in the batch formulation combined with primary or secondary techniques","mg/Nm3","500","1000","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The lower levels are associated with the use of electric melting.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Special glass ","Nitrates in batch formulation","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Minimisation of nitrate input in the batch formulation combined with primary or secondary techniques","mg/Nm3","500","1000","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The lower levels are associated with the use of electric melting."]
["Glass","3. Mineral industry","Special glass ","Nitrates in batch formulation","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Minimisation of nitrate input in the batch formulation combined with primary or secondary techniques","kg/tonne melted glass","1","6","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The lower levels are associated with the use of electric melting.\n\nThe conversion factors of 2,5 × 10 –3 and 6,5 × 10 –3 have been used for the determination of the lower and upper value of the BAT- AEL range respectively, with values being approximated. A case-by-case conversion factor may have to be applied based on the type of production.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Special glass ","Nitrates in batch formulation","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Minimisation of nitrate input in the batch formulation combined with primary or secondary techniques","kg/tonne melted glass","1","6","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The lower levels are associated with the use of electric melting.\n\nThe conversion factors of 2,5 × 10 –3 and 6,5 × 10 –3 have been used for the determination of the lower and upper value of the BAT- AEL range respectively, with values being approximated. A case-by-case conversion factor may have to be applied based on the type of production."]
["Glass","3. Mineral industry","Special glass ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Combustion modifications","mg/Nm3","600","800","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Special glass ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Combustion modifications","mg/Nm3","600","800","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)",0]
["Glass","3. Mineral industry","Special glass ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Combustion modifications","kg/tonne melted glass","1.5","3.2","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The conversion factors of 2,5 × 10 –3 and 4 × 10 –3 have been used for the determination of the lower and upper value of the BAT-AEL range (see Table 2), with some values being approximated. However, a case-by-case conversion factor needs to be applied based on the type of production.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Special glass ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Combustion modifications","kg/tonne melted glass","1.5","3.2","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The conversion factors of 2,5 × 10 –3 and 4 × 10 –3 have been used for the determination of the lower and upper value of the BAT-AEL range (see Table 2), with some values being approximated. However, a case-by-case conversion factor needs to be applied based on the type of production."]
["Glass","3. Mineral industry","Special glass ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Electric melting","mg/Nm3","N/A","100","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Special glass ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Electric melting","mg/Nm3","N/A","100","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)",0]
["Glass","3. Mineral industry","Special glass ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Electric melting","kg/tonne melted glass","0.25","0.4","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The conversion factors of 2,5 × 10 –3 and 4 × 10 –3 have been used for the determination of the lower and upper value of the BAT-AEL range (see Table 2), with some values being approximated. However, a case-by-case conversion factor needs to be applied based on the type of production.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Special glass ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Electric melting","kg/tonne melted glass","0.25","0.4","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The conversion factors of 2,5 × 10 –3 and 4 × 10 –3 have been used for the determination of the lower and upper value of the BAT-AEL range (see Table 2), with some values being approximated. However, a case-by-case conversion factor needs to be applied based on the type of production."]
["Glass","3. Mineral industry","Special glass ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Oxy-fuel melting","mg/Nm3","N/A","N/A","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The higher values are related to a special production of borosilicate glass tubes for pharmaceutical use.\n\nThe achievable levels depend on the quality of the natural gas and oxygen available (nitrogen content).",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Special glass ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Oxy-fuel melting","mg/Nm3","N/A","N/A","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The higher values are related to a special production of borosilicate glass tubes for pharmaceutical use.\n\nThe achievable levels depend on the quality of the natural gas and oxygen available (nitrogen content)."]
["Glass","3. Mineral industry","Special glass ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Oxy-fuel melting","kg/tonne melted glass","1","3","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The conversion factors of 2,5 × 10 –3 and 4 × 10 –3 have been used for the determination of the lower and upper value of the BAT-AEL range (see Table 2), with some values being approximated. However, a case-by-case conversion factor needs to be applied based on the type of production.\n\nThe higher values are related to a special production of borosilicate glass tubes for pharmaceutical use.\n\nThe achievable levels depend on the quality of the natural gas and oxygen available (nitrogen content).",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Special glass ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Oxy-fuel melting","kg/tonne melted glass","1","3","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The conversion factors of 2,5 × 10 –3 and 4 × 10 –3 have been used for the determination of the lower and upper value of the BAT-AEL range (see Table 2), with some values being approximated. However, a case-by-case conversion factor needs to be applied based on the type of production.\n\nThe higher values are related to a special production of borosilicate glass tubes for pharmaceutical use.\n\nThe achievable levels depend on the quality of the natural gas and oxygen available (nitrogen content)."]
["Glass","3. Mineral industry","Special glass ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Secondary techniques","mg/Nm3","N/A","500","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Special glass ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Secondary techniques","mg/Nm3","N/A","500","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)",0]
["Glass","3. Mineral industry","Special glass ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Secondary techniques","kg/tonne melted glass","1","3","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The conversion factors of 2,5 × 10 –3 and 4 × 10 –3 have been used for the determination of the lower and upper value of the BAT-AEL range (see Table 2), with some values being approximated. However, a case-by-case conversion factor needs to be applied based on the type of production.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Special glass ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Nitrogen dioxide","Secondary techniques","kg/tonne melted glass","1","3","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The conversion factors of 2,5 × 10 –3 and 4 × 10 –3 have been used for the determination of the lower and upper value of the BAT-AEL range (see Table 2), with some values being approximated. However, a case-by-case conversion factor needs to be applied based on the type of production."]
["Glass","3. Mineral industry","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes- Curing oven emissions ","Air","Phenol","BAT is to reduce emissions from downstream processes by using one or a combination of the following techniques: (i) Impact jets and cyclones; (ii) Wet scrubbers; (iii) Wet electrostatic precipitators; (iv) Stone wool filters; (v) Waste gas incineration","mg/Nm3","2","5","Amber",0,"273.15","101.3","N/A","Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes- Curing oven emissions ","Air","Phenol","BAT is to reduce emissions from downstream processes by using one or a combination of the following techniques: (i) Impact jets and cyclones; (ii) Wet scrubbers; (iii) Wet electrostatic precipitators; (iv) Stone wool filters; (v) Waste gas incineration","mg/Nm3","2","5","Amber",0,"273.15","101.3","N/A","Daily average (continuous)",0]
["Glass","3. Mineral industry","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes- Curing oven emissions ","Air","Phenol","BAT is to reduce emissions from downstream processes by using one or a combination of the following techniques: (i) Impact jets and cyclones; (ii) Wet scrubbers; (iii) Wet electrostatic precipitators; (iv) Stone wool filters; (v) Waste gas incineration","kg/tonne melted glass","N/A","0.03","Amber",0,"273.15","101.3","N/A","Daily average (continuous)","The specific mass emissions refer to 1 tonne of produced glass",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes- Curing oven emissions ","Air","Phenol","BAT is to reduce emissions from downstream processes by using one or a combination of the following techniques: (i) Impact jets and cyclones; (ii) Wet scrubbers; (iii) Wet electrostatic precipitators; (iv) Stone wool filters; (v) Waste gas incineration","kg/tonne melted glass","N/A","0.03","Amber",0,"273.15","101.3","N/A","Daily average (continuous)","The specific mass emissions refer to 1 tonne of produced glass"]
["Glass","3. Mineral industry","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes- Forming area ","Air","Phenol","BAT is to reduce emissions from downstream processes by using one or a combination of the following techniques: (i) Impact jets and cyclones; (ii) Wet scrubbers; (iii) Wet electrostatic precipitators; (iv) Stone wool filters; (v) Waste gas incineration","mg/Nm3","5","10","Amber",0,"273.15","101.3","N/A","Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes- Forming area ","Air","Phenol","BAT is to reduce emissions from downstream processes by using one or a combination of the following techniques: (i) Impact jets and cyclones; (ii) Wet scrubbers; (iii) Wet electrostatic precipitators; (iv) Stone wool filters; (v) Waste gas incineration","mg/Nm3","5","10","Amber",0,"273.15","101.3","N/A","Daily average (continuous)",0]
["Glass","3. Mineral industry","Domestic glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Selenium and compounds, except hydrogen selenide (as Se)","When selenium compounds are used for decolourising the glass, BAT is to reduce selenium emissions from the melting furnace by using one or a combination of the following techniques: (i) Minimising the use of selenium compounds in the batch formulation, through a suitable selection of the raw materials; (ii) Dry or semi-dry scrubbing, in combination with a filtration system","mg/Nm3","N/A","1","Amber",0,"273.15","101.3",0.08,"Daily average (continuous)","The values refer to the sum of selenium present in the flue-gases in both solid and gaseous phases.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Domestic glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Selenium and compounds, except hydrogen selenide (as Se)","When selenium compounds are used for decolourising the glass, BAT is to reduce selenium emissions from the melting furnace by using one or a combination of the following techniques: (i) Minimising the use of selenium compounds in the batch formulation, through a suitable selection of the raw materials; (ii) Dry or semi-dry scrubbing, in combination with a filtration system","mg/Nm3","N/A","1","Amber",0,"273.15","101.3",0.08,"Daily average (continuous)","The values refer to the sum of selenium present in the flue-gases in both solid and gaseous phases."]
["Glass","3. Mineral industry","Flat glass","Colored Glass","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Selenium and compounds, except hydrogen selenide (as Se)","When selenium compounds are used for colouring the glass, BAT is to reduce selenium emissions from the melting furnace by using one or a combination of the following techniques: (i) Minimising the evaporation of selenium from the batch composition by selecting raw material with a higher retention efficiency in the glass and reduced volatilisation; (ii) Applying a filtration system; (iii) Applying a dry or semi-dry scrubbing in combination with a filtration system","mg/Nm3","1","3","Amber",0,"273.15","101.3",0.08,"Daily average (continuous)","BAT-AELs for selenium emissions from the melting furnace in the flat glass sector for the production of coloured glass\n\nThe lower levels correspond to conditions where the reduction of Se emissions is a priority over a lower production of solid waste from filter dust. In this case, a high stoichiometric ratio (reagent/pollutant) is applied and a significant solid waste stream is generated.\n\n",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Flat glass","Colored Glass","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Selenium and compounds, except hydrogen selenide (as Se)","When selenium compounds are used for colouring the glass, BAT is to reduce selenium emissions from the melting furnace by using one or a combination of the following techniques: (i) Minimising the evaporation of selenium from the batch composition by selecting raw material with a higher retention efficiency in the glass and reduced volatilisation; (ii) Applying a filtration system; (iii) Applying a dry or semi-dry scrubbing in combination with a filtration system","mg/Nm3","1","3","Amber",0,"273.15","101.3",0.08,"Daily average (continuous)","BAT-AELs for selenium emissions from the melting furnace in the flat glass sector for the production of coloured glass\n\nThe lower levels correspond to conditions where the reduction of Se emissions is a priority over a lower production of solid waste from filter dust. In this case, a high stoichiometric ratio (reagent/pollutant) is applied and a significant solid waste stream is generated.\n\n"]
["Glass","3. Mineral industry","Container glass","Unspecified","Unspecified","Unspecified","Natural gas ","Unspecified","Melting furnace","Air","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce Sox emissions from the melting furnace by using one or a combination of the following techniques: (i) Dry or semi-dry scrubbing with a filtration system; (ii) minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance; (iii) Use of low sulphur content fuels","mg/Nm3","200","500","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","For special types of coloured glasses (e.g. reduced green glasses), concerns related to the achievable emission levels may require investigating the sulphur balance. Values reported in the table may be difficult to achieve in combination with filter dust recycling and the rate of recycling of external cullet.\n\nThe lower levels are associated with conditions where the reduction of SO X is a high priority over a lower production of solid waste corresponding to the sulphate-rich filter dust.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Container glass","Unspecified","Unspecified","Unspecified","Natural gas ","Unspecified","Melting furnace","Air","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce Sox emissions from the melting furnace by using one or a combination of the following techniques: (i) Dry or semi-dry scrubbing with a filtration system; (ii) minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance; (iii) Use of low sulphur content fuels","mg/Nm3","200","500","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","For special types of coloured glasses (e.g. reduced green glasses), concerns related to the achievable emission levels may require investigating the sulphur balance. Values reported in the table may be difficult to achieve in combination with filter dust recycling and the rate of recycling of external cullet.\n\nThe lower levels are associated with conditions where the reduction of SO X is a high priority over a lower production of solid waste corresponding to the sulphate-rich filter dust."]
["Glass","3. Mineral industry","Container glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes","Air","Sulphur Dioxide (24 Hour Mean)","When SO 3 is used for surface treatment operations, BAT is to reduce SO X emissions by using one or a combination of the following techniques: (i) minimising the product losses by ensuring a good sealing of the application system; (ii) applying a secondary technique, e.g. wet scrubbing","mg/Nm3","100","200","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3","N/A","Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Container glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes","Air","Sulphur Dioxide (24 Hour Mean)","When SO 3 is used for surface treatment operations, BAT is to reduce SO X emissions by using one or a combination of the following techniques: (i) minimising the product losses by ensuring a good sealing of the application system; (ii) applying a secondary technique, e.g. wet scrubbing","mg/Nm3","100","200","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3","N/A","Daily average (continuous)",0]
["Glass","3. Mineral industry","Domestic glass","Unspecified","Unspecified","Unspecified","Electric melting","Unspecified","Melting furnace","Air","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance; (ii) Use of low sulphur content; (iii) Dry or semi-dry scrubbing in combination with a filtration system ","mg/Nm3","N/A","100","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Domestic glass","Unspecified","Unspecified","Unspecified","Electric melting","Unspecified","Melting furnace","Air","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance; (ii) Use of low sulphur content; (iii) Dry or semi-dry scrubbing in combination with a filtration system ","mg/Nm3","N/A","100","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)",0]
["Glass","3. Mineral industry","Domestic glass","Unspecified","Unspecified","Unspecified","Electric melting","Unspecified","Melting furnace","Air","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance; (ii) Use of low sulphur content; (iii) Dry or semi-dry scrubbing in combination with a filtration system ","kg/tonne melted glass","N/A","0.25","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","A conversion factor of 2,5 × 10 –3 has been applied (see Table 2). However, a case-by-case conversion factor may have to be applied for specific productions.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Domestic glass","Unspecified","Unspecified","Unspecified","Electric melting","Unspecified","Melting furnace","Air","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance; (ii) Use of low sulphur content; (iii) Dry or semi-dry scrubbing in combination with a filtration system ","kg/tonne melted glass","N/A","0.25","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","A conversion factor of 2,5 × 10 –3 has been applied (see Table 2). However, a case-by-case conversion factor may have to be applied for specific productions."]
["Glass","3. Mineral industry","Domestic glass","Unspecified","Unspecified","Unspecified","Fuel oil","Unspecified","Melting furnace","Air","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance; (ii) Use of low sulphur content; (iii) Dry or semi-dry scrubbing in combination with a filtration system ","mg/Nm3","N/A","1000","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The levels are related to the use of 1 % sulphur fuel oil in combination with secondary abatement techniques.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Domestic glass","Unspecified","Unspecified","Unspecified","Fuel oil","Unspecified","Melting furnace","Air","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance; (ii) Use of low sulphur content; (iii) Dry or semi-dry scrubbing in combination with a filtration system ","mg/Nm3","N/A","1000","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The levels are related to the use of 1 % sulphur fuel oil in combination with secondary abatement techniques."]
["Glass","3. Mineral industry","Domestic glass","Unspecified","Unspecified","Unspecified","Fuel oil","Unspecified","Melting furnace","Air","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance; (ii) Use of low sulphur content; (iii) Dry or semi-dry scrubbing in combination with a filtration system ","kg/tonne melted glass","N/A","2.5","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The levels are related to the use of 1 % sulphur fuel oil in combination with secondary abatement techniques.\n\nA conversion factor of 2,5 × 10 –3 has been applied (see Table 2). However, a case-by-case conversion factor may have to be applied for specific productions.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Domestic glass","Unspecified","Unspecified","Unspecified","Fuel oil","Unspecified","Melting furnace","Air","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance; (ii) Use of low sulphur content; (iii) Dry or semi-dry scrubbing in combination with a filtration system ","kg/tonne melted glass","N/A","2.5","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The levels are related to the use of 1 % sulphur fuel oil in combination with secondary abatement techniques.\n\nA conversion factor of 2,5 × 10 –3 has been applied (see Table 2). However, a case-by-case conversion factor may have to be applied for specific productions."]
["Glass","3. Mineral industry","Domestic glass","Unspecified","Unspecified","Unspecified","Natural gas ","Unspecified","Melting furnace","Air","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance; (ii) Use of low sulphur content; (iii) Dry or semi-dry scrubbing in combination with a filtration system ","mg/Nm3","200","300","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Domestic glass","Unspecified","Unspecified","Unspecified","Natural gas ","Unspecified","Melting furnace","Air","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance; (ii) Use of low sulphur content; (iii) Dry or semi-dry scrubbing in combination with a filtration system ","mg/Nm3","200","300","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)",0]
["Glass","3. Mineral industry","Domestic glass","Unspecified","Unspecified","Unspecified","Natural gas ","Unspecified","Melting furnace","Air","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance; (ii) Use of low sulphur content; (iii) Dry or semi-dry scrubbing in combination with a filtration system ","kg/tonne melted glass","0.5","0.75","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","A conversion factor of 2,5 × 10 –3 has been applied (see Table 2). However, a case-by-case conversion factor may have to be applied for specific productions.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Domestic glass","Unspecified","Unspecified","Unspecified","Natural gas ","Unspecified","Melting furnace","Air","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance; (ii) Use of low sulphur content; (iii) Dry or semi-dry scrubbing in combination with a filtration system ","kg/tonne melted glass","0.5","0.75","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","A conversion factor of 2,5 × 10 –3 has been applied (see Table 2). However, a case-by-case conversion factor may have to be applied for specific productions."]
["Glass","3. Mineral industry","Filament glass fibre","Unspecified","Unspecified","Unspecified","Fuel oil","Unspecified","Melting furnace","Air","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance; (ii) Use of low sulphur content fuels; (iii) Dry or semi dry scrubbing in combination wtih a filtration system; (iv) Use of wet scrubbing ","mg/Nm3","500","1000","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The higher levels of the range are associated with the use of sulphates in the batch formulation for refining the glass.\n\nThe associated emission levels are related to the use of 1 % sulphur fuel oil in combination with secondary abatement techniques.\n\nThe lower levels correspond to conditions where the reduction of SO X is a priority over a lower production of solid waste corresponding to the sulphate-rich filter dust. In this case, the lower levels are associated with the use of a bag filter.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Filament glass fibre","Unspecified","Unspecified","Unspecified","Fuel oil","Unspecified","Melting furnace","Air","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance; (ii) Use of low sulphur content fuels; (iii) Dry or semi dry scrubbing in combination wtih a filtration system; (iv) Use of wet scrubbing ","mg/Nm3","500","1000","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The higher levels of the range are associated with the use of sulphates in the batch formulation for refining the glass.\n\nThe associated emission levels are related to the use of 1 % sulphur fuel oil in combination with secondary abatement techniques.\n\nThe lower levels correspond to conditions where the reduction of SO X is a priority over a lower production of solid waste corresponding to the sulphate-rich filter dust. In this case, the lower levels are associated with the use of a bag filter."]
["Glass","3. Mineral industry","Filament glass fibre","Unspecified","Unspecified","Unspecified","Fuel oil","Unspecified","Melting furnace","Air","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance; (ii) Use of low sulphur content fuels; (iii) Dry or semi dry scrubbing in combination wtih a filtration system; (iv) Use of wet scrubbing ","kg/tonne melted glass","2.25","4.5","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The higher levels of the range are associated with the use of sulphates in the batch formulation for refining the glass.\n\nThe conversion factor reported in Table 2 (4,5 × 10 –3 ) has been applied.\n\nThe associated emission levels are related to the use of 1 % sulphur fuel oil in combination with secondary abatement techniques.\n\nThe lower levels correspond to conditions where the reduction of SO X is a priority over a lower production of solid waste corresponding to the sulphate-rich filter dust. In this case, the lower levels are associated with the use of a bag filter.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Filament glass fibre","Unspecified","Unspecified","Unspecified","Fuel oil","Unspecified","Melting furnace","Air","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance; (ii) Use of low sulphur content fuels; (iii) Dry or semi dry scrubbing in combination wtih a filtration system; (iv) Use of wet scrubbing ","kg/tonne melted glass","2.25","4.5","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The higher levels of the range are associated with the use of sulphates in the batch formulation for refining the glass.\n\nThe conversion factor reported in Table 2 (4,5 × 10 –3 ) has been applied.\n\nThe associated emission levels are related to the use of 1 % sulphur fuel oil in combination with secondary abatement techniques.\n\nThe lower levels correspond to conditions where the reduction of SO X is a priority over a lower production of solid waste corresponding to the sulphate-rich filter dust. In this case, the lower levels are associated with the use of a bag filter."]
["Glass","3. Mineral industry","Filament glass fibre","Unspecified","Unspecified","Unspecified","Natural gas ","Unspecified","Melting furnace","Air","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance; (ii) Use of low sulphur content fuels; (iii) Dry or semi dry scrubbing in combination wtih a filtration system; (iv) Use of wet scrubbing ","mg/Nm3","200","800","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","Values at levels of < 30 mg/Nm 3 (< 0,14 kg/tonne melted glass) have been reported for boron-free formulations, with the application of primary techniques.\n\nFor oxy-fuel furnaces with the application of wet scrubbing, the BAT-AEL is reported to be < 0,1 kg/tonne melted glass of SO X , expressed as SO 2 .",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Filament glass fibre","Unspecified","Unspecified","Unspecified","Natural gas ","Unspecified","Melting furnace","Air","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance; (ii) Use of low sulphur content fuels; (iii) Dry or semi dry scrubbing in combination wtih a filtration system; (iv) Use of wet scrubbing ","mg/Nm3","200","800","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","Values at levels of < 30 mg/Nm 3 (< 0,14 kg/tonne melted glass) have been reported for boron-free formulations, with the application of primary techniques.\n\nFor oxy-fuel furnaces with the application of wet scrubbing, the BAT-AEL is reported to be < 0,1 kg/tonne melted glass of SO X , expressed as SO 2 ."]
["Glass","3. Mineral industry","Filament glass fibre","Unspecified","Unspecified","Unspecified","Natural gas ","Unspecified","Melting furnace","Air","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance; (ii) Use of low sulphur content fuels; (iii) Dry or semi dry scrubbing in combination wtih a filtration system; (iv) Use of wet scrubbing ","kg/tonne melted glass","0.9","3.6","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The higher levels of the range are associated with the use of sulphates in the batch formulation for refining the glass.\n\nThe conversion factor reported in Table 2 (4,5 × 10 –3 ) has been applied.\n\nFor oxy-fuel furnaces with the application of wet scrubbing, the BAT-AEL is reported to be < 0,1 kg/tonne melted glass of SO X , expressed as SO 2 .",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Filament glass fibre","Unspecified","Unspecified","Unspecified","Natural gas ","Unspecified","Melting furnace","Air","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance; (ii) Use of low sulphur content fuels; (iii) Dry or semi dry scrubbing in combination wtih a filtration system; (iv) Use of wet scrubbing ","kg/tonne melted glass","0.9","3.6","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The higher levels of the range are associated with the use of sulphates in the batch formulation for refining the glass.\n\nThe conversion factor reported in Table 2 (4,5 × 10 –3 ) has been applied.\n\nFor oxy-fuel furnaces with the application of wet scrubbing, the BAT-AEL is reported to be < 0,1 kg/tonne melted glass of SO X , expressed as SO 2 ."]
["Glass","3. Mineral industry","Flat glass","Unspecified","Unspecified","Unspecified","Fuel oil","Unspecified","Melting furnace","Air","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Dry or semi-dry scrubbing, in combination with a filtration system; (ii) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance; (iii) Use of low sulphur content fuels","mg/Nm3",500,1300,"Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The lower levels are associated with conditions where the reduction of SO X has a high priority over a lower production of solid waste corresponding to the sulphate-rich filter dust.\n\nThe associated emission levels are related to the use of 1 % sulphur fuel oil in combination with secondary abatement techniques\n\nFor large flat glass furnaces, concerns related to the achievable emission levels may require investigating the sulphur balance. Values reported in the table may be difficult to achieve in combination with filter dust recycling\n\n",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Flat glass","Unspecified","Unspecified","Unspecified","Fuel oil","Unspecified","Melting furnace","Air","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Dry or semi-dry scrubbing, in combination with a filtration system; (ii) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance; (iii) Use of low sulphur content fuels","mg/Nm3",500,1300,"Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The lower levels are associated with conditions where the reduction of SO X has a high priority over a lower production of solid waste corresponding to the sulphate-rich filter dust.\n\nThe associated emission levels are related to the use of 1 % sulphur fuel oil in combination with secondary abatement techniques\n\nFor large flat glass furnaces, concerns related to the achievable emission levels may require investigating the sulphur balance. Values reported in the table may be difficult to achieve in combination with filter dust recycling\n\n"]
["Glass","3. Mineral industry","Flat glass","Unspecified","Unspecified","Unspecified","Fuel oil","Unspecified","Melting furnace","Air","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Dry or semi-dry scrubbing, in combination with a filtration system; (ii) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance; (iii) Use of low sulphur content fuels","kg/tonne melted glass",1.25,3.25,"Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The lower levels are associated with conditions where the reduction of SO X has a high priority over a lower production of solid waste corresponding to the sulphate-rich filter dust.\n\nThe associated emission levels are related to the use of 1 % sulphur fuel oil in combination with secondary abatement techniques\n\nFor large flat glass furnaces, concerns related to the achievable emission levels may require investigating the sulphur balance. Values reported in the table may be difficult to achieve in combination with filter dust recycling\n\nThe associated emission levels are related to the use of 1 % sulphur fuel oil in combination with secondary abatement techniques.\n\n",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Flat glass","Unspecified","Unspecified","Unspecified","Fuel oil","Unspecified","Melting furnace","Air","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Dry or semi-dry scrubbing, in combination with a filtration system; (ii) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance; (iii) Use of low sulphur content fuels","kg/tonne melted glass",1.25,3.25,"Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The lower levels are associated with conditions where the reduction of SO X has a high priority over a lower production of solid waste corresponding to the sulphate-rich filter dust.\n\nThe associated emission levels are related to the use of 1 % sulphur fuel oil in combination with secondary abatement techniques\n\nFor large flat glass furnaces, concerns related to the achievable emission levels may require investigating the sulphur balance. Values reported in the table may be difficult to achieve in combination with filter dust recycling\n\nThe associated emission levels are related to the use of 1 % sulphur fuel oil in combination with secondary abatement techniques.\n\n"]
["Glass","3. Mineral industry","Flat glass","Unspecified","Unspecified","Unspecified","Natural gas ","Unspecified","Melting furnace","Air","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Dry or semi-dry scrubbing, in combination with a filtration system; (ii) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance; (iii) Use of low sulphur content fuels","mg/Nm3","300","500","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The lower levels are associated with conditions where the reduction of SO X has a high priority over a lower production of solid waste corresponding to the sulphate-rich filter dust.\n\n",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Flat glass","Unspecified","Unspecified","Unspecified","Natural gas ","Unspecified","Melting furnace","Air","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Dry or semi-dry scrubbing, in combination with a filtration system; (ii) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance; (iii) Use of low sulphur content fuels","mg/Nm3","300","500","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The lower levels are associated with conditions where the reduction of SO X has a high priority over a lower production of solid waste corresponding to the sulphate-rich filter dust.\n\n"]
["Glass","3. Mineral industry","Flat glass","Unspecified","Unspecified","Unspecified","Natural gas ","Unspecified","Melting furnace","Air","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Dry or semi-dry scrubbing, in combination with a filtration system; (ii) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance; (iii) Use of low sulphur content fuels","kg/tonne melted glass","0.75","1.25","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The lower levels are associated with conditions where the reduction of SO X has a high priority over a lower production of solid waste corresponding to the sulphate-rich filter dust.\n\nThe conversion factor reported in Table 2 (2,5 × 10 –3 ) has been applied.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Flat glass","Unspecified","Unspecified","Unspecified","Natural gas ","Unspecified","Melting furnace","Air","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Dry or semi-dry scrubbing, in combination with a filtration system; (ii) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance; (iii) Use of low sulphur content fuels","kg/tonne melted glass","0.75","1.25","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The lower levels are associated with conditions where the reduction of SO X has a high priority over a lower production of solid waste corresponding to the sulphate-rich filter dust.\n\nThe conversion factor reported in Table 2 (2,5 × 10 –3 ) has been applied."]
["Glass","3. Mineral industry","Flat glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes","Air","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce emissions to air from the downstream processes by using one or a combination of the following techniques: (i) Minimising the losses of coating products applied to the flat glass by ensuring a good sealing of the application system; (ii) Minimising the losses of SO2 from the annealing ler, by operating the control system in an optimum manner; (iii) Combining the SO2 emissions from the lehr with the waste fas from the melting furnace, when technically feasible and where a secondary treatment system is applied (filter and dry or semi-dry scrubber); (iv) Applying a secondary technique, e.g. wet scrubbing, or dry scrubbing and filtration","mg/Nm3","N/A","200","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3","N/A","Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Flat glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes","Air","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce emissions to air from the downstream processes by using one or a combination of the following techniques: (i) Minimising the losses of coating products applied to the flat glass by ensuring a good sealing of the application system; (ii) Minimising the losses of SO2 from the annealing ler, by operating the control system in an optimum manner; (iii) Combining the SO2 emissions from the lehr with the waste fas from the melting furnace, when technically feasible and where a secondary treatment system is applied (filter and dry or semi-dry scrubber); (iv) Applying a secondary technique, e.g. wet scrubbing, or dry scrubbing and filtration","mg/Nm3","N/A","200","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3","N/A","Daily average (continuous)",0]
["Glass","3. Mineral industry","Frits ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Sulphur Dioxide (24 Hour Mean)","BAT is to control SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of sulphur; (ii) Dry or semi dry scrubbing in combination with a filtration system; (iii) Use of low sulphur content fuels ","mg/Nm3","50","200","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Frits ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Sulphur Dioxide (24 Hour Mean)","BAT is to control SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of sulphur; (ii) Dry or semi dry scrubbing in combination with a filtration system; (iii) Use of low sulphur content fuels ","mg/Nm3","50","200","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)",0]
["Glass","3. Mineral industry","Frits ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Sulphur Dioxide (24 Hour Mean)","BAT is to control SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of sulphur; (ii) Dry or semi dry scrubbing in combination with a filtration system; (iii) Use of low sulphur content fuels ","kg/tonne melted glass","0.25","1.5","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The conversion factors of 5 × 10 –3 and 7,5 × 10 –3 have been used; however, the values indicated in the table may have been approximated. A case-by-case conversion factor may have to be applied based on the type of combustion",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Frits ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Sulphur Dioxide (24 Hour Mean)","BAT is to control SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of sulphur; (ii) Dry or semi dry scrubbing in combination with a filtration system; (iii) Use of low sulphur content fuels ","kg/tonne melted glass","0.25","1.5","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The conversion factors of 5 × 10 –3 and 7,5 × 10 –3 have been used; however, the values indicated in the table may have been approximated. A case-by-case conversion factor may have to be applied based on the type of combustion"]
["Glass","3. Mineral industry","HTIW wools","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes ","Air","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnaces and downstream processes by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of sulphur; (ii) Use of low sulphur content fuel","mg/Nm3","N/A","50","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3","N/A","Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","HTIW wools","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes ","Air","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnaces and downstream processes by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of sulphur; (ii) Use of low sulphur content fuel","mg/Nm3","N/A","50","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3","N/A","Daily average (continuous)",0]
["Glass","3. Mineral industry","HTIW wools","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnaces and downstream processes by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of sulphur; (ii) Use of low sulphur content fuel","mg/Nm3","N/A","50","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","HTIW wools","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnaces and downstream processes by using one or a combination of the following techniques: (i) Selection of raw materials for the batch formulation with a low content of sulphur; (ii) Use of low sulphur content fuel","mg/Nm3","N/A","50","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)",0]
["Glass","3. Mineral industry","Mineral wool","Glass wool ","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance ; (ii) Use of low sulphur content fuels' (iii) Dry or semi-dry scrubbing, in combination with a filtration system; (iv) Use of wet scrubbing","mg/Nm3","50","150","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The lower levels of the ranges are associated with the use of electric melting. The higher levels are associated with high levels of cullet recycling.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Mineral wool","Glass wool ","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance ; (ii) Use of low sulphur content fuels' (iii) Dry or semi-dry scrubbing, in combination with a filtration system; (iv) Use of wet scrubbing","mg/Nm3","50","150","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The lower levels of the ranges are associated with the use of electric melting. The higher levels are associated with high levels of cullet recycling."]
["Glass","3. Mineral industry","Mineral wool","Glass wool ","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance ; (ii) Use of low sulphur content fuels' (iii) Dry or semi-dry scrubbing, in combination with a filtration system; (iv) Use of wet scrubbing","kg/tonne melted glass","0.1","0.3","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","This BATL-AEL is for gas-fired and elctric furnaces\n\nThe lower levels of the ranges are associated with the use of electric melting. The higher levels are associated with high levels of cullet recycling.\n\nThe conversion factors of 2 × 10 –3 for glass wool and 2,5 × 10 –3 for stone wool have been used",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Mineral wool","Glass wool ","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance ; (ii) Use of low sulphur content fuels' (iii) Dry or semi-dry scrubbing, in combination with a filtration system; (iv) Use of wet scrubbing","kg/tonne melted glass","0.1","0.3","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","This BATL-AEL is for gas-fired and elctric furnaces\n\nThe lower levels of the ranges are associated with the use of electric melting. The higher levels are associated with high levels of cullet recycling.\n\nThe conversion factors of 2 × 10 –3 for glass wool and 2,5 × 10 –3 for stone wool have been used"]
["Glass","3. Mineral industry","Mineral wool","Stone wool","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance ; (ii) Use of low sulphur content fuels' (iii) Dry or semi-dry scrubbing, in combination with a filtration system; (iv) Use of wet scrubbing","mg/Nm3","N/A","350","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","This BATL-AEL is for gas-fired and elctric furnaces",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Mineral wool","Stone wool","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance ; (ii) Use of low sulphur content fuels' (iii) Dry or semi-dry scrubbing, in combination with a filtration system; (iv) Use of wet scrubbing","mg/Nm3","N/A","350","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","This BATL-AEL is for gas-fired and elctric furnaces"]
["Glass","3. Mineral industry","Mineral wool","Stone wool","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance ; (ii) Use of low sulphur content fuels' (iii) Dry or semi-dry scrubbing, in combination with a filtration system; (iv) Use of wet scrubbing","kg/tonne melted glass","N/A","0.9","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","This BATL-AEL is for gas-fired and elctric furnaces\n\nThe conversion factors of 2 × 10 –3 for glass wool and 2,5 × 10 –3 for stone wool have been used",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Mineral wool","Stone wool","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance ; (ii) Use of low sulphur content fuels' (iii) Dry or semi-dry scrubbing, in combination with a filtration system; (iv) Use of wet scrubbing","kg/tonne melted glass","N/A","0.9","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","This BATL-AEL is for gas-fired and elctric furnaces\n\nThe conversion factors of 2 × 10 –3 for glass wool and 2,5 × 10 –3 for stone wool have been used"]
["Glass","3. Mineral industry","Mineral wool","Stone wool","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance ; (ii) Use of low sulphur content fuels' (iii) Dry or semi-dry scrubbing, in combination with a filtration system; (iv) Use of wet scrubbing","mg/Nm3","N/A","400","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","This BATL-AEL is for Cupola furnaces, no briquettes or slag recycling\n\nThe BAT-AEL is associated with conditions where the reduction of SO X emissions has a high priority over a lower production of solid waste.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Mineral wool","Stone wool","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance ; (ii) Use of low sulphur content fuels' (iii) Dry or semi-dry scrubbing, in combination with a filtration system; (iv) Use of wet scrubbing","mg/Nm3","N/A","400","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","This BATL-AEL is for Cupola furnaces, no briquettes or slag recycling\n\nThe BAT-AEL is associated with conditions where the reduction of SO X emissions has a high priority over a lower production of solid waste."]
["Glass","3. Mineral industry","Mineral wool","Stone wool","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance ; (ii) Use of low sulphur content fuels' (iii) Dry or semi-dry scrubbing, in combination with a filtration system; (iv) Use of wet scrubbing","kg/tonne melted glass","N/A","1.0","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","This BATL-AEL is for Cupola furnaces, no briquettes or slag recycling\n\nThe BAT-AEL is associated with conditions where the reduction of SO X emissions has a high priority over a lower production of solid waste.\n\nThe conversion factors of 2 × 10 –3 for glass wool and 2,5 × 10 –3 for stone wool have been used",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Mineral wool","Stone wool","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance ; (ii) Use of low sulphur content fuels' (iii) Dry or semi-dry scrubbing, in combination with a filtration system; (iv) Use of wet scrubbing","kg/tonne melted glass","N/A","1.0","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","This BATL-AEL is for Cupola furnaces, no briquettes or slag recycling\n\nThe BAT-AEL is associated with conditions where the reduction of SO X emissions has a high priority over a lower production of solid waste.\n\nThe conversion factors of 2 × 10 –3 for glass wool and 2,5 × 10 –3 for stone wool have been used"]
["Glass","3. Mineral industry","Mineral wool","Stone wool","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance ; (ii) Use of low sulphur content fuels' (iii) Dry or semi-dry scrubbing, in combination with a filtration system; (iv) Use of wet scrubbing","mg/Nm3","N/A","1400","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","This BATL-AEL is for Cupola furnaces, with cement briquettes or slag recycling\n\nWhen reduction of waste has a high priority over SO X emissions, higher emission values may be expected. The achievable levels should be based on a sulphur balance.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Mineral wool","Stone wool","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance ; (ii) Use of low sulphur content fuels' (iii) Dry or semi-dry scrubbing, in combination with a filtration system; (iv) Use of wet scrubbing","mg/Nm3","N/A","1400","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","This BATL-AEL is for Cupola furnaces, with cement briquettes or slag recycling\n\nWhen reduction of waste has a high priority over SO X emissions, higher emission values may be expected. The achievable levels should be based on a sulphur balance."]
["Glass","3. Mineral industry","Mineral wool","Stone wool","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance ; (ii) Use of low sulphur content fuels' (iii) Dry or semi-dry scrubbing, in combination with a filtration system; (iv) Use of wet scrubbing","kg/tonne melted glass","N/A","3.5","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","This BATL-AEL is for Cupola furnaces, with cement briquettes or slag recycling\n\nWhen reduction of waste has a high priority over SO X emissions, higher emission values may be expected. The achievable levels should be based on a sulphur balance.\n\nThe conversion factors of 2 × 10 –3 for glass wool and 2,5 × 10 –3 for stone wool have been used",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Mineral wool","Stone wool","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance ; (ii) Use of low sulphur content fuels' (iii) Dry or semi-dry scrubbing, in combination with a filtration system; (iv) Use of wet scrubbing","kg/tonne melted glass","N/A","3.5","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","This BATL-AEL is for Cupola furnaces, with cement briquettes or slag recycling\n\nWhen reduction of waste has a high priority over SO X emissions, higher emission values may be expected. The achievable levels should be based on a sulphur balance.\n\nThe conversion factors of 2 × 10 –3 for glass wool and 2,5 × 10 –3 for stone wool have been used"]
["Glass","3. Mineral industry","Special glass ","Unspecified","Unspecified","Unspecified","Fuel oil","Unspecified","Melting furnace","Air","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance; (ii) Use of low sulphur content fuels; (iii) Dry or semi-dry scrubbing, in combustion with a filtration system ","mg/Nm3","500","800","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The ranges take into account the variable sulphur balances associated with the type of glass produced.\n\nThe associated emission levels are related to the use of 1 % sulphur fuel oil in combination with secondary abatement techniques.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Special glass ","Unspecified","Unspecified","Unspecified","Fuel oil","Unspecified","Melting furnace","Air","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance; (ii) Use of low sulphur content fuels; (iii) Dry or semi-dry scrubbing, in combustion with a filtration system ","mg/Nm3","500","800","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The ranges take into account the variable sulphur balances associated with the type of glass produced.\n\nThe associated emission levels are related to the use of 1 % sulphur fuel oil in combination with secondary abatement techniques."]
["Glass","3. Mineral industry","Special glass ","Unspecified","Unspecified","Unspecified","Fuel oil","Unspecified","Melting furnace","Air","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance; (ii) Use of low sulphur content fuels; (iii) Dry or semi-dry scrubbing, in combustion with a filtration system ","kg/tonne melted glass","1.25","2","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The ranges take into account the variable sulphur balances associated with the type of glass produced.\n\nThe associated emission levels are related to the use of 1 % sulphur fuel oil in combination with secondary abatement techniques.\n\nThe conversion factor of 2,5 × 10 –3 (see Table 2) has been used. However, a case-by-case conversion factor may have to be applied based on the type of production.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Special glass ","Unspecified","Unspecified","Unspecified","Fuel oil","Unspecified","Melting furnace","Air","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance; (ii) Use of low sulphur content fuels; (iii) Dry or semi-dry scrubbing, in combustion with a filtration system ","kg/tonne melted glass","1.25","2","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The ranges take into account the variable sulphur balances associated with the type of glass produced.\n\nThe associated emission levels are related to the use of 1 % sulphur fuel oil in combination with secondary abatement techniques.\n\nThe conversion factor of 2,5 × 10 –3 (see Table 2) has been used. However, a case-by-case conversion factor may have to be applied based on the type of production."]
["Glass","3. Mineral industry","Special glass ","Unspecified","Unspecified","Unspecified","Natural gas, Electric melting","Unspecified","Melting furnace","Air","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance; (ii) Use of low sulphur content fuels; (iii) Dry or semi-dry scrubbing, in combustion with a filtration system ","mg/Nm3","30","200","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The ranges take into account the variable sulphur balances associated with the type of glass produced.\n\nThe lower levels are associated with the use of electric melting and batch formulations without sulphates.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Special glass ","Unspecified","Unspecified","Unspecified","Natural gas, Electric melting","Unspecified","Melting furnace","Air","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance; (ii) Use of low sulphur content fuels; (iii) Dry or semi-dry scrubbing, in combustion with a filtration system ","mg/Nm3","30","200","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The ranges take into account the variable sulphur balances associated with the type of glass produced.\n\nThe lower levels are associated with the use of electric melting and batch formulations without sulphates."]
["Glass","3. Mineral industry","Special glass ","Unspecified","Unspecified","Unspecified","Natural gas, Electric melting","Unspecified","Melting furnace","Air","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance; (ii) Use of low sulphur content fuels; (iii) Dry or semi-dry scrubbing, in combustion with a filtration system ","kg/tonne melted glass","0.08","0.5","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The ranges take into account the variable sulphur balances associated with the type of glass produced.\n\nThe lower levels are associated with the use of electric melting and batch formulations without sulphates.\n\nThe conversion factor of 2,5 × 10 –3 (see Table 2) has been used. However, a case-by-case conversion factor may have to be applied based on the type of production.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Special glass ","Unspecified","Unspecified","Unspecified","Natural gas, Electric melting","Unspecified","Melting furnace","Air","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce SO X emissions from the melting furnace by using one or a combination of the following techniques: (i) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance; (ii) Use of low sulphur content fuels; (iii) Dry or semi-dry scrubbing, in combustion with a filtration system ","kg/tonne melted glass","0.08","0.5","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","The ranges take into account the variable sulphur balances associated with the type of glass produced.\n\nThe lower levels are associated with the use of electric melting and batch formulations without sulphates.\n\nThe conversion factor of 2,5 × 10 –3 (see Table 2) has been used. However, a case-by-case conversion factor may have to be applied based on the type of production."]
["Glass","3. Mineral industry","Container glass","Unspecified","Unspecified","Unspecified","Natural gas ","Unspecified","Melting furnace","Air","SOX expressed as SO3","BAT is to reduce Sox emissions from the melting furnace by using one or a combination of the following techniques: (i) Dry or semi-dry scrubbing with a filtration system; (ii) minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance; (iii) Use of low sulphur content fuels","kg/tonne melted glass","0.3","0.75","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","For special types of coloured glasses (e.g. reduced green glasses), concerns related to the achievable emission levels may require investigating the sulphur balance. Values reported in the table may be difficult to achieve in combination with filter dust recycling and the rate of recycling of external cullet.\n\nThe lower levels are associated with conditions where the reduction of SO X is a high priority over a lower production of solid waste corresponding to the sulphate-rich filter dust.\n\nThe conversion factor reported in Table 2 for general cases (1,5 × 10 –3 ) has been applied.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Container glass","Unspecified","Unspecified","Unspecified","Natural gas ","Unspecified","Melting furnace","Air","SOX expressed as SO3","BAT is to reduce Sox emissions from the melting furnace by using one or a combination of the following techniques: (i) Dry or semi-dry scrubbing with a filtration system; (ii) minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance; (iii) Use of low sulphur content fuels","kg/tonne melted glass","0.3","0.75","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","For special types of coloured glasses (e.g. reduced green glasses), concerns related to the achievable emission levels may require investigating the sulphur balance. Values reported in the table may be difficult to achieve in combination with filter dust recycling and the rate of recycling of external cullet.\n\nThe lower levels are associated with conditions where the reduction of SO X is a high priority over a lower production of solid waste corresponding to the sulphate-rich filter dust.\n\nThe conversion factor reported in Table 2 for general cases (1,5 × 10 –3 ) has been applied."]
["Glass","3. Mineral industry","Container glass","Unspecified","Unspecified","Unspecified","Fuel oil","Unspecified","Melting furnace","Air","SOX expressed as SO4","BAT is to reduce Sox emissions from the melting furnace by using one or a combination of the following techniques: (i) Dry or semi-dry scrubbing with a filtration system; (ii) minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance; (iii) Use of low sulphur content fuels","mg/Nm3","500","1200","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","For special types of coloured glasses (e.g. reduced green glasses), concerns related to the achievable emission levels may require investigating the sulphur balance. Values reported in the table may be difficult to achieve in combination with filter dust recycling and the rate of recycling of external cullet.\n\nThe lower levels are associated with conditions where the reduction of SO X is a high priority over a lower production of solid waste corresponding to the sulphate-rich filter dust.\n\nThe associated emission levels are related to the use of 1 % sulphur fuel oil in combination with secondary abatement techniques",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Container glass","Unspecified","Unspecified","Unspecified","Fuel oil","Unspecified","Melting furnace","Air","SOX expressed as SO4","BAT is to reduce Sox emissions from the melting furnace by using one or a combination of the following techniques: (i) Dry or semi-dry scrubbing with a filtration system; (ii) minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance; (iii) Use of low sulphur content fuels","mg/Nm3","500","1200","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","For special types of coloured glasses (e.g. reduced green glasses), concerns related to the achievable emission levels may require investigating the sulphur balance. Values reported in the table may be difficult to achieve in combination with filter dust recycling and the rate of recycling of external cullet.\n\nThe lower levels are associated with conditions where the reduction of SO X is a high priority over a lower production of solid waste corresponding to the sulphate-rich filter dust.\n\nThe associated emission levels are related to the use of 1 % sulphur fuel oil in combination with secondary abatement techniques"]
["Glass","3. Mineral industry","Container glass","Unspecified","Unspecified","Unspecified","Fuel oil","Unspecified","Melting furnace","Air","SOX expressed as SO5","BAT is to reduce Sox emissions from the melting furnace by using one or a combination of the following techniques: (i) Dry or semi-dry scrubbing with a filtration system; (ii) minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance; (iii) Use of low sulphur content fuels","kg/tonne melted glass","0.75","1.8","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","For special types of coloured glasses (e.g. reduced green glasses), concerns related to the achievable emission levels may require investigating the sulphur balance. Values reported in the table may be difficult to achieve in combination with filter dust recycling and the rate of recycling of external cullet.\n\nThe lower levels are associated with conditions where the reduction of SO X is a high priority over a lower production of solid waste corresponding to the sulphate-rich filter dust.\n\nThe associated emission levels are related to the use of 1 % sulphur fuel oil in combination with secondary abatement techniques\n\nThe conversion factor reported in Table 2 for general cases (1,5 × 10 –3 ) has been applied.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Container glass","Unspecified","Unspecified","Unspecified","Fuel oil","Unspecified","Melting furnace","Air","SOX expressed as SO5","BAT is to reduce Sox emissions from the melting furnace by using one or a combination of the following techniques: (i) Dry or semi-dry scrubbing with a filtration system; (ii) minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance; (iii) Use of low sulphur content fuels","kg/tonne melted glass","0.75","1.8","Green","Continuous measurements of dust, NO X and SO2 emissions or discontinuous measurements at least twice per year, associated with the control of surrogate parameters to ensure that the treatment system is working properly between measurements","273.15","101.3",0.08,"Daily average (continuous)","For special types of coloured glasses (e.g. reduced green glasses), concerns related to the achievable emission levels may require investigating the sulphur balance. Values reported in the table may be difficult to achieve in combination with filter dust recycling and the rate of recycling of external cullet.\n\nThe lower levels are associated with conditions where the reduction of SO X is a high priority over a lower production of solid waste corresponding to the sulphate-rich filter dust.\n\nThe associated emission levels are related to the use of 1 % sulphur fuel oil in combination with secondary abatement techniques\n\nThe conversion factor reported in Table 2 for general cases (1,5 × 10 –3 ) has been applied."]
["Glass","3. Mineral industry","Container glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes","Air","Tin compounds, including organotin, expressed as Sn","When tin, organotin or titanium compounds are used for hot-end coating operations, BAT is to reduce emissions by using one or a combination of the following techniques: (i) Minimising the losses of the coating product by ensuring a good sealing of the application system and applying an effective extracting hood; (ii) Combining the flue-gas from the coating operations with the waste gas from the melting furnace or with the combustion air of the furnace, when a secondary treatment system is applied (filter and dry or semi-dry scrubber); (iii) Applying a secondary technique, e.g. wet scrubbing, dry scrubbing plus filtration","mg/Nm3","N/A","5","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3","N/A","Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Container glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes","Air","Tin compounds, including organotin, expressed as Sn","When tin, organotin or titanium compounds are used for hot-end coating operations, BAT is to reduce emissions by using one or a combination of the following techniques: (i) Minimising the losses of the coating product by ensuring a good sealing of the application system and applying an effective extracting hood; (ii) Combining the flue-gas from the coating operations with the waste gas from the melting furnace or with the combustion air of the furnace, when a secondary treatment system is applied (filter and dry or semi-dry scrubber); (iii) Applying a secondary technique, e.g. wet scrubbing, dry scrubbing plus filtration","mg/Nm3","N/A","5","Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3","N/A","Daily average (continuous)",0]
["Glass","3. Mineral industry","Container glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes","Air","Titanium compounds expressed as Ti","When tin, organotin or titanium compounds are used for hot-end coating operations, BAT is to reduce emissions by using one or a combination of the following techniques: (i) Minimising the losses of the coating product by ensuring a good sealing of the application system and applying an effective extracting hood; (ii) Combining the flue-gas from the coating operations with the waste gas from the melting furnace or with the combustion air of the furnace, when a secondary treatment system is applied (filter and dry or semi-dry scrubber); (iii) Applying a secondary technique, e.g. wet scrubbing, dry scrubbing plus filtration","mg/Nm3","N/A",5,"Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3","N/A","Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Container glass","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes","Air","Titanium compounds expressed as Ti","When tin, organotin or titanium compounds are used for hot-end coating operations, BAT is to reduce emissions by using one or a combination of the following techniques: (i) Minimising the losses of the coating product by ensuring a good sealing of the application system and applying an effective extracting hood; (ii) Combining the flue-gas from the coating operations with the waste gas from the melting furnace or with the combustion air of the furnace, when a secondary treatment system is applied (filter and dry or semi-dry scrubber); (iii) Applying a secondary technique, e.g. wet scrubbing, dry scrubbing plus filtration","mg/Nm3","N/A",5,"Green","Regular periodic measurements of emissions of HCl, HF, CO and metals, in particular when raw materials containing such substances are used or partial combustion may occur","273.15","101.3","N/A","Daily average (continuous)",0]
["Glass","3. Mineral industry","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes- Curing oven emissions ","Air","Particulates (PM10) (24 hr Mean)","BAT is to reduce emissions from downstream processes by using one or a combination of the following techniques: (i) Impact jets and cyclones; (ii) Wet scrubbers; (iii) Wet electrostatic precipitators; (iv) Stone wool filters; (v) Waste gas incineration","mg/Nm3","5","30","Amber",0,"273.15","101.3","N/A","Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes- Curing oven emissions ","Air","Particulates (PM10) (24 hr Mean)","BAT is to reduce emissions from downstream processes by using one or a combination of the following techniques: (i) Impact jets and cyclones; (ii) Wet scrubbers; (iii) Wet electrostatic precipitators; (iv) Stone wool filters; (v) Waste gas incineration","mg/Nm3","5","30","Amber",0,"273.15","101.3","N/A","Daily average (continuous)",0]
["Glass","3. Mineral industry","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes- Curing oven emissions ","Air","Particulates (PM10) (24 hr Mean)","BAT is to reduce emissions from downstream processes by using one or a combination of the following techniques: (i) Impact jets and cyclones; (ii) Wet scrubbers; (iii) Wet electrostatic precipitators; (iv) Stone wool filters; (v) Waste gas incineration","kg/tonne melted glass","N/A","0.2","Amber",0,"273.15","101.3","N/A","Daily average (continuous)","The specific mass emissions refer to 1 tonne of produced glass",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes- Curing oven emissions ","Air","Particulates (PM10) (24 hr Mean)","BAT is to reduce emissions from downstream processes by using one or a combination of the following techniques: (i) Impact jets and cyclones; (ii) Wet scrubbers; (iii) Wet electrostatic precipitators; (iv) Stone wool filters; (v) Waste gas incineration","kg/tonne melted glass","N/A","0.2","Amber",0,"273.15","101.3","N/A","Daily average (continuous)","The specific mass emissions refer to 1 tonne of produced glass"]
["Glass","3. Mineral industry","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes- Forming area ","Air","Particulates (PM10) (24 hr Mean)","BAT is to reduce emissions from downstream processes by using one or a combination of the following techniques: (i) Impact jets and cyclones; (ii) Wet scrubbers; (iii) Wet electrostatic precipitators; (iv) Stone wool filters; (v) Waste gas incineration","mg/Nm3","20","50","Amber",0,"273.15","101.3","N/A","Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes- Forming area ","Air","Particulates (PM10) (24 hr Mean)","BAT is to reduce emissions from downstream processes by using one or a combination of the following techniques: (i) Impact jets and cyclones; (ii) Wet scrubbers; (iii) Wet electrostatic precipitators; (iv) Stone wool filters; (v) Waste gas incineration","mg/Nm3","20","50","Amber",0,"273.15","101.3","N/A","Daily average (continuous)",0]
["Glass","3. Mineral industry","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes- Curing oven emissions ","Air","VOC","BAT is to reduce emissions from downstream processes by using one or a combination of the following techniques: (i) Impact jets and cyclones; (ii) Wet scrubbers; (iii) Wet electrostatic precipitators; (iv) Stone wool filters; (v) Waste gas incineration","mg/Nm3","N/A","10","Amber",0,"273.15","101.3","N/A","Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes- Curing oven emissions ","Air","VOC","BAT is to reduce emissions from downstream processes by using one or a combination of the following techniques: (i) Impact jets and cyclones; (ii) Wet scrubbers; (iii) Wet electrostatic precipitators; (iv) Stone wool filters; (v) Waste gas incineration","mg/Nm3","N/A","10","Amber",0,"273.15","101.3","N/A","Daily average (continuous)",0]
["Glass","3. Mineral industry","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes- Curing oven emissions ","Air","VOC","BAT is to reduce emissions from downstream processes by using one or a combination of the following techniques: (i) Impact jets and cyclones; (ii) Wet scrubbers; (iii) Wet electrostatic precipitators; (iv) Stone wool filters; (v) Waste gas incineration","kg/tonne melted glass","N/A","0.065","Amber",0,"273.15","101.3","N/A","Daily average (continuous)","The specific mass emissions refer to 1 tonne of produced glass",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes- Curing oven emissions ","Air","VOC","BAT is to reduce emissions from downstream processes by using one or a combination of the following techniques: (i) Impact jets and cyclones; (ii) Wet scrubbers; (iii) Wet electrostatic precipitators; (iv) Stone wool filters; (v) Waste gas incineration","kg/tonne melted glass","N/A","0.065","Amber",0,"273.15","101.3","N/A","Daily average (continuous)","The specific mass emissions refer to 1 tonne of produced glass"]
["Glass","3. Mineral industry","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes- Forming area ","Air","VOC","BAT is to reduce emissions from downstream processes by using one or a combination of the following techniques: (i) Impact jets and cyclones; (ii) Wet scrubbers; (iii) Wet electrostatic precipitators; (iv) Stone wool filters; (v) Waste gas incineration","mg/Nm3","10","30","Amber",0,"273.15","101.3","N/A","Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes- Forming area ","Air","VOC","BAT is to reduce emissions from downstream processes by using one or a combination of the following techniques: (i) Impact jets and cyclones; (ii) Wet scrubbers; (iii) Wet electrostatic precipitators; (iv) Stone wool filters; (v) Waste gas incineration","mg/Nm3","10","30","Amber",0,"273.15","101.3","N/A","Daily average (continuous)",0]
["Glass","3. Mineral industry","HTIW wools","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","VOC","Primary and/or secondary techniques","mg/Nm3","10","20","Amber",0,"273.15","101.3",0.08,"Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","HTIW wools","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Melting furnace","Air","VOC","Primary and/or secondary techniques","mg/Nm3","10","20","Amber",0,"273.15","101.3",0.08,"Daily average (continuous)",0]
["Iron and steel","2. Production and processing of metals","Coke Oven Plants","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Air","Particulates (PM10) (24 hr Mean)","BAT for the coke oven underfiring is to reduce the emissions by using the following techniques: (i) preventing leakage between the oven chamber and the heating chamber by means of regular coke oven operation; (ii) repairing leakage between the oven chamber and the heating chamber (only applicable to existing plants); (iii) incorporating low-nitrogen oxides (NOX) techniques in the construction of new batteries, such as staged combustion\nand the use of thinner bricks and refractory with a better thermal conductivity (only applicable to new plants); (iv) using desulphurised coke oven gas (COG) process gases ","mg/Nm3",1,20,"Green","Discontinuous ",0,0,0.05,"Daily mean average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Coke Oven Plants","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Air","Particulates (PM10) (24 hr Mean)","BAT for the coke oven underfiring is to reduce the emissions by using the following techniques: (i) preventing leakage between the oven chamber and the heating chamber by means of regular coke oven operation; (ii) repairing leakage between the oven chamber and the heating chamber (only applicable to existing plants); (iii) incorporating low-nitrogen oxides (NOX) techniques in the construction of new batteries, such as staged combustion\nand the use of thinner bricks and refractory with a better thermal conductivity (only applicable to new plants); (iv) using desulphurised coke oven gas (COG) process gases ","mg/Nm3",1,20,"Green","Discontinuous ",0,0,0.05,"Daily mean average",0]
["Iron and steel","2. Production and processing of metals","Coke Oven Plants","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Coke grading and handling","Air","Particulates (PM10) (24 hr Mean)","BAT for coke grading and handling is to prevent or reduce dust emissions by using the following techniques in combination: (i)use of building or device enclosures; (ii) efficient extraction and subsequent dry dedusting ","mg/Nm3","N/A",10,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Coke Oven Plants","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Coke grading and handling","Air","Particulates (PM10) (24 hr Mean)","BAT for coke grading and handling is to prevent or reduce dust emissions by using the following techniques in combination: (i)use of building or device enclosures; (ii) efficient extraction and subsequent dry dedusting ","mg/Nm3","N/A",10,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0]
["Iron and steel","2. Production and processing of metals","Coke Oven Plants","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Coke pushing","Air","Particulates (PM10) (24 hr Mean)","BAT for coke pushing is to reduce dust emissions by using the following techniques: (i)  extraction by means of an integrated coke transfer machine equipped with a hood; (ii) using a one point or a mobile quenching car","mg/Nm3","N/A",20,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Coke Oven Plants","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Coke pushing","Air","Particulates (PM10) (24 hr Mean)","BAT for coke pushing is to reduce dust emissions by using the following techniques: (i)  extraction by means of an integrated coke transfer machine equipped with a hood; (ii) using a one point or a mobile quenching car","mg/Nm3","N/A",20,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0]
["Iron and steel","2. Production and processing of metals","Coke Oven Plants","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Coke pushing","Air","Particulates (PM10) (24 hr Mean)","BAT for coke pushing is to reduce dust emissions by using the following techniques: (i) using land-based extraction gas treatment with a bag filter or other abatement systems","mg/Nm3","N/A",10,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Coke Oven Plants","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Coke pushing","Air","Particulates (PM10) (24 hr Mean)","BAT for coke pushing is to reduce dust emissions by using the following techniques: (i) using land-based extraction gas treatment with a bag filter or other abatement systems","mg/Nm3","N/A",10,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0]
["Iron and steel","2. Production and processing of metals","Coke Oven Plants","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Coke quenching","Air","Particulates (PM10) (24 hr Mean)","BAT for coke quenching is to reduce dust emissions by using one of the following techniques: (i) using coke dry quenching (CDQ) with the recovery of sensible heat and the removal of dust from charging, handling\nand screening operations by means of a bag filter","mg/Nm3","N/A",20,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Coke Oven Plants","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Coke quenching","Air","Particulates (PM10) (24 hr Mean)","BAT for coke quenching is to reduce dust emissions by using one of the following techniques: (i) using coke dry quenching (CDQ) with the recovery of sensible heat and the removal of dust from charging, handling\nand screening operations by means of a bag filter","mg/Nm3","N/A",20,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0]
["Iron and steel","2. Production and processing of metals","Coke Oven Plants","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Coke quenching","Air","Particulates (PM10) (24 hr Mean)","BAT for coke quenching is to reduce dust emissions by using one of the following techniques: (i) using coke stabilisation quenching (CSQ)","g/t","N/A",10,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Coke Oven Plants","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Coke quenching","Air","Particulates (PM10) (24 hr Mean)","BAT for coke quenching is to reduce dust emissions by using one of the following techniques: (i) using coke stabilisation quenching (CSQ)","g/t","N/A",10,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0]
["Iron and steel","2. Production and processing of metals","Coke Oven Plants","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Coke quenching","Air","Particulates (PM10) (24 hr Mean)","BAT for coke quenching is to reduce dust emissions by using one of the following techniques: (i) using emission-minimised conventional wet quenching","g/t","N/A",25,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Coke Oven Plants","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Coke quenching","Air","Particulates (PM10) (24 hr Mean)","BAT for coke quenching is to reduce dust emissions by using one of the following techniques: (i) using emission-minimised conventional wet quenching","g/t","N/A",25,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0]
["Iron and steel","2. Production and processing of metals","Other","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: Basic oxygen furnace (BOF) gas recovery by supressed combustion","Air","Particulates (PM10) (24 hr Mean)","BAT for basic oxygen furnace (BOF) gas recovery by suppressed combustion is to extract the BOF gas during blowing as much as possible and to clean it by using the following techniques in combination: (i) use of a suppressed combustion process; (ii) prededusting to remove coarse dust by means of dry separation techniques (e.g. deflector, cyclone) or wet separators; (iii) dust abatement by means of dry dedusting for new and existing plants or wet dedusting for existing plants\n","mg/Nm3",10,30,"Green","Continuous",0,0,"Unspecified ",0,"This BAT AEL is for dust abatement by dry dedusting",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Other","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: Basic oxygen furnace (BOF) gas recovery by supressed combustion","Air","Particulates (PM10) (24 hr Mean)","BAT for basic oxygen furnace (BOF) gas recovery by suppressed combustion is to extract the BOF gas during blowing as much as possible and to clean it by using the following techniques in combination: (i) use of a suppressed combustion process; (ii) prededusting to remove coarse dust by means of dry separation techniques (e.g. deflector, cyclone) or wet separators; (iii) dust abatement by means of dry dedusting for new and existing plants or wet dedusting for existing plants\n","mg/Nm3",10,30,"Green","Continuous",0,0,"Unspecified ",0,"This BAT AEL is for dust abatement by dry dedusting"]
["Iron and steel","2. Production and processing of metals","Other","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: Basic oxygen furnace (BOF) gas recovery by supressed combustion","Air","Particulates (PM10) (24 hr Mean)","BAT for basic oxygen furnace (BOF) gas recovery by suppressed combustion is to extract the BOF gas during blowing as much as possible and to clean it by using the following techniques in combination: (i) use of a suppressed combustion process; (ii) prededusting to remove coarse dust by means of dry separation techniques (e.g. deflector, cyclone) or wet separators; (iii) dust abatement by means of dry dedusting for new and existing plants or wet dedusting for existing plants\n","mg/Nm3","N/A",50,"Green","Continuous",0,0,"Unspecified ",0,"This BAT AEL is for dust abatement by wet dedusting",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Other","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: Basic oxygen furnace (BOF) gas recovery by supressed combustion","Air","Particulates (PM10) (24 hr Mean)","BAT for basic oxygen furnace (BOF) gas recovery by suppressed combustion is to extract the BOF gas during blowing as much as possible and to clean it by using the following techniques in combination: (i) use of a suppressed combustion process; (ii) prededusting to remove coarse dust by means of dry separation techniques (e.g. deflector, cyclone) or wet separators; (iii) dust abatement by means of dry dedusting for new and existing plants or wet dedusting for existing plants\n","mg/Nm3","N/A",50,"Green","Continuous",0,0,"Unspecified ",0,"This BAT AEL is for dust abatement by wet dedusting"]
["Iron and steel","2. Production and processing of metals","Other","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: Basic oxygen furnace (BOF) gas recovery during oxygen blowing in the case of full combustion","Air","Particulates (PM10) (24 hr Mean)","BAT for basic oxygen furnace (BOF) gas recovery during oxygen blowing in the case of full combustion is to\nreduce dust emissions by using one of the following techniques:  dry dedusting (e.g. ESP or bag filter) for new and existing plants","mg/Nm3",10,30,"Green","Continuous",0,0,"Unspecified ","Average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Other","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: Basic oxygen furnace (BOF) gas recovery during oxygen blowing in the case of full combustion","Air","Particulates (PM10) (24 hr Mean)","BAT for basic oxygen furnace (BOF) gas recovery during oxygen blowing in the case of full combustion is to\nreduce dust emissions by using one of the following techniques:  dry dedusting (e.g. ESP or bag filter) for new and existing plants","mg/Nm3",10,30,"Green","Continuous",0,0,"Unspecified ","Average over the sampling period",0]
["Iron and steel","2. Production and processing of metals","Other","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: Basic oxygen furnace (BOF) gas recovery during oxygen blowing in the case of full combustion","Air","Particulates (PM10) (24 hr Mean)","BAT for basic oxygen furnace (BOF) gas recovery during oxygen blowing in the case of full combustion is to\nreduce dust emissions by using one of the following techniques:  wet dedusting (e.g. ESP or bag filter) for existing plants","mg/Nm3","N/A",50,"Green","Continuous",0,0,"Unspecified ","Average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Other","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: Basic oxygen furnace (BOF) gas recovery during oxygen blowing in the case of full combustion","Air","Particulates (PM10) (24 hr Mean)","BAT for basic oxygen furnace (BOF) gas recovery during oxygen blowing in the case of full combustion is to\nreduce dust emissions by using one of the following techniques:  wet dedusting (e.g. ESP or bag filter) for existing plants","mg/Nm3","N/A",50,"Green","Continuous",0,0,"Unspecified ","Average over the sampling period",0]
["Iron and steel","2. Production and processing of metals","Other","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: On-site slag processing ","Air","Particulates (PM10) (24 hr Mean)","BAT for on-site slag processing is to reduce dust emissions by using one or a combination of the following\ntechniques: (i) Efficient extraction of the slag crusher and screening devices with subsequent off-gas cleaning, if relevant; (ii) transport of untreated slag by shovel loaders; (iii) extraction or wetting of conveyor transfer points for broken material; (iv) wetting of slag storage heaps; (v) use of water fogs when broken slag is loaded\n","mg/Nm3",10,20,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Other","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: On-site slag processing ","Air","Particulates (PM10) (24 hr Mean)","BAT for on-site slag processing is to reduce dust emissions by using one or a combination of the following\ntechniques: (i) Efficient extraction of the slag crusher and screening devices with subsequent off-gas cleaning, if relevant; (ii) transport of untreated slag by shovel loaders; (iii) extraction or wetting of conveyor transfer points for broken material; (iv) wetting of slag storage heaps; (v) use of water fogs when broken slag is loaded\n","mg/Nm3",10,20,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0]
["Iron and steel","2. Production and processing of metals","Other","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: Secondary dusting, reladling of hot metal from the torpedo ladle, hot metal pretreatment, BOF-related processes, secondary metallurgy and continuous casting","Air","Particulates (PM10) (24 hr Mean)","BAT is to minimise dust emissions by means of process integrated techniques, such as general techniques to prevent or control\ndiffuse or fugitive emissions, and by using appropriate enclosures and hoods with efficient extraction and a subsequent\noff-gas cleaning by means of a bag filter or an ESP.","mg/Nm3",1,15,"Green","Discontinuous ",0,0,"Unspecified ","Daily mean value","This BAT-AEL is in the case of bag filters ",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Other","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: Secondary dusting, reladling of hot metal from the torpedo ladle, hot metal pretreatment, BOF-related processes, secondary metallurgy and continuous casting","Air","Particulates (PM10) (24 hr Mean)","BAT is to minimise dust emissions by means of process integrated techniques, such as general techniques to prevent or control\ndiffuse or fugitive emissions, and by using appropriate enclosures and hoods with efficient extraction and a subsequent\noff-gas cleaning by means of a bag filter or an ESP.","mg/Nm3",1,15,"Green","Discontinuous ",0,0,"Unspecified ","Daily mean value","This BAT-AEL is in the case of bag filters "]
["Iron and steel","2. Production and processing of metals","Other","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: Secondary dusting, reladling of hot metal from the torpedo ladle, hot metal pretreatment, BOF-related processes, secondary metallurgy and continuous casting","Air","Particulates (PM10) (24 hr Mean)","BAT is to minimise dust emissions by means of process integrated techniques, such as general techniques to prevent or control\ndiffuse or fugitive emissions, and by using appropriate enclosures and hoods with efficient extraction and a subsequent\noff-gas cleaning by means of a bag filter or an ESP.","mg/Nm3","N/A",20,"Green","Continuous",0,0,"Unspecified ","Daily mean value","This BAT-AEL is in the case of electrostatic precipitators ",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Other","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: Secondary dusting, reladling of hot metal from the torpedo ladle, hot metal pretreatment, BOF-related processes, secondary metallurgy and continuous casting","Air","Particulates (PM10) (24 hr Mean)","BAT is to minimise dust emissions by means of process integrated techniques, such as general techniques to prevent or control\ndiffuse or fugitive emissions, and by using appropriate enclosures and hoods with efficient extraction and a subsequent\noff-gas cleaning by means of a bag filter or an ESP.","mg/Nm3","N/A",20,"Green","Continuous",0,0,"Unspecified ","Daily mean value","This BAT-AEL is in the case of electrostatic precipitators "]
["Iron and steel","2. Production and processing of metals","Other","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: Secondary dusting, reladling of hot metal from the torpedo ladle, hot metal pretreatment, BOF-related processes, secondary metallurgy and continuous casting","Air","Particulates (PM10) (24 hr Mean)","BAT is to minimise dust emissions by means of process integrated techniques, such as general techniques to prevent or control\ndiffuse or fugitive emissions, and by using appropriate enclosures and hoods with efficient extraction and a subsequent\noff-gas cleaning by means of a bag filter or an ESP.","mg/Nm3",1,10,"Green","Continuous",0,0,"Unspecified ","Daily mean value","This BAT-AEL is in the case of bag filters if the emissions from hot metal pretreatment and the secondary metallurgy are treated separately ",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Other","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: Secondary dusting, reladling of hot metal from the torpedo ladle, hot metal pretreatment, BOF-related processes, secondary metallurgy and continuous casting","Air","Particulates (PM10) (24 hr Mean)","BAT is to minimise dust emissions by means of process integrated techniques, such as general techniques to prevent or control\ndiffuse or fugitive emissions, and by using appropriate enclosures and hoods with efficient extraction and a subsequent\noff-gas cleaning by means of a bag filter or an ESP.","mg/Nm3",1,10,"Green","Continuous",0,0,"Unspecified ","Daily mean value","This BAT-AEL is in the case of bag filters if the emissions from hot metal pretreatment and the secondary metallurgy are treated separately "]
["Iron and steel","2. Production and processing of metals","Other","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: Secondary dusting, reladling of hot metal from the torpedo ladle, hot metal pretreatment, BOF-related processes, secondary metallurgy and continuous casting","Air","Particulates (PM10) (24 hr Mean)","BAT is to minimise dust emissions by means of process integrated techniques, such as general techniques to prevent or control\ndiffuse or fugitive emissions, and by using appropriate enclosures and hoods with efficient extraction and a subsequent\noff-gas cleaning by means of a bag filter or an ESP.","mg/Nm3","N/A",20,"Green","Continuous",0,0,"Unspecified ","Daily mean value","This BAT-AEL is in the case of electrostatic precipitators if the emissions from hot metal pretreatment and the secondary metallurgy are treated separately ",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Other","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: Secondary dusting, reladling of hot metal from the torpedo ladle, hot metal pretreatment, BOF-related processes, secondary metallurgy and continuous casting","Air","Particulates (PM10) (24 hr Mean)","BAT is to minimise dust emissions by means of process integrated techniques, such as general techniques to prevent or control\ndiffuse or fugitive emissions, and by using appropriate enclosures and hoods with efficient extraction and a subsequent\noff-gas cleaning by means of a bag filter or an ESP.","mg/Nm3","N/A",20,"Green","Continuous",0,0,"Unspecified ","Daily mean value","This BAT-AEL is in the case of electrostatic precipitators if the emissions from hot metal pretreatment and the secondary metallurgy are treated separately "]
["Iron and steel","2. Production and processing of metals","Other","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: Waste water from continous casting machines ","Air","Particulates (PM10) (24 hr Mean)","BAT is to minimise the waste water discharge from continuous casting by using the following techniques in combination: (i) the removal of solids by flocculation, sedimentation and/or filtration; (ii) the removal of oil in skimming tanks or any other effective device; (iii) the recirculation of cooling water and water from vacuum generation as much as possible.","mg/l","N/A",20,"Green","Discontinuous ",0,0,"Unspecified ","Random sample or a 24 hour composite sample ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Other","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: Waste water from continous casting machines ","Air","Particulates (PM10) (24 hr Mean)","BAT is to minimise the waste water discharge from continuous casting by using the following techniques in combination: (i) the removal of solids by flocculation, sedimentation and/or filtration; (ii) the removal of oil in skimming tanks or any other effective device; (iii) the recirculation of cooling water and water from vacuum generation as much as possible.","mg/l","N/A",20,"Green","Discontinuous ",0,0,"Unspecified ","Random sample or a 24 hour composite sample ",0]
["Iron and steel","2. Production and processing of metals","Other","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: Waste water from continous casting machines ","Air","Particulates (PM10) (24 hr Mean)","BAT is to minimise the waste water discharge from continuous casting by using the following techniques in combination: (i) the removal of solids by flocculation, sedimentation and/or filtration; (ii) the removal of oil in skimming tanks or any other effective device; (iii) the recirculation of cooling water and water from vacuum generation as much as possible.","mg/l","N/A",5,"Green","Discontinuous ",0,0,"Unspecified ","Random sample or a 24 hour composite sample ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Other","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: Waste water from continous casting machines ","Air","Particulates (PM10) (24 hr Mean)","BAT is to minimise the waste water discharge from continuous casting by using the following techniques in combination: (i) the removal of solids by flocculation, sedimentation and/or filtration; (ii) the removal of oil in skimming tanks or any other effective device; (iii) the recirculation of cooling water and water from vacuum generation as much as possible.","mg/l","N/A",5,"Green","Discontinuous ",0,0,"Unspecified ","Random sample or a 24 hour composite sample ",0]
["Iron and steel","2. Production and processing of metals","Other","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: Waste water from continous casting machines ","Air","Particulates (PM10) (24 hr Mean)","BAT is to minimise the waste water discharge from continuous casting by using the following techniques in combination: (i) the removal of solids by flocculation, sedimentation and/or filtration; (ii) the removal of oil in skimming tanks or any other effective device; (iii) the recirculation of cooling water and water from vacuum generation as much as possible.","mg/l","N/A",2,"Green","Discontinuous ",0,0,"Unspecified ","Random sample or a 24 hour composite sample ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Other","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: Waste water from continous casting machines ","Air","Particulates (PM10) (24 hr Mean)","BAT is to minimise the waste water discharge from continuous casting by using the following techniques in combination: (i) the removal of solids by flocculation, sedimentation and/or filtration; (ii) the removal of oil in skimming tanks or any other effective device; (iii) the recirculation of cooling water and water from vacuum generation as much as possible.","mg/l","N/A",2,"Green","Discontinuous ",0,0,"Unspecified ","Random sample or a 24 hour composite sample ",0]
["Iron and steel","2. Production and processing of metals","Other","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: Waste water from continous casting machines ","Air","Particulates (PM10) (24 hr Mean)","BAT is to minimise the waste water discharge from continuous casting by using the following techniques in combination: (i) the removal of solids by flocculation, sedimentation and/or filtration; (ii) the removal of oil in skimming tanks or any other effective device; (iii) the recirculation of cooling water and water from vacuum generation as much as possible.","mg/l","N/A",0.5,"Green","Discontinuous ",0,0,"Unspecified ","Random sample or a 24 hour composite sample ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Other","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: Waste water from continous casting machines ","Air","Particulates (PM10) (24 hr Mean)","BAT is to minimise the waste water discharge from continuous casting by using the following techniques in combination: (i) the removal of solids by flocculation, sedimentation and/or filtration; (ii) the removal of oil in skimming tanks or any other effective device; (iii) the recirculation of cooling water and water from vacuum generation as much as possible.","mg/l","N/A",0.5,"Green","Discontinuous ",0,0,"Unspecified ","Random sample or a 24 hour composite sample ",0]
["Iron and steel","2. Production and processing of metals","Other","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: Waste water from continous casting machines ","Air","Particulates (PM10) (24 hr Mean)","BAT is to minimise the waste water discharge from continuous casting by using the following techniques in combination: (i) the removal of solids by flocculation, sedimentation and/or filtration; (ii) the removal of oil in skimming tanks or any other effective device; (iii) the recirculation of cooling water and water from vacuum generation as much as possible.","mg/l","N/A",0.5,"Green","Discontinuous ",0,0,"Unspecified ","Random sample or a 24 hour composite sample ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Other","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: Waste water from continous casting machines ","Air","Particulates (PM10) (24 hr Mean)","BAT is to minimise the waste water discharge from continuous casting by using the following techniques in combination: (i) the removal of solids by flocculation, sedimentation and/or filtration; (ii) the removal of oil in skimming tanks or any other effective device; (iii) the recirculation of cooling water and water from vacuum generation as much as possible.","mg/l","N/A",0.5,"Green","Discontinuous ",0,0,"Unspecified ","Random sample or a 24 hour composite sample ",0]
["Iron and steel","2. Production and processing of metals","Other","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: Waste water from continous casting machines ","Air","Particulates (PM10) (24 hr Mean)","BAT is to minimise the waste water discharge from continuous casting by using the following techniques in combination: (i) the removal of solids by flocculation, sedimentation and/or filtration; (ii) the removal of oil in skimming tanks or any other effective device; (iii) the recirculation of cooling water and water from vacuum generation as much as possible.","mg/l","N/A",5,"Green","Discontinuous ",0,0,"Unspecified ","Random sample or a 24 hour composite sample ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Other","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: Waste water from continous casting machines ","Air","Particulates (PM10) (24 hr Mean)","BAT is to minimise the waste water discharge from continuous casting by using the following techniques in combination: (i) the removal of solids by flocculation, sedimentation and/or filtration; (ii) the removal of oil in skimming tanks or any other effective device; (iii) the recirculation of cooling water and water from vacuum generation as much as possible.","mg/l","N/A",5,"Green","Discontinuous ",0,0,"Unspecified ","Random sample or a 24 hour composite sample ",0]
["Iron and steel","2. Production and processing of metals","Other","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Blast Furnaces: Blast furnace gas ","Air","Particulates (PM10) (24 hr Mean)","BAT is to reduce dust emissions from the blast furnace gas by using one or a combination of the following techniques:\n\nUsing dry predusting devices: (i) deflectors; (ii) dust catchers; (iii) cyclones; (iv) electrostatic precipitators.\n\nSubsequent dust abatement: (i) hurdle-type scrubbers; (ii) venturi scrubbers; (iii) annular gap scrubbers; (iv) wet electrostatic precipitators; (v) disintegrators ","mg/Nm3","N/A",10,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Other","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Blast Furnaces: Blast furnace gas ","Air","Particulates (PM10) (24 hr Mean)","BAT is to reduce dust emissions from the blast furnace gas by using one or a combination of the following techniques:\n\nUsing dry predusting devices: (i) deflectors; (ii) dust catchers; (iii) cyclones; (iv) electrostatic precipitators.\n\nSubsequent dust abatement: (i) hurdle-type scrubbers; (ii) venturi scrubbers; (iii) annular gap scrubbers; (iv) wet electrostatic precipitators; (v) disintegrators ","mg/Nm3","N/A",10,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0]
["Iron and steel","2. Production and processing of metals","Other","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Blast Furnaces: casting house ","Air","Particulates (PM10) (24 hr Mean)","BAT for casting house (tap holes, runners, torpedo ladles charging points, skimmers) is to prevent or reduce diffuse dust emissions by using the following techniques: (i) Covering runners; (ii) optimising the capture efficiency for diffuse dust emissions and fumes with subsequent off-gas cleaning by means of\nan electrostatic precipitator or bag filter; (iii) ume suppression using nitrogen while tapping, where applicable and where no collecting and dedusting system for\ntapping emissions is installed.\n","mg/Nm3",1,15,"Amber",0,0,0,"Unspecified ","Daily mean value",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Other","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Blast Furnaces: casting house ","Air","Particulates (PM10) (24 hr Mean)","BAT for casting house (tap holes, runners, torpedo ladles charging points, skimmers) is to prevent or reduce diffuse dust emissions by using the following techniques: (i) Covering runners; (ii) optimising the capture efficiency for diffuse dust emissions and fumes with subsequent off-gas cleaning by means of\nan electrostatic precipitator or bag filter; (iii) ume suppression using nitrogen while tapping, where applicable and where no collecting and dedusting system for\ntapping emissions is installed.\n","mg/Nm3",1,15,"Amber",0,0,0,"Unspecified ","Daily mean value",0]
["Iron and steel","2. Production and processing of metals","Other","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Blast Furnaces: Hot blast stoves","Air","Particulates (PM10) (24 hr Mean)","BAT for hot blast stoves is to reduce emissions by using desulphurised and dedusted surplus coke oven gas, dedusted blast furnace gas, dedusted basic oxygen furnace gas and natural gas, individually or in combination.","mg/Nm3","N/A",10,"Green","Discontinuous ",0,0,0.03,"Daily mean values",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Other","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Blast Furnaces: Hot blast stoves","Air","Particulates (PM10) (24 hr Mean)","BAT for hot blast stoves is to reduce emissions by using desulphurised and dedusted surplus coke oven gas, dedusted blast furnace gas, dedusted basic oxygen furnace gas and natural gas, individually or in combination.","mg/Nm3","N/A",10,"Green","Discontinuous ",0,0,0.03,"Daily mean values",0]
["Iron and steel","2. Production and processing of metals","Other","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Blast Furnaces: Loading from the storage bunkers of the coal injection unit","Air","Particulates (PM10) (24 hr Mean)","BAT for displaced air during loading from the storage bunkers of the coal injection unit is to capture dust emissions and perform subsequent dry dedusting.","mg/Nm3","N/A",20,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Other","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Blast Furnaces: Loading from the storage bunkers of the coal injection unit","Air","Particulates (PM10) (24 hr Mean)","BAT for displaced air during loading from the storage bunkers of the coal injection unit is to capture dust emissions and perform subsequent dry dedusting.","mg/Nm3","N/A",20,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0]
["Iron and steel","2. Production and processing of metals","Other","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Electric arc furnace steelmaking and casting: Electric Arc Furnace (EAF) primary and secondary dedusting","Air","Particulates (PM10) (24 hr Mean)","BAT for the electric arc furnace (EAF) primary and secondary dedusting (including scrap preheating, charging, melting, tapping, ladle furnace and secondary metallurgy) is to achieve an efficient extraction of all emission sources by using one of the techniques listed below and to use subsequent dedusting by means of a bag filter: (i) a combination of direct off-gas extraction (4th or 2nd hole) and hood systems; (ii) direct gas extraction and doghouse systems; (iii) direct gas extraction and total building evacuation (low-capacity electric arc furnaces (EAF) may not require direct gas\nextraction to achieve the same extraction efficiency)\n\n","mg/Nm3","N/A",5,"Green","Continuous",0,0,"Unspecified ","Daily mean value",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Other","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Electric arc furnace steelmaking and casting: Electric Arc Furnace (EAF) primary and secondary dedusting","Air","Particulates (PM10) (24 hr Mean)","BAT for the electric arc furnace (EAF) primary and secondary dedusting (including scrap preheating, charging, melting, tapping, ladle furnace and secondary metallurgy) is to achieve an efficient extraction of all emission sources by using one of the techniques listed below and to use subsequent dedusting by means of a bag filter: (i) a combination of direct off-gas extraction (4th or 2nd hole) and hood systems; (ii) direct gas extraction and doghouse systems; (iii) direct gas extraction and total building evacuation (low-capacity electric arc furnaces (EAF) may not require direct gas\nextraction to achieve the same extraction efficiency)\n\n","mg/Nm3","N/A",5,"Green","Continuous",0,0,"Unspecified ","Daily mean value",0]
["Iron and steel","2. Production and processing of metals","Other","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Electric arc furnace steelmaking and casting: On-site slag processing ","Air","Particulates (PM10) (24 hr Mean)","BAT for on-site slag processing is to reduce dust emissions by using one or a combination of the following techniques: (i) efficient extraction of the slag crusher and screening devices with subsequent off-gas cleaning, if relevant; (ii) transport of untreated slag by shovel loaders; (iii) extraction or wetting of conveyor transfer points for broken material; (iv) wetting of slag storage heaps; (v) use of water fogs when broken slag is loaded","mg/Nm3",10,20,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Other","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Electric arc furnace steelmaking and casting: On-site slag processing ","Air","Particulates (PM10) (24 hr Mean)","BAT for on-site slag processing is to reduce dust emissions by using one or a combination of the following techniques: (i) efficient extraction of the slag crusher and screening devices with subsequent off-gas cleaning, if relevant; (ii) transport of untreated slag by shovel loaders; (iii) extraction or wetting of conveyor transfer points for broken material; (iv) wetting of slag storage heaps; (v) use of water fogs when broken slag is loaded","mg/Nm3",10,20,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0]
["Iron and steel","2. Production and processing of metals","Pelletisation plans","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Crushing. Grinding and drying","Air","Particulates (PM10) (24 hr Mean)","BAT is to reduce the dust emissions in the waste gases by using one or a combination of the following techniques: (i) an electrostatic precipitator; (ii) a bag filter; (iii) a wet scrubber","mg/Nm3","N/A",20,"Green","Discontinuous ",0,0,"Unspecified ","Daily mean values",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Pelletisation plans","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Crushing. Grinding and drying","Air","Particulates (PM10) (24 hr Mean)","BAT is to reduce the dust emissions in the waste gases by using one or a combination of the following techniques: (i) an electrostatic precipitator; (ii) a bag filter; (iii) a wet scrubber","mg/Nm3","N/A",20,"Green","Discontinuous ",0,0,"Unspecified ","Daily mean values",0]
["Iron and steel","2. Production and processing of metals","Pelletisation plans","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Induration strand; Pellet handling and screening ","Air","Particulates (PM10) (24 hr Mean)","BAT is to reduce the dust emissions in the waste gases by using one or a combination of the following techniques: (i) an electrostatic precipitator; (ii) a bag filter; (iii) a wet scrubber","mg/Nm3",10,15,"Green","Discontinuous ",0,0,"Unspecified ","Daily mean values",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Pelletisation plans","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Induration strand; Pellet handling and screening ","Air","Particulates (PM10) (24 hr Mean)","BAT is to reduce the dust emissions in the waste gases by using one or a combination of the following techniques: (i) an electrostatic precipitator; (ii) a bag filter; (iii) a wet scrubber","mg/Nm3",10,15,"Green","Discontinuous ",0,0,"Unspecified ","Daily mean values",0]
["Iron and steel","2. Production and processing of metals","Sinter Plant","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Sinter strand","Air","Particulates (PM10) (24 hr Mean)","BAT for primary emissions for existing plants is to reduce dust emissions from the sinter strand waste gas by using\nadvanced electrostatic precipitators when bag filters are not applicable.","mg/Nm3",20,40,"Green","Continuous",0,0,"Unspecified ","Daily mean value","The advanced electrostatic precipitator  should be designed and operated to achieve these values",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Sinter Plant","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Sinter strand","Air","Particulates (PM10) (24 hr Mean)","BAT for primary emissions for existing plants is to reduce dust emissions from the sinter strand waste gas by using\nadvanced electrostatic precipitators when bag filters are not applicable.","mg/Nm3",20,40,"Green","Continuous",0,0,"Unspecified ","Daily mean value","The advanced electrostatic precipitator  should be designed and operated to achieve these values"]
["Iron and steel","2. Production and processing of metals","Sinter Plant","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Sinter strand","Air","Particulates (PM10) (24 hr Mean)","BAT for primary emissions from sinter plants is to reduce dust emissions from the sinter strand waste gas by means of a bag filter.\n\n","mg/Nm3",1,15,"Green","Continuous",0,0,"Unspecified ","Daily mean value",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Sinter Plant","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Sinter strand","Air","Particulates (PM10) (24 hr Mean)","BAT for primary emissions from sinter plants is to reduce dust emissions from the sinter strand waste gas by means of a bag filter.\n\n","mg/Nm3",1,15,"Green","Continuous",0,0,"Unspecified ","Daily mean value",0]
["Iron and steel","2. Production and processing of metals","Sinter Plant","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Sinter strand","Air","Particulates (PM10) (24 hr Mean)","BAT for secondary emissions from sinter strand discharge, sinter crushing, cooling, screening and conveyor transfer points is to prevent dust emissions and/or to achieve an efficient extraction and subsequently to reduce dust emissions by using : an electrostatic precipitator or a bag filter","mg/Nm3","N/A",30,"Green","Continuous",0,0,"Unspecified ","Daily mean value",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Sinter Plant","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Sinter strand","Air","Particulates (PM10) (24 hr Mean)","BAT for secondary emissions from sinter strand discharge, sinter crushing, cooling, screening and conveyor transfer points is to prevent dust emissions and/or to achieve an efficient extraction and subsequently to reduce dust emissions by using : an electrostatic precipitator or a bag filter","mg/Nm3","N/A",30,"Green","Continuous",0,0,"Unspecified ","Daily mean value",0]
["Iron and steel","2. Production and processing of metals","Sinter Plant","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Sinter strand","Air","Particulates (PM10) (24 hr Mean)","BAT for secondary emissions from sinter strand discharge, sinter crushing, cooling, screening and conveyor transfer points is to prevent dust emissions and/or to achieve an efficient extraction and subsequently to reduce dust emissions by using : Hooding and/or enclosure","mg/Nm3","N/A",10,"Green","Continuous",0,0,"Unspecified ","Daily mean value",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Sinter Plant","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Sinter strand","Air","Particulates (PM10) (24 hr Mean)","BAT for secondary emissions from sinter strand discharge, sinter crushing, cooling, screening and conveyor transfer points is to prevent dust emissions and/or to achieve an efficient extraction and subsequently to reduce dust emissions by using : Hooding and/or enclosure","mg/Nm3","N/A",10,"Green","Continuous",0,0,"Unspecified ","Daily mean value",0]
["Iron and steel","2. Production and processing of metals","Coke Oven Plants","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Coal charging systems ","Air","Particulates (PM10) (24 hr Mean)","BAT is to charge coke oven chambers with emission-reduced charging systems. \n\nIf, however, the gases are extracted and treated outside the coke oven, charging with a land-based treatment of the\nextracted gases is the preferred method. Treatment should consist of an efficient extraction of the emissions with\nsubsequent combustion to reduce organic compounds and the use of a bag filter to reduce particulates.","g/t","N/A",5,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Coke Oven Plants","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Coal charging systems ","Air","Particulates (PM10) (24 hr Mean)","BAT is to charge coke oven chambers with emission-reduced charging systems. \n\nIf, however, the gases are extracted and treated outside the coke oven, charging with a land-based treatment of the\nextracted gases is the preferred method. Treatment should consist of an efficient extraction of the emissions with\nsubsequent combustion to reduce organic compounds and the use of a bag filter to reduce particulates.","g/t","N/A",5,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0]
["Iron and steel","2. Production and processing of metals","Coke Oven Plants","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Coal charging systems ","Air","Particulates (PM10) (24 hr Mean)","BAT is to charge coke oven chambers with emission-reduced charging systems. \n\nIf, however, the gases are extracted and treated outside the coke oven, charging with a land-based treatment of the\nextracted gases is the preferred method. Treatment should consist of an efficient extraction of the emissions with\nsubsequent combustion to reduce organic compounds and the use of a bag filter to reduce particulates.","mg/Nm3","N/A",50,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Coke Oven Plants","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Coal charging systems ","Air","Particulates (PM10) (24 hr Mean)","BAT is to charge coke oven chambers with emission-reduced charging systems. \n\nIf, however, the gases are extracted and treated outside the coke oven, charging with a land-based treatment of the\nextracted gases is the preferred method. Treatment should consist of an efficient extraction of the emissions with\nsubsequent combustion to reduce organic compounds and the use of a bag filter to reduce particulates.","mg/Nm3","N/A",50,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0]
["Iron and steel","2. Production and processing of metals","Coke Oven Plants","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Storage and handling of pulverised coal","Air","Particulates (PM10) (24 hr Mean)","BAT for storage and handling of pulverised coal is to prevent or reduce diffuse dust emissions by using one or a combination of the following techniques: (i) storing pulverised materials in bunkers and warehouses; (ii) using closed or enclosed conveyors; (iii)  minimising the drop heights depending on the plant size and construction; (iv) reducing emissions from charging of the coal tower and the charging car; (v) using efficient extraction and subsequent dedusting\n","mg/Nm3",10,20,"Amber",0,0,0,"Unspecified ","Average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Coke Oven Plants","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Storage and handling of pulverised coal","Air","Particulates (PM10) (24 hr Mean)","BAT for storage and handling of pulverised coal is to prevent or reduce diffuse dust emissions by using one or a combination of the following techniques: (i) storing pulverised materials in bunkers and warehouses; (ii) using closed or enclosed conveyors; (iii)  minimising the drop heights depending on the plant size and construction; (iv) reducing emissions from charging of the coal tower and the charging car; (v) using efficient extraction and subsequent dedusting\n","mg/Nm3",10,20,"Amber",0,0,0,"Unspecified ","Average over the sampling period",0]
["Iron and steel","2. Production and processing of metals","Pelletisation plans","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Induration strand","Air","Hydrogen chloride","BAT is to reduce the sulphur oxides (SOX), hydrogen chloride (HCl) and hydrogen fluoride (HF) emissions from the\ninduration strand waste gas by using one of the following techniques: (i) a wet scrubber; (ii) semi-dry absorption with a subsequent dedusting system","mg/Nm3",1,3,"Green","Discontinuous ","Unspecified ","Unspecified ","Unspecified ","Daily mean values",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Pelletisation plans","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Induration strand","Air","Hydrogen chloride","BAT is to reduce the sulphur oxides (SOX), hydrogen chloride (HCl) and hydrogen fluoride (HF) emissions from the\ninduration strand waste gas by using one of the following techniques: (i) a wet scrubber; (ii) semi-dry absorption with a subsequent dedusting system","mg/Nm3",1,3,"Green","Discontinuous ","Unspecified ","Unspecified ","Unspecified ","Daily mean values",0]
["Iron and steel","2. Production and processing of metals","Pelletisation plans","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Induration strand","Air","Hydrogen fluoride (as F) (Ecological - Daily Mean)","BAT is to reduce the sulphur oxides (SOX), hydrogen chloride (HCl) and hydrogen fluoride (HF) emissions from the\ninduration strand waste gas by using one of the following techniques: (i) a wet scrubber; (ii) semi-dry absorption with a subsequent dedusting system","mg/Nm3",1,3,"Green","Discontinuous ","Unspecified ","Unspecified ","Unspecified ","Daily mean values",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Pelletisation plans","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Induration strand","Air","Hydrogen fluoride (as F) (Ecological - Daily Mean)","BAT is to reduce the sulphur oxides (SOX), hydrogen chloride (HCl) and hydrogen fluoride (HF) emissions from the\ninduration strand waste gas by using one of the following techniques: (i) a wet scrubber; (ii) semi-dry absorption with a subsequent dedusting system","mg/Nm3",1,3,"Green","Discontinuous ","Unspecified ","Unspecified ","Unspecified ","Daily mean values",0]
["Iron and steel","2. Production and processing of metals","Other","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Electric arc furnace steelmaking and casting: Waste water from continous casting machines ","Air","Iron","BAT is to minimise the waste water discharge from continuous casting by using the following techniques in combination: (i) the removal of solids by flocculation, sedimentation and/or filtration; (ii) the removal of oil in skimming tanks or any other effective device; (iii) the recirculation of cooling water and water from vacuum generation as much as possible","mg/Nm3","N/A",5,"Green","Discontinuous ",0,0,"Unspecified ","Qualified random sample or a 24 hour composite",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Other","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Electric arc furnace steelmaking and casting: Waste water from continous casting machines ","Air","Iron","BAT is to minimise the waste water discharge from continuous casting by using the following techniques in combination: (i) the removal of solids by flocculation, sedimentation and/or filtration; (ii) the removal of oil in skimming tanks or any other effective device; (iii) the recirculation of cooling water and water from vacuum generation as much as possible","mg/Nm3","N/A",5,"Green","Discontinuous ",0,0,"Unspecified ","Qualified random sample or a 24 hour composite",0]
["Iron and steel","2. Production and processing of metals","Other","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Electric arc furnace steelmaking and casting: Electric Arc Furnace (EAF) primary and secondary dedusting","Air","Mercury and compounds, except mercury alkyls, (as","BAT for the electric arc furnace (EAF) primary and secondary dedusting (including scrap preheating, charging, melting, tapping, ladle furnace and secondary metallurgy) is to achieve an efficient extraction of all emission sources by using one of the techniques listed below and to use subsequent dedusting by means of a bag filter: (i) a combination of direct off-gas extraction (4th or 2nd hole) and hood systems; (ii) direct gas extraction and doghouse systems; (iii) direct gas extraction and total building evacuation (low-capacity electric arc furnaces (EAF) may not require direct gas\nextraction to achieve the same extraction efficiency)\n\n","mg/Nm3","N/A",0.05,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Other","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Electric arc furnace steelmaking and casting: Electric Arc Furnace (EAF) primary and secondary dedusting","Air","Mercury and compounds, except mercury alkyls, (as","BAT for the electric arc furnace (EAF) primary and secondary dedusting (including scrap preheating, charging, melting, tapping, ladle furnace and secondary metallurgy) is to achieve an efficient extraction of all emission sources by using one of the techniques listed below and to use subsequent dedusting by means of a bag filter: (i) a combination of direct off-gas extraction (4th or 2nd hole) and hood systems; (ii) direct gas extraction and doghouse systems; (iii) direct gas extraction and total building evacuation (low-capacity electric arc furnaces (EAF) may not require direct gas\nextraction to achieve the same extraction efficiency)\n\n","mg/Nm3","N/A",0.05,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0]
["Iron and steel","2. Production and processing of metals","Sinter Plant","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Sinter strand","Air","Mercury and compounds, except mercury alkyls, (as","BAT for primary emissions from sinter strands is to prevent or reduce mercury emissions by selecting raw materials with a low mercury content or to treat waste gases in combination with activated carbon or\nactivated lignite coke injection.","mg/Nm3",0.03,0.05,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period","Discontinuous measurement, spot samples for at least half an hour",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Sinter Plant","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Sinter strand","Air","Mercury and compounds, except mercury alkyls, (as","BAT for primary emissions from sinter strands is to prevent or reduce mercury emissions by selecting raw materials with a low mercury content or to treat waste gases in combination with activated carbon or\nactivated lignite coke injection.","mg/Nm3",0.03,0.05,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period","Discontinuous measurement, spot samples for at least half an hour"]
["Iron and steel","2. Production and processing of metals","Other","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Electric arc furnace steelmaking and casting: Waste water from continous casting machines ","Air","Nickel (total Ni compounds in the PM10 fraction)","BAT is to minimise the waste water discharge from continuous casting by using the following techniques in combination: (i) the removal of solids by flocculation, sedimentation and/or filtration; (ii) the removal of oil in skimming tanks or any other effective device; (iii) the recirculation of cooling water and water from vacuum generation as much as possible","mg/Nm3","N/A",0.5,"Green","Discontinuous ",0,0,"Unspecified ","Qualified random sample or a 24 hour composite",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Other","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Electric arc furnace steelmaking and casting: Waste water from continous casting machines ","Air","Nickel (total Ni compounds in the PM10 fraction)","BAT is to minimise the waste water discharge from continuous casting by using the following techniques in combination: (i) the removal of solids by flocculation, sedimentation and/or filtration; (ii) the removal of oil in skimming tanks or any other effective device; (iii) the recirculation of cooling water and water from vacuum generation as much as possible","mg/Nm3","N/A",0.5,"Green","Discontinuous ",0,0,"Unspecified ","Qualified random sample or a 24 hour composite",0]
["Iron and steel","2. Production and processing of metals","Coke Oven Plants","Unspecified","Unspecified","Newor substantially revamped","Unspecified","Unspecified","Unspecified","Air","Nitrogen dioxide","BAT for the coke oven underfiring is to reduce the emissions by using the following techniques: (i) preventing leakage between the oven chamber and the heating chamber by means of regular coke oven operation; (ii) repairing leakage between the oven chamber and the heating chamber (only applicable to existing plants); (iii) incorporating low-nitrogen oxides (NOX) techniques in the construction of new batteries, such as staged combustion\nand the use of thinner bricks and refractory with a better thermal conductivity (only applicable to new plants); (iv) using desulphurised coke oven gas (COG) process gases ","mg/Nm3",350,500,"Green","Discontinuous ",0,0,0.05,"Daily mean average","This BAT is for new or substantially revamped\nplants (less than 10 years old)",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Coke Oven Plants","Unspecified","Unspecified","Newor substantially revamped","Unspecified","Unspecified","Unspecified","Air","Nitrogen dioxide","BAT for the coke oven underfiring is to reduce the emissions by using the following techniques: (i) preventing leakage between the oven chamber and the heating chamber by means of regular coke oven operation; (ii) repairing leakage between the oven chamber and the heating chamber (only applicable to existing plants); (iii) incorporating low-nitrogen oxides (NOX) techniques in the construction of new batteries, such as staged combustion\nand the use of thinner bricks and refractory with a better thermal conductivity (only applicable to new plants); (iv) using desulphurised coke oven gas (COG) process gases ","mg/Nm3",350,500,"Green","Discontinuous ",0,0,0.05,"Daily mean average","This BAT is for new or substantially revamped\nplants (less than 10 years old)"]
["Iron and steel","2. Production and processing of metals","Coke Oven Plants","Unspecified","Unspecified","Existing","Unspecified","Unspecified","Unspecified","Air","Nitrogen dioxide","BAT for the coke oven underfiring is to reduce the emissions by using the following techniques: (i) preventing leakage between the oven chamber and the heating chamber by means of regular coke oven operation; (ii) repairing leakage between the oven chamber and the heating chamber (only applicable to existing plants); (iii) incorporating low-nitrogen oxides (NOX) techniques in the construction of new batteries, such as staged combustion\nand the use of thinner bricks and refractory with a better thermal conductivity (only applicable to new plants); (iv) using desulphurised coke oven gas (COG) process gases ","mg/Nm3",500,650,"Green","Discontinuous ",0,0,0.05,"Daily mean average","This BAT is for older plants with well maintained batteries and incorporated low- nitrogen oxides (NOX) techniques.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Coke Oven Plants","Unspecified","Unspecified","Existing","Unspecified","Unspecified","Unspecified","Air","Nitrogen dioxide","BAT for the coke oven underfiring is to reduce the emissions by using the following techniques: (i) preventing leakage between the oven chamber and the heating chamber by means of regular coke oven operation; (ii) repairing leakage between the oven chamber and the heating chamber (only applicable to existing plants); (iii) incorporating low-nitrogen oxides (NOX) techniques in the construction of new batteries, such as staged combustion\nand the use of thinner bricks and refractory with a better thermal conductivity (only applicable to new plants); (iv) using desulphurised coke oven gas (COG) process gases ","mg/Nm3",500,650,"Green","Discontinuous ",0,0,0.05,"Daily mean average","This BAT is for older plants with well maintained batteries and incorporated low- nitrogen oxides (NOX) techniques."]
["Iron and steel","2. Production and processing of metals","Sinter Plant","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Sinter strand","Air","Nitrogen dioxide","BAT for primary emissions from sinter strands is to reduce total nitrogen oxides (NOX) emissions by using one or\na combination of the following techniques:\n\nProcess integrated measures which can include: (i) waste gas recirculation; (ii) other primary measures, such as the use of anthracite or the use of low-NOX burners for ignition\n\n","mg/Nm3","N/A",500,"Green","Continuous",0,0,"Unspecified ","Daily mean value",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Sinter Plant","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Sinter strand","Air","Nitrogen dioxide","BAT for primary emissions from sinter strands is to reduce total nitrogen oxides (NOX) emissions by using one or\na combination of the following techniques:\n\nProcess integrated measures which can include: (i) waste gas recirculation; (ii) other primary measures, such as the use of anthracite or the use of low-NOX burners for ignition\n\n","mg/Nm3","N/A",500,"Green","Continuous",0,0,"Unspecified ","Daily mean value",0]
["Iron and steel","2. Production and processing of metals","Sinter Plant","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Sinter strand","Air","Nitrogen dioxide","End-of-pipe techniques which can include:  selective catalytic reduction (SCR)","mg/Nm3","N/A",120,"Green","Continuous",0,0,0.15,"Daily mean value",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Sinter Plant","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Sinter strand","Air","Nitrogen dioxide","End-of-pipe techniques which can include:  selective catalytic reduction (SCR)","mg/Nm3","N/A",120,"Green","Continuous",0,0,0.15,"Daily mean value",0]
["Iron and steel","2. Production and processing of metals","Sinter Plant","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Sinter strand","Air","Nitrogen dioxide","End-of-pipe techniques which can include: the regenerative activated carbon (RAC) process","mg/Nm3","N/A",250,"Green","Continuous",0,0,0.15,"Daily mean value",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Sinter Plant","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Sinter strand","Air","Nitrogen dioxide","End-of-pipe techniques which can include: the regenerative activated carbon (RAC) process","mg/Nm3","N/A",250,"Green","Continuous",0,0,0.15,"Daily mean value",0]
["Iron and steel","2. Production and processing of metals","Other","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Blast Furnaces: Hot blast stoves","Air","Nitrogen dioxide","BAT for hot blast stoves is to reduce emissions by using desulphurised and dedusted surplus coke oven gas, dedusted blast furnace gas, dedusted basic oxygen furnace gas and natural gas, individually or in combination.","mg/Nm3","N/A",100,"Green","Discontinuous ",0,0,0.03,"Daily mean values",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Other","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Blast Furnaces: Hot blast stoves","Air","Nitrogen dioxide","BAT for hot blast stoves is to reduce emissions by using desulphurised and dedusted surplus coke oven gas, dedusted blast furnace gas, dedusted basic oxygen furnace gas and natural gas, individually or in combination.","mg/Nm3","N/A",100,"Green","Discontinuous ",0,0,0.03,"Daily mean values",0]
["Iron and steel","2. Production and processing of metals","Other","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Electric arc furnace steelmaking and casting: Electric Arc Furnace (EAF) primary and secondary dedusting","Air","PCDD/F","BAT for the electric arc furnace (EAF) primary and secondary dedusting (including scrap preheating, charging, melting, tapping, ladle furnace and secondary metallurgy) is to prevent and reduce polychlorinated dibenzodioxins/furans (PCDD/F) and polychlorinated biphenyls (PCB) emissions by avoiding, as much as possible, raw materials which contain PCDD/F and PCB or their precursors (see BAT 6 and 7) and using one or a combination of the following techniques, in conjunction with an appropriate dust removal system: (i) appropriate post-combustion; (ii) appropriate rapid quenching; (iii) injection of adequate adsorption agents into the duct before dedusting.","ng I-TEQ/Nm3","N/A",0.1,"Green","Discontinuous ",0,0,"Unspecified ","6-8 hour random sample","In some cases, the BAT-associated emission level can be achieved with primary measures only.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Other","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Electric arc furnace steelmaking and casting: Electric Arc Furnace (EAF) primary and secondary dedusting","Air","PCDD/F","BAT for the electric arc furnace (EAF) primary and secondary dedusting (including scrap preheating, charging, melting, tapping, ladle furnace and secondary metallurgy) is to prevent and reduce polychlorinated dibenzodioxins/furans (PCDD/F) and polychlorinated biphenyls (PCB) emissions by avoiding, as much as possible, raw materials which contain PCDD/F and PCB or their precursors (see BAT 6 and 7) and using one or a combination of the following techniques, in conjunction with an appropriate dust removal system: (i) appropriate post-combustion; (ii) appropriate rapid quenching; (iii) injection of adequate adsorption agents into the duct before dedusting.","ng I-TEQ/Nm3","N/A",0.1,"Green","Discontinuous ",0,0,"Unspecified ","6-8 hour random sample","In some cases, the BAT-associated emission level can be achieved with primary measures only."]
["Iron and steel","2. Production and processing of metals","Sinter Plant","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Sinter strand","Air","PCDD/F","BAT for primary emissions from sinter strands is to reduce emissions of polychlorinated dibenzodioxins/furans (PCDD/F) and polychlorinated biphenyls (PCB) by the injection of adequate adsorption agents into the waste gas duct of the sinter strand before dedusting with a bag filter ","ng I-TEQ/Nm3",0.05,0.2,"Green","Discontinuous ",0,0,0,0,0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Sinter Plant","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Sinter strand","Air","PCDD/F","BAT for primary emissions from sinter strands is to reduce emissions of polychlorinated dibenzodioxins/furans (PCDD/F) and polychlorinated biphenyls (PCB) by the injection of adequate adsorption agents into the waste gas duct of the sinter strand before dedusting with a bag filter ","ng I-TEQ/Nm3",0.05,0.2,"Green","Discontinuous ",0,0,0,0,0]
["Iron and steel","2. Production and processing of metals","Sinter Plant","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Sinter strand","Air","PCDD/F","BAT for primary emissions from sinter strands is to reduce emissions of polychlorinated dibenzodioxins/furans (PCDD/F) and polychlorinated biphenyls (PCB) by the injection of adequate adsorption agents into the waste gas duct of the sinter strand before dedusting with an advanced electrostatic precipitators when bag filters are not applicable","ng I-TEQ/Nm3",0.2,0.4,"Green","Discontinuous ",0,0,"Unspecified ","6-8 hour random sample",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Sinter Plant","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Sinter strand","Air","PCDD/F","BAT for primary emissions from sinter strands is to reduce emissions of polychlorinated dibenzodioxins/furans (PCDD/F) and polychlorinated biphenyls (PCB) by the injection of adequate adsorption agents into the waste gas duct of the sinter strand before dedusting with an advanced electrostatic precipitators when bag filters are not applicable","ng I-TEQ/Nm3",0.2,0.4,"Green","Discontinuous ",0,0,"Unspecified ","6-8 hour random sample",0]
["Iron and steel","2. Production and processing of metals","Coke Oven Plants","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Coke oven gas (COG)","Air","Hydrogen sulphide","BAT is to reduce the sulphur content of the coke oven gas (COG) by: (i) desulphurisation by absorption systems","mg/Nm3",300,1000,"Green","Discontinuous ",0,0,"Unspecified ","Daily mean average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Coke Oven Plants","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Coke oven gas (COG)","Air","Hydrogen sulphide","BAT is to reduce the sulphur content of the coke oven gas (COG) by: (i) desulphurisation by absorption systems","mg/Nm3",300,1000,"Green","Discontinuous ",0,0,"Unspecified ","Daily mean average",0]
["Iron and steel","2. Production and processing of metals","Coke Oven Plants","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Coke oven gas (COG)","Air","Hydrogen sulphide","BAT is to reduce the sulphur content of the coke oven gas (COG) by: (ii)  wet oxidative desulphurisation","mg/Nm3","N/A",10,"Green","Discontinuous ",0,0,"Unspecified ","Daily mean average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Coke Oven Plants","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Coke oven gas (COG)","Air","Hydrogen sulphide","BAT is to reduce the sulphur content of the coke oven gas (COG) by: (ii)  wet oxidative desulphurisation","mg/Nm3","N/A",10,"Green","Discontinuous ",0,0,"Unspecified ","Daily mean average",0]
["Iron and steel","2. Production and processing of metals","Sinter Plant","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Sinter strand","Air","Sulphur Dioxide (24 Hour Mean)","BAT for primary emissions from sinter strands is to reduce sulphur oxide (SOX) emissions by using one or a\ncombination of the following techniques: (i)lowering the sulphur input by using coke breeze with a low sulphur content; (ii) lowering the sulphur input by minimisation of coke breeze consumption; (iii)  lowering the sulphur input by using iron ore with a low sulphur content; (iv) injection of adequate adsorption agents into the waste gas duct of the sinter strand before dedusting by bag filter","mg/Nm3",350,500,"Green","Continuous",0,0,"Unspecified ","Daily mean value","The lower value is assoviated with BAT (iv) ",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Sinter Plant","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Sinter strand","Air","Sulphur Dioxide (24 Hour Mean)","BAT for primary emissions from sinter strands is to reduce sulphur oxide (SOX) emissions by using one or a\ncombination of the following techniques: (i)lowering the sulphur input by using coke breeze with a low sulphur content; (ii) lowering the sulphur input by minimisation of coke breeze consumption; (iii)  lowering the sulphur input by using iron ore with a low sulphur content; (iv) injection of adequate adsorption agents into the waste gas duct of the sinter strand before dedusting by bag filter","mg/Nm3",350,500,"Green","Continuous",0,0,"Unspecified ","Daily mean value","The lower value is assoviated with BAT (iv) "]
["Iron and steel","2. Production and processing of metals","Sinter Plant","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Sinter strand","Air","Sulphur Dioxide (24 Hour Mean)","Wet desulphurisation or regenerative activated carbon (RAC) process (with particular consideration for the prerequisites for application)","mg/Nm3","N/A",100,"Green","Continuous",0,0,"Unspecified ","Daily mean value",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Sinter Plant","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Sinter strand","Air","Sulphur Dioxide (24 Hour Mean)","Wet desulphurisation or regenerative activated carbon (RAC) process (with particular consideration for the prerequisites for application)","mg/Nm3","N/A",100,"Green","Continuous",0,0,"Unspecified ","Daily mean value",0]
["Iron and steel","2. Production and processing of metals","Coke Oven Plants","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","BAT for the coke oven underfiring is to reduce the emissions by using the following techniques: (i) preventing leakage between the oven chamber and the heating chamber by means of regular coke oven operation; (ii) repairing leakage between the oven chamber and the heating chamber (only applicable to existing plants); (iii) incorporating low-nitrogen oxides (NOX) techniques in the construction of new batteries, such as staged combustion\nand the use of thinner bricks and refractory with a better thermal conductivity (only applicable to new plants); (iv) using desulphurised coke oven gas (COG) process gases ","mg/Nm3",200,500,"Green","Discontinuous ",0,0,0.05,"Daily mean average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Coke Oven Plants","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","BAT for the coke oven underfiring is to reduce the emissions by using the following techniques: (i) preventing leakage between the oven chamber and the heating chamber by means of regular coke oven operation; (ii) repairing leakage between the oven chamber and the heating chamber (only applicable to existing plants); (iii) incorporating low-nitrogen oxides (NOX) techniques in the construction of new batteries, such as staged combustion\nand the use of thinner bricks and refractory with a better thermal conductivity (only applicable to new plants); (iv) using desulphurised coke oven gas (COG) process gases ","mg/Nm3",200,500,"Green","Discontinuous ",0,0,0.05,"Daily mean average",0]
["Iron and steel","2. Production and processing of metals","Pelletisation plans","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Induration strand","Air","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce the sulphur oxides (SOX), hydrogen chloride (HCl) and hydrogen fluoride (HF) emissions from the\ninduration strand waste gas by using one of the following techniques: (i) a wet scrubber; (ii) semi-dry absorption with a subsequent dedusting system","mg/Nm3",30,50,"Green","Continuous",0,0,"Unspecified ","Daily mean values",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Pelletisation plans","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Induration strand","Air","Sulphur Dioxide (24 Hour Mean)","BAT is to reduce the sulphur oxides (SOX), hydrogen chloride (HCl) and hydrogen fluoride (HF) emissions from the\ninduration strand waste gas by using one of the following techniques: (i) a wet scrubber; (ii) semi-dry absorption with a subsequent dedusting system","mg/Nm3",30,50,"Green","Continuous",0,0,"Unspecified ","Daily mean values",0]
["Iron and steel","2. Production and processing of metals","Other","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Blast Furnaces: Hot blast stoves","Air","Sulphur Dioxide (24 Hour Mean)","BAT for hot blast stoves is to reduce emissions by using desulphurised and dedusted surplus coke oven gas, dedusted blast furnace gas, dedusted basic oxygen furnace gas and natural gas, individually or in combination.","mg/Nm3","N/A",200,"Green","Discontinuous ",0,0,0.03,"Daily mean values",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Other","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Blast Furnaces: Hot blast stoves","Air","Sulphur Dioxide (24 Hour Mean)","BAT for hot blast stoves is to reduce emissions by using desulphurised and dedusted surplus coke oven gas, dedusted blast furnace gas, dedusted basic oxygen furnace gas and natural gas, individually or in combination.","mg/Nm3","N/A",200,"Green","Discontinuous ",0,0,0.03,"Daily mean values",0]
["Iron and steel","2. Production and processing of metals","Other","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Electric arc furnace steelmaking and casting: Waste water from continous casting machines ","Water","Suspended solids","BAT is to minimise the waste water discharge from continuous casting by using the following techniques in combination: (i) the removal of solids by flocculation, sedimentation and/or filtration; (ii) the removal of oil in skimming tanks or any other effective device; (iii) the recirculation of cooling water and water from vacuum generation as much as possible","mg/Nm3","N/A",20,"Green","Discontinuous ",0,0,"Unspecified ","Qualified random sample or a 24 hour composite",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Other","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Electric arc furnace steelmaking and casting: Waste water from continous casting machines ","Water","Suspended solids","BAT is to minimise the waste water discharge from continuous casting by using the following techniques in combination: (i) the removal of solids by flocculation, sedimentation and/or filtration; (ii) the removal of oil in skimming tanks or any other effective device; (iii) the recirculation of cooling water and water from vacuum generation as much as possible","mg/Nm3","N/A",20,"Green","Discontinuous ",0,0,"Unspecified ","Qualified random sample or a 24 hour composite",0]
["Iron and steel","2. Production and processing of metals","Other","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Electric arc furnace steelmaking and casting: Waste water from continous casting machines ","Air","Chromium (VI) compounds (as Cr)","BAT is to minimise the waste water discharge from continuous casting by using the following techniques in combination: (i) the removal of solids by flocculation, sedimentation and/or filtration; (ii) the removal of oil in skimming tanks or any other effective device; (iii) the recirculation of cooling water and water from vacuum generation as much as possible","mg/Nm3","N/A",0.5,"Green","Discontinuous ",0,0,"Unspecified ","Qualified random sample or a 24 hour composite",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Other","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Electric arc furnace steelmaking and casting: Waste water from continous casting machines ","Air","Chromium (VI) compounds (as Cr)","BAT is to minimise the waste water discharge from continuous casting by using the following techniques in combination: (i) the removal of solids by flocculation, sedimentation and/or filtration; (ii) the removal of oil in skimming tanks or any other effective device; (iii) the recirculation of cooling water and water from vacuum generation as much as possible","mg/Nm3","N/A",0.5,"Green","Discontinuous ",0,0,"Unspecified ","Qualified random sample or a 24 hour composite",0]
["Iron and steel","2. Production and processing of metals","Other","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Electric arc furnace steelmaking and casting: Waste water from continous casting machines ","Air","Total hydrocarbons","BAT is to minimise the waste water discharge from continuous casting by using the following techniques in combination: (i) the removal of solids by flocculation, sedimentation and/or filtration; (ii) the removal of oil in skimming tanks or any other effective device; (iii) the recirculation of cooling water and water from vacuum generation as much as possible","mg/Nm3","N/A",5,"Green","Discontinuous ",0,0,"Unspecified ","Qualified random sample or a 24 hour composite",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Other","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Electric arc furnace steelmaking and casting: Waste water from continous casting machines ","Air","Total hydrocarbons","BAT is to minimise the waste water discharge from continuous casting by using the following techniques in combination: (i) the removal of solids by flocculation, sedimentation and/or filtration; (ii) the removal of oil in skimming tanks or any other effective device; (iii) the recirculation of cooling water and water from vacuum generation as much as possible","mg/Nm3","N/A",5,"Green","Discontinuous ",0,0,"Unspecified ","Qualified random sample or a 24 hour composite",0]
["Iron and steel","2. Production and processing of metals","Other","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Electric arc furnace steelmaking and casting: Waste water from continous casting machines ","Air","Zinc","BAT is to minimise the waste water discharge from continuous casting by using the following techniques in combination: (i) the removal of solids by flocculation, sedimentation and/or filtration; (ii) the removal of oil in skimming tanks or any other effective device; (iii) the recirculation of cooling water and water from vacuum generation as much as possible","mg/Nm3","N/A",2,"Green","Discontinuous ",0,0,"Unspecified ","Qualified random sample or a 24 hour composite",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Other","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Electric arc furnace steelmaking and casting: Waste water from continous casting machines ","Air","Zinc","BAT is to minimise the waste water discharge from continuous casting by using the following techniques in combination: (i) the removal of solids by flocculation, sedimentation and/or filtration; (ii) the removal of oil in skimming tanks or any other effective device; (iii) the recirculation of cooling water and water from vacuum generation as much as possible","mg/Nm3","N/A",2,"Green","Discontinuous ",0,0,"Unspecified ","Qualified random sample or a 24 hour composite",0]
["Iron and steel","2. Production and processing of metals","Coke Oven Plants","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Blast Furnaces: Pretreated waste water from the coking process and coke oven gas (COG)","Water","Ammonia (ecological receptor - Sensitive Lichens)","BAT for pretreated waste water from the coking process and coke oven gas (COG) cleaning is to use biological waste water treatment with integrated denitrification/nitrification stages.","mg/l","N/A",20,"Green","Discontinuous ",0,0,"Unspecified ",0,0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Coke Oven Plants","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Blast Furnaces: Pretreated waste water from the coking process and coke oven gas (COG)","Water","Ammonia (ecological receptor - Sensitive Lichens)","BAT for pretreated waste water from the coking process and coke oven gas (COG) cleaning is to use biological waste water treatment with integrated denitrification/nitrification stages.","mg/l","N/A",20,"Green","Discontinuous ",0,0,"Unspecified ",0,0]
["Iron and steel","2. Production and processing of metals","Coke Oven Plants","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Blast Furnaces: Pretreated waste water from the coking process and coke oven gas (COG)","Water","Ammonia (ecological receptor - Sensitive Lichens)","BAT for pretreated waste water from the coking process and coke oven gas (COG) cleaning is to use biological waste water treatment with integrated denitrification/nitrification stages.","mg/l","N/A",220,"Green","Discontinuous ",0,0,"Unspecified ",0,0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Coke Oven Plants","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Blast Furnaces: Pretreated waste water from the coking process and coke oven gas (COG)","Water","Ammonia (ecological receptor - Sensitive Lichens)","BAT for pretreated waste water from the coking process and coke oven gas (COG) cleaning is to use biological waste water treatment with integrated denitrification/nitrification stages.","mg/l","N/A",220,"Green","Discontinuous ",0,0,"Unspecified ",0,0]
["Iron and steel","2. Production and processing of metals","Pelletisation plans","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Water","Ammonia (ecological receptor - Sensitive Lichens)","BAT for pelletisation plants is to treat the effluent water prior to discharge by using a combination of the following techniques: (i) neutralisation; (ii) flocculation; (iii) sedimentation; (iv) sand filtration; (v) Heavy metal precipitation ","mg/l","N/A",160,"Green","Discontinuous ",0,0,"Unspecified ","Random sample of 24 hour composite sample ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Pelletisation plans","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Water","Ammonia (ecological receptor - Sensitive Lichens)","BAT for pelletisation plants is to treat the effluent water prior to discharge by using a combination of the following techniques: (i) neutralisation; (ii) flocculation; (iii) sedimentation; (iv) sand filtration; (v) Heavy metal precipitation ","mg/l","N/A",160,"Green","Discontinuous ",0,0,"Unspecified ","Random sample of 24 hour composite sample ",0]
["Iron and steel","2. Production and processing of metals","Sinter Plant","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Sinter strand","Water","Ammonia (ecological receptor - Sensitive Lichens)","BAT is to treat the effluent water from sinter plants where rinsing water is used or where a wet waste gas treatment system is applied, with the exception of cooling water prior to discharge by using a combination of the following techniques: (i) Heavy metal precipitation; (ii) neutralisation; (iii) sand filtration","mg/l","N/A",100,"Green","Discontinuous ",0,0,"Unspecified ","Random sample of 24 hour composite sample ","Sum of arsenic (As), cadmium (Cd), chromium (Cr), copper (Cu), mercury (Hg), nickel (Ni), lead (Pb), and zinc (Zn)",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Sinter Plant","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Sinter strand","Water","Ammonia (ecological receptor - Sensitive Lichens)","BAT is to treat the effluent water from sinter plants where rinsing water is used or where a wet waste gas treatment system is applied, with the exception of cooling water prior to discharge by using a combination of the following techniques: (i) Heavy metal precipitation; (ii) neutralisation; (iii) sand filtration","mg/l","N/A",100,"Green","Discontinuous ",0,0,"Unspecified ","Random sample of 24 hour composite sample ","Sum of arsenic (As), cadmium (Cd), chromium (Cr), copper (Cu), mercury (Hg), nickel (Ni), lead (Pb), and zinc (Zn)"]
["Iron and steel","2. Production and processing of metals","Coke Oven Plants","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Blast Furnaces: Pretreated waste water from the coking process and coke oven gas (COG)","Water","Ammonia (ecological receptor - Sensitive Lichens)","BAT for pretreated waste water from the coking process and coke oven gas (COG) cleaning is to use biological waste water treatment with integrated denitrification/nitrification stages.","mg/l","N/A",0.1,"Green","Discontinuous ",0,0,"Unspecified ","Random sample or a 24 hour composite sample ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Coke Oven Plants","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Blast Furnaces: Pretreated waste water from the coking process and coke oven gas (COG)","Water","Ammonia (ecological receptor - Sensitive Lichens)","BAT for pretreated waste water from the coking process and coke oven gas (COG) cleaning is to use biological waste water treatment with integrated denitrification/nitrification stages.","mg/l","N/A",0.1,"Green","Discontinuous ",0,0,"Unspecified ","Random sample or a 24 hour composite sample ",0]
["Iron and steel","2. Production and processing of metals","Other","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Blast Furnaces: Blast furnace gas ","Water","Ammonia (ecological receptor - Sensitive Lichens)","BAT for treating waste water from blast furnace gas treatment is to use flocculation (coagulation) and sedimentation and the reduction of easily released cyanide, if necessary.","mg/l","N/A",0.4,"Green","Discontinuous ",0,0,"Unspecified ","Random sample or a 24 hour composite sample ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Other","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Blast Furnaces: Blast furnace gas ","Water","Ammonia (ecological receptor - Sensitive Lichens)","BAT for treating waste water from blast furnace gas treatment is to use flocculation (coagulation) and sedimentation and the reduction of easily released cyanide, if necessary.","mg/l","N/A",0.4,"Green","Discontinuous ",0,0,"Unspecified ","Random sample or a 24 hour composite sample ",0]
["Iron and steel","2. Production and processing of metals","Coke Oven Plants","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Coal grinding plants ","Air","Particulates (PM10) (24 hr Mean)","BAT for coal grinding plants (coal preparation including crushing, grinding, pulverising and screening) is to prevent or reduce dust emissions by using one or a combination of the following techniques: (i) building and/or device enclosure (crusher, pulveriser, sieves); (ii) efficient extraction and use of a subsequent dry dedusting systems.","mg/Nm3",10,20,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Coke Oven Plants","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Coal grinding plants ","Air","Particulates (PM10) (24 hr Mean)","BAT for coal grinding plants (coal preparation including crushing, grinding, pulverising and screening) is to prevent or reduce dust emissions by using one or a combination of the following techniques: (i) building and/or device enclosure (crusher, pulveriser, sieves); (ii) efficient extraction and use of a subsequent dry dedusting systems.","mg/Nm3",10,20,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0]
["Iron and steel","2. Production and processing of metals","Sinter Plant","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Sinter strand","Water","Ammonia (ecological receptor - Sensitive Lichens)","BAT is to treat the effluent water from sinter plants where rinsing water is used or where a wet waste gas treatment system is applied, with the exception of cooling water prior to discharge by using a combination of the following techniques: (i) Heavy metal precipitation; (ii) neutralisation; (iii) sand filtration","mg/l","N/A",0.1,"Green","Discontinuous ",0,0,"Unspecified ","Random sample of 24 hour composite sample ","Sum of arsenic (As), cadmium (Cd), chromium (Cr), copper (Cu), mercury (Hg), nickel (Ni), lead (Pb), and zinc (Zn)",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Sinter Plant","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Sinter strand","Water","Ammonia (ecological receptor - Sensitive Lichens)","BAT is to treat the effluent water from sinter plants where rinsing water is used or where a wet waste gas treatment system is applied, with the exception of cooling water prior to discharge by using a combination of the following techniques: (i) Heavy metal precipitation; (ii) neutralisation; (iii) sand filtration","mg/l","N/A",0.1,"Green","Discontinuous ",0,0,"Unspecified ","Random sample of 24 hour composite sample ","Sum of arsenic (As), cadmium (Cd), chromium (Cr), copper (Cu), mercury (Hg), nickel (Ni), lead (Pb), and zinc (Zn)"]
["Iron and steel","2. Production and processing of metals","Pelletisation plans","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Water","Ammonia (ecological receptor - Sensitive Lichens)","BAT for pelletisation plants is to treat the effluent water prior to discharge by using a combination of the following techniques: (i) neutralisation; (ii) flocculation; (iii) sedimentation; (iv) sand filtration; (v) Heavy metal precipitation ","mg/l","N/A",0.55000000000000004,"Green","Discontinuous ",0,0,"Unspecified ","Random sample of 24 hour composite sample ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Pelletisation plans","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Water","Ammonia (ecological receptor - Sensitive Lichens)","BAT for pelletisation plants is to treat the effluent water prior to discharge by using a combination of the following techniques: (i) neutralisation; (ii) flocculation; (iii) sedimentation; (iv) sand filtration; (v) Heavy metal precipitation ","mg/l","N/A",0.55000000000000004,"Green","Discontinuous ",0,0,"Unspecified ","Random sample of 24 hour composite sample ",0]
["Iron and steel","2. Production and processing of metals","Other","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Blast Furnaces: Blast furnace gas ","Water","Ammonia (ecological receptor - Sensitive Lichens)","BAT for treating waste water from blast furnace gas treatment is to use flocculation (coagulation) and sedimentation and the reduction of easily released cyanide, if necessary.","mg/l","N/A",5,"Green","Discontinuous ",0,0,"Unspecified ","Random sample or a 24 hour composite sample ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Other","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Blast Furnaces: Blast furnace gas ","Water","Ammonia (ecological receptor - Sensitive Lichens)","BAT for treating waste water from blast furnace gas treatment is to use flocculation (coagulation) and sedimentation and the reduction of easily released cyanide, if necessary.","mg/l","N/A",5,"Green","Discontinuous ",0,0,"Unspecified ","Random sample or a 24 hour composite sample ",0]
["Iron and steel","2. Production and processing of metals","Pelletisation plans","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Water","Ammonia (ecological receptor - Sensitive Lichens)","BAT for pelletisation plants is to treat the effluent water prior to discharge by using a combination of the following techniques: (i) neutralisation; (ii) flocculation; (iii) sedimentation; (iv) sand filtration; (v) Heavy metal precipitation ","mg/l","N/A",45,"Green","Discontinuous ",0,0,"Unspecified ","Random sample of 24 hour composite sample ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Pelletisation plans","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Water","Ammonia (ecological receptor - Sensitive Lichens)","BAT for pelletisation plants is to treat the effluent water prior to discharge by using a combination of the following techniques: (i) neutralisation; (ii) flocculation; (iii) sedimentation; (iv) sand filtration; (v) Heavy metal precipitation ","mg/l","N/A",45,"Green","Discontinuous ",0,0,"Unspecified ","Random sample of 24 hour composite sample ",0]
["Iron and steel","2. Production and processing of metals","Other","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Blast Furnaces: Blast furnace gas ","Water","Ammonia (ecological receptor - Sensitive Lichens)","BAT for treating waste water from blast furnace gas treatment is to use flocculation (coagulation) and sedimentation and the reduction of easily released cyanide, if necessary.","mg/l","N/A",0.5,"Green","Discontinuous ",0,0,"Unspecified ","Random sample or a 24 hour composite sample ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Other","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Blast Furnaces: Blast furnace gas ","Water","Ammonia (ecological receptor - Sensitive Lichens)","BAT for treating waste water from blast furnace gas treatment is to use flocculation (coagulation) and sedimentation and the reduction of easily released cyanide, if necessary.","mg/l","N/A",0.5,"Green","Discontinuous ",0,0,"Unspecified ","Random sample or a 24 hour composite sample ",0]
["Iron and steel","2. Production and processing of metals","Coke Oven Plants","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Blast Furnaces: Pretreated waste water from the coking process and coke oven gas (COG)","Water","Ammonia (ecological receptor - Sensitive Lichens)","BAT for pretreated waste water from the coking process and coke oven gas (COG) cleaning is to use biological waste water treatment with integrated denitrification/nitrification stages.","mg/l","N/A",0.5,"Green","Discontinuous ",0,0,"Unspecified ","Random sample or a 24 hour composite sample ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Coke Oven Plants","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Blast Furnaces: Pretreated waste water from the coking process and coke oven gas (COG)","Water","Ammonia (ecological receptor - Sensitive Lichens)","BAT for pretreated waste water from the coking process and coke oven gas (COG) cleaning is to use biological waste water treatment with integrated denitrification/nitrification stages.","mg/l","N/A",0.5,"Green","Discontinuous ",0,0,"Unspecified ","Random sample or a 24 hour composite sample ",0]
["Iron and steel","2. Production and processing of metals","Coke Oven Plants","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Blast Furnaces: Pretreated waste water from the coking process and coke oven gas (COG)","Water","Ammonia (ecological receptor - Sensitive Lichens)","BAT for pretreated waste water from the coking process and coke oven gas (COG) cleaning is to use biological waste water treatment with integrated denitrification/nitrification stages.","mg/l","N/A",0.05,"Green","Discontinuous ",0,0,"Unspecified ","Random sample or a 24 hour composite sample ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Coke Oven Plants","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Blast Furnaces: Pretreated waste water from the coking process and coke oven gas (COG)","Water","Ammonia (ecological receptor - Sensitive Lichens)","BAT for pretreated waste water from the coking process and coke oven gas (COG) cleaning is to use biological waste water treatment with integrated denitrification/nitrification stages.","mg/l","N/A",0.05,"Green","Discontinuous ",0,0,"Unspecified ","Random sample or a 24 hour composite sample ",0]
["Iron and steel","2. Production and processing of metals","Coke Oven Plants","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Blast Furnaces: Pretreated waste water from the coking process and coke oven gas (COG)","Water","Ammonia (ecological receptor - Sensitive Lichens)","BAT for pretreated waste water from the coking process and coke oven gas (COG) cleaning is to use biological waste water treatment with integrated denitrification/nitrification stages.","mg/l","N/A",0.1,"Green","Discontinuous ",0,0,"Unspecified ",0,0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Coke Oven Plants","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Blast Furnaces: Pretreated waste water from the coking process and coke oven gas (COG)","Water","Ammonia (ecological receptor - Sensitive Lichens)","BAT for pretreated waste water from the coking process and coke oven gas (COG) cleaning is to use biological waste water treatment with integrated denitrification/nitrification stages.","mg/l","N/A",0.1,"Green","Discontinuous ",0,0,"Unspecified ",0,0]
["Iron and steel","2. Production and processing of metals","Coke Oven Plants","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Blast Furnaces: Pretreated waste water from the coking process and coke oven gas (COG)","Water","Ammonia (ecological receptor - Sensitive Lichens)","BAT for pretreated waste water from the coking process and coke oven gas (COG) cleaning is to use biological waste water treatment with integrated denitrification/nitrification stages.","mg/l",15,50,"Green","Discontinuous ",0,0,"Unspecified ","Random sample or a 24 hour composite sample ","Regarding the sum of ammonia-nitrogen (NH4 +-N), nitrate-nitrogen (NO3 - -N) and nitrite-nitrogen (NO2 - -N), values of < 35 mg/l are usually associated with the application of advanced biological waste water treatment plants with predenitrification/nitrification and post-denitrification.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Coke Oven Plants","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Blast Furnaces: Pretreated waste water from the coking process and coke oven gas (COG)","Water","Ammonia (ecological receptor - Sensitive Lichens)","BAT for pretreated waste water from the coking process and coke oven gas (COG) cleaning is to use biological waste water treatment with integrated denitrification/nitrification stages.","mg/l",15,50,"Green","Discontinuous ",0,0,"Unspecified ","Random sample or a 24 hour composite sample ","Regarding the sum of ammonia-nitrogen (NH4 +-N), nitrate-nitrogen (NO3 - -N) and nitrite-nitrogen (NO2 - -N), values of < 35 mg/l are usually associated with the application of advanced biological waste water treatment plants with predenitrification/nitrification and post-denitrification."]
["Iron and steel","2. Production and processing of metals","Other","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Blast Furnaces: Blast furnace gas ","Water","Ammonia (ecological receptor - Sensitive Lichens)","BAT for treating waste water from blast furnace gas treatment is to use flocculation (coagulation) and sedimentation and the reduction of easily released cyanide, if necessary.","mg/l","N/A",30,"Green","Discontinuous ",0,0,"Unspecified ","Random sample or a 24 hour composite sample ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Other","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Blast Furnaces: Blast furnace gas ","Water","Ammonia (ecological receptor - Sensitive Lichens)","BAT for treating waste water from blast furnace gas treatment is to use flocculation (coagulation) and sedimentation and the reduction of easily released cyanide, if necessary.","mg/l","N/A",30,"Green","Discontinuous ",0,0,"Unspecified ","Random sample or a 24 hour composite sample ",0]
["Iron and steel","2. Production and processing of metals","Pelletisation plans","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Water","Ammonia (ecological receptor - Sensitive Lichens)","BAT for pelletisation plants is to treat the effluent water prior to discharge by using a combination of the following techniques: (i) neutralisation; (ii) flocculation; (iii) sedimentation; (iv) sand filtration; (v) Heavy metal precipitation ","mg/l","N/A",50,"Green","Discontinuous ",0,0,"Unspecified ","Random sample of 24 hour composite sample ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Pelletisation plans","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Water","Ammonia (ecological receptor - Sensitive Lichens)","BAT for pelletisation plants is to treat the effluent water prior to discharge by using a combination of the following techniques: (i) neutralisation; (ii) flocculation; (iii) sedimentation; (iv) sand filtration; (v) Heavy metal precipitation ","mg/l","N/A",50,"Green","Discontinuous ",0,0,"Unspecified ","Random sample of 24 hour composite sample ",0]
["Iron and steel","2. Production and processing of metals","Sinter Plant","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Sinter strand","Water","Ammonia (ecological receptor - Sensitive Lichens)","BAT is to treat the effluent water from sinter plants where rinsing water is used or where a wet waste gas treatment system is applied, with the exception of cooling water prior to discharge by using a combination of the following techniques: (i) Heavy metal precipitation; (ii) neutralisation; (iii) sand filtration","mg/l","N/A",30,"Green","Discontinuous ","Unspecified ","Unspecified ","Unspecified ","Random sample of 24 hour composite sample ","Sum of arsenic (As), cadmium (Cd), chromium (Cr), copper (Cu), mercury (Hg), nickel (Ni), lead (Pb), and zinc (Zn)",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Sinter Plant","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Sinter strand","Water","Ammonia (ecological receptor - Sensitive Lichens)","BAT is to treat the effluent water from sinter plants where rinsing water is used or where a wet waste gas treatment system is applied, with the exception of cooling water prior to discharge by using a combination of the following techniques: (i) Heavy metal precipitation; (ii) neutralisation; (iii) sand filtration","mg/l","N/A",30,"Green","Discontinuous ","Unspecified ","Unspecified ","Unspecified ","Random sample of 24 hour composite sample ","Sum of arsenic (As), cadmium (Cd), chromium (Cr), copper (Cu), mercury (Hg), nickel (Ni), lead (Pb), and zinc (Zn)"]
["Iron and steel","2. Production and processing of metals","Coke Oven Plants","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Blast Furnaces: Pretreated waste water from the coking process and coke oven gas (COG)","Water","Ammonia (ecological receptor - Sensitive Lichens)","BAT for pretreated waste water from the coking process and coke oven gas (COG) cleaning is to use biological waste water treatment with integrated denitrification/nitrification stages.","mg/l","N/A",4,"Green","Discontinuous ",0,0,"Unspecified ","Random sample or a 24 hour composite sample ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Coke Oven Plants","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Blast Furnaces: Pretreated waste water from the coking process and coke oven gas (COG)","Water","Ammonia (ecological receptor - Sensitive Lichens)","BAT for pretreated waste water from the coking process and coke oven gas (COG) cleaning is to use biological waste water treatment with integrated denitrification/nitrification stages.","mg/l","N/A",4,"Green","Discontinuous ",0,0,"Unspecified ","Random sample or a 24 hour composite sample ",0]
["Iron and steel","2. Production and processing of metals","Other","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Blast Furnaces: Blast furnace gas ","Water","Ammonia (ecological receptor - Sensitive Lichens)","BAT for treating waste water from blast furnace gas treatment is to use flocculation (coagulation) and sedimentation and the reduction of easily released cyanide, if necessary.","mg/l","N/A",2,"Green","Discontinuous ",0,0,"Unspecified ","Random sample or a 24 hour composite sample ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Other","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Blast Furnaces: Blast furnace gas ","Water","Ammonia (ecological receptor - Sensitive Lichens)","BAT for treating waste water from blast furnace gas treatment is to use flocculation (coagulation) and sedimentation and the reduction of easily released cyanide, if necessary.","mg/l","N/A",2,"Green","Discontinuous ",0,0,"Unspecified ","Random sample or a 24 hour composite sample ",0]
["LCP","1. Energy industries","Unspecified","Unspecified","Unspecified","Unspecified","Co-incineration of waste with coal and/or lignite","< 300 MWth ","Unspecified","Air","Cadmium and its compounds (as Cd)","In order to reduce dust and particulate-bound metal emissions to air from the co-incineration of waste with coal and/or lignite, BAT is to use one or a combination of the techniques given in BAT 22.","ug/Nm3",5,"12","Green","Once every 6 months",0,0,0.06,"Average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Unspecified","Unspecified","Co-incineration of waste with coal and/or lignite","< 300 MWth ","Unspecified","Air","Cadmium and its compounds (as Cd)","In order to reduce dust and particulate-bound metal emissions to air from the co-incineration of waste with coal and/or lignite, BAT is to use one or a combination of the techniques given in BAT 22.","ug/Nm3",5,"12","Green","Once every 6 months",0,0,0.06,"Average over the sampling period",0]
["LCP","1. Energy industries","Unspecified","Unspecified","Unspecified","Unspecified","Co-incineration of waste with coal and/or lignite","≥ 300 MWth","Unspecified","Air","Cadmium and its compounds (as Cd)","In order to reduce dust and particulate-bound metal emissions to air from the co-incineration of waste with coal and/or lignite, BAT is to use one or a combination of the techniques given in BAT 22.","ug/Nm3",5,"6","Green","Once every 3 months ",0,0,0.06,"Average of samples obtained during one year",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Unspecified","Unspecified","Co-incineration of waste with coal and/or lignite","≥ 300 MWth","Unspecified","Air","Cadmium and its compounds (as Cd)","In order to reduce dust and particulate-bound metal emissions to air from the co-incineration of waste with coal and/or lignite, BAT is to use one or a combination of the techniques given in BAT 22.","ug/Nm3",5,"6","Green","Once every 3 months ",0,0,0.06,"Average of samples obtained during one year",0]
["LCP","1. Energy industries","Unspecified","Unspecified","Unspecified","Unspecified","Co-incineration of waste with biomass and/or peat","Unspecified ","Unspecified","Air","Cadmium and its compounds (as Cd)","In order to reduce dust and particulate-bound metal emissions to air from the co-incineration of waste with biomass and/or peat, BAT is to use one or a combination of the techniques given in BAT 26.","ug/Nm3","N/A","5","Amber",0,0,0,0.06,"Average of samples obtained during one year",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Unspecified","Unspecified","Co-incineration of waste with biomass and/or peat","Unspecified ","Unspecified","Air","Cadmium and its compounds (as Cd)","In order to reduce dust and particulate-bound metal emissions to air from the co-incineration of waste with biomass and/or peat, BAT is to use one or a combination of the techniques given in BAT 26.","ug/Nm3","N/A","5","Amber",0,0,0,0.06,"Average of samples obtained during one year",0]
["LCP","1. Energy industries","Unspecified","Unspecified","All","Plants operated ≥ 1 500 h/yr or for Newcombustion plants","Coal and/or lignite ","≥ 300 MWth","Unspecified","Air","Carbon monoxide",0,"mg/Nm3",30,"140","Amber","Continuous ",0,0,0.06,"Yearly ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","Plants operated ≥ 1 500 h/yr or for Newcombustion plants","Coal and/or lignite ","≥ 300 MWth","Unspecified","Air","Carbon monoxide",0,"mg/Nm3",30,"140","Amber","Continuous ",0,0,0.06,"Yearly ",0]
["LCP","1. Energy industries","Unspecified","Unspecified","Coal-fired PC boiler","Plants operated ≥ 1 500 h/yr or for Newcombustion plants","Coal and/or lignite ","≥ 300 MWth","Unspecified","Air","Carbon monoxide",0,"mg/Nm3",5,"100","Amber","Continuous ",0,0,0.06,"Yearly ","The higher end of the range may be up to 140 mg/Nm3 in the case of limitations due to boiler design, and/or in the case of fluidised bed boilers not fitted with secondary abatement techniques for NOX emissions reduction.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Coal-fired PC boiler","Plants operated ≥ 1 500 h/yr or for Newcombustion plants","Coal and/or lignite ","≥ 300 MWth","Unspecified","Air","Carbon monoxide",0,"mg/Nm3",5,"100","Amber","Continuous ",0,0,0.06,"Yearly ","The higher end of the range may be up to 140 mg/Nm3 in the case of limitations due to boiler design, and/or in the case of fluidised bed boilers not fitted with secondary abatement techniques for NOX emissions reduction."]
["LCP","1. Energy industries","Unspecified","Unspecified","FBC boiler combusting coal and/or lignite and lignite-fired PC boiler","Plants operated ≥ 1 500 h/yr or for Newcombustion plants","Coal and/or lignite ","≥ 300 MWth","Unspecified","Air","Carbon monoxide",0,"mg/Nm3",30,"100","Amber","Continuous ",0,0,0.06,"Yearly ","The higher end of the range may be up to 140 mg/Nm3 in the case of limitations due to boiler design, and/or in the case of fluidised bed boilers not fitted with secondary abatement techniques for NOX emissions reduction.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","FBC boiler combusting coal and/or lignite and lignite-fired PC boiler","Plants operated ≥ 1 500 h/yr or for Newcombustion plants","Coal and/or lignite ","≥ 300 MWth","Unspecified","Air","Carbon monoxide",0,"mg/Nm3",30,"100","Amber","Continuous ",0,0,0.06,"Yearly ","The higher end of the range may be up to 140 mg/Nm3 in the case of limitations due to boiler design, and/or in the case of fluidised bed boilers not fitted with secondary abatement techniques for NOX emissions reduction."]
["LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Coal and/or lignite ","<100 MWth","Unspecified","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below.; (ii) Bag filter; (iii) Boiler sorbent injection (in-furnace or in- bed); (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",2,18,"Green","Continuous ",0,0,0.06,"Yearly","These BAT-AELs do not apply to plants operated < 1 500 h/yr.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Coal and/or lignite ","<100 MWth","Unspecified","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below.; (ii) Bag filter; (iii) Boiler sorbent injection (in-furnace or in- bed); (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",2,18,"Green","Continuous ",0,0,0.06,"Yearly","These BAT-AELs do not apply to plants operated < 1 500 h/yr."]
["LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Coal and/or lignite ","<100 MWth","Unspecified","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below.; (ii) Bag filter; (iii) Boiler sorbent injection (in-furnace or in- bed); (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",4,22,"Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ","For plants operated < 500 h/yr, these levels are indicative.\n\nThe higher end of the BAT-AEL range is 28 mg/Nm3 for plants put into operation no later than 7 January 2014.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Coal and/or lignite ","<100 MWth","Unspecified","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below.; (ii) Bag filter; (iii) Boiler sorbent injection (in-furnace or in- bed); (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",4,22,"Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ","For plants operated < 500 h/yr, these levels are indicative.\n\nThe higher end of the BAT-AEL range is 28 mg/Nm3 for plants put into operation no later than 7 January 2014."]
["LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Coal and/or lignite ","≥ 1 000 MWth","Unspecified","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below.; (ii) Bag filter; (iii) Boiler sorbent injection (in-furnace or in- bed); (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",2,8,"Green","Continuous ",0,0,0.06,"Yearly",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Coal and/or lignite ","≥ 1 000 MWth","Unspecified","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below.; (ii) Bag filter; (iii) Boiler sorbent injection (in-furnace or in- bed); (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",2,8,"Green","Continuous ",0,0,0.06,"Yearly",0]
["LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Coal and/or lignite ","≥ 1 000 MWth","Unspecified","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below.; (ii) Bag filter; (iii) Boiler sorbent injection (in-furnace or in- bed); (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",3,11,"Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ","The higher end of the BAT-AEL range is 14 mg/Nm3 for plants put into operation no later than 7 January 2014.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Coal and/or lignite ","≥ 1 000 MWth","Unspecified","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below.; (ii) Bag filter; (iii) Boiler sorbent injection (in-furnace or in- bed); (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",3,11,"Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ","The higher end of the BAT-AEL range is 14 mg/Nm3 for plants put into operation no later than 7 January 2014."]
["LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Coal and/or lignite ","100-300 MWth","Unspecified","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below.; (ii) Bag filter; (iii) Boiler sorbent injection (in-furnace or in- bed); (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",2,14,"Green","Continuous ",0,0,0.06,"Yearly",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Coal and/or lignite ","100-300 MWth","Unspecified","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below.; (ii) Bag filter; (iii) Boiler sorbent injection (in-furnace or in- bed); (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",2,14,"Green","Continuous ",0,0,0.06,"Yearly",0]
["LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Coal and/or lignite ","100-300 MWth","Unspecified","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below.; (ii) Bag filter; (iii) Boiler sorbent injection (in-furnace or in- bed); (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",4,22,"Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ","The higher end of the BAT-AEL range is 25 mg/Nm3 for plants put into operation no later than 7 January 2014.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Coal and/or lignite ","100-300 MWth","Unspecified","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below.; (ii) Bag filter; (iii) Boiler sorbent injection (in-furnace or in- bed); (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",4,22,"Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ","The higher end of the BAT-AEL range is 25 mg/Nm3 for plants put into operation no later than 7 January 2014."]
["LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Coal and/or lignite ","300-1000 MWth","Unspecified","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below.; (ii) Bag filter; (iii) Boiler sorbent injection (in-furnace or in- bed); (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",2,10,"Green","Continuous ",0,0,0.06,"Yearly","The higher end of the BAT-AEL range is 12 mg/Nm3 for plants put into operation no later than 7 January 2014.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Coal and/or lignite ","300-1000 MWth","Unspecified","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below.; (ii) Bag filter; (iii) Boiler sorbent injection (in-furnace or in- bed); (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",2,10,"Green","Continuous ",0,0,0.06,"Yearly","The higher end of the BAT-AEL range is 12 mg/Nm3 for plants put into operation no later than 7 January 2014."]
["LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Coal and/or lignite ","300-1000 MWth","Unspecified","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below.; (ii) Bag filter; (iii) Boiler sorbent injection (in-furnace or in- bed); (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",3,11,"Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ","The higher end of the BAT-AEL range is 20 mg/Nm3 for plants put into operation no later than 7 January 2014.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Coal and/or lignite ","300-1000 MWth","Unspecified","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below.; (ii) Bag filter; (iii) Boiler sorbent injection (in-furnace or in- bed); (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",3,11,"Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ","The higher end of the BAT-AEL range is 20 mg/Nm3 for plants put into operation no later than 7 January 2014."]
["LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Solid biomass and/or peat","< 100 MWth","Unspecified","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Dry or semi-dry FGD system; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Fuel choice","mg/Nm3",2,"15","Green","Continuous ",0,0,0.06,"Yearly","These BAT-AELs do not apply to plants operated < 1 500 h/yr.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Solid biomass and/or peat","< 100 MWth","Unspecified","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Dry or semi-dry FGD system; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Fuel choice","mg/Nm3",2,"15","Green","Continuous ",0,0,0.06,"Yearly","These BAT-AELs do not apply to plants operated < 1 500 h/yr."]
["LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Solid biomass and/or peat","< 100 MWth","Unspecified","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Dry or semi-dry FGD system; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Fuel choice","mg/Nm3",2,"22","Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ","For plants operated < 500 h/yr, these levels are indicative.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Solid biomass and/or peat","< 100 MWth","Unspecified","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Dry or semi-dry FGD system; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Fuel choice","mg/Nm3",2,"22","Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ","For plants operated < 500 h/yr, these levels are indicative."]
["LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Solid biomass and/or peat","≥ 300 MWth","Unspecified","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Dry or semi-dry FGD system; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Fuel choice","mg/Nm3",2,"10","Green","Continuous ",0,0,0.06,"Yearly","These BAT-AELs do not apply to plants operated < 1 500 h/yr.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Solid biomass and/or peat","≥ 300 MWth","Unspecified","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Dry or semi-dry FGD system; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Fuel choice","mg/Nm3",2,"10","Green","Continuous ",0,0,0.06,"Yearly","These BAT-AELs do not apply to plants operated < 1 500 h/yr."]
["LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Solid biomass and/or peat","≥ 300 MWth","Unspecified","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Dry or semi-dry FGD system; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Fuel choice","mg/Nm3",2,"16","Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ","For plants operated < 500 h/yr, these levels are indicative.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Solid biomass and/or peat","≥ 300 MWth","Unspecified","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Dry or semi-dry FGD system; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Fuel choice","mg/Nm3",2,"16","Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ","For plants operated < 500 h/yr, these levels are indicative."]
["LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Solid biomass and/or peat","100-300 MWth","Unspecified","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Dry or semi-dry FGD system; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Fuel choice","mg/Nm3",2,"12","Green","Continuous ",0,0,0.06,"Yearly","These BAT-AELs do not apply to plants operated < 1 500 h/yr.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Solid biomass and/or peat","100-300 MWth","Unspecified","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Dry or semi-dry FGD system; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Fuel choice","mg/Nm3",2,"12","Green","Continuous ",0,0,0.06,"Yearly","These BAT-AELs do not apply to plants operated < 1 500 h/yr."]
["LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Solid biomass and/or peat","100-300 MWth","Unspecified","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Dry or semi-dry FGD system; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Fuel choice","mg/Nm3",2,"18","Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ","For plants operated < 500 h/yr, these levels are indicative.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Solid biomass and/or peat","100-300 MWth","Unspecified","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Dry or semi-dry FGD system; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Fuel choice","mg/Nm3",2,"18","Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ","For plants operated < 500 h/yr, these levels are indicative."]
["LCP","1. Energy industries","Unspecified","Unspecified","All","New","Coal and/or lignite ","<100 MWth","Unspecified","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below.; (ii) Bag filter; (iii) Boiler sorbent injection (in-furnace or in- bed); (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",2,5,"Green","Continuous ",0,0,0.06,"Yearly",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","New","Coal and/or lignite ","<100 MWth","Unspecified","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below.; (ii) Bag filter; (iii) Boiler sorbent injection (in-furnace or in- bed); (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",2,5,"Green","Continuous ",0,0,0.06,"Yearly",0]
["LCP","1. Energy industries","Unspecified","Unspecified","All","New","Coal and/or lignite ","<100 MWth","Unspecified","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below.; (ii) Bag filter; (iii) Boiler sorbent injection (in-furnace or in- bed); (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",4,16,"Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","New","Coal and/or lignite ","<100 MWth","Unspecified","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below.; (ii) Bag filter; (iii) Boiler sorbent injection (in-furnace or in- bed); (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",4,16,"Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ",0]
["LCP","1. Energy industries","Unspecified","Unspecified","All","New","Coal and/or lignite ","≥ 1 000 MWth","Unspecified","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below.; (ii) Bag filter; (iii) Boiler sorbent injection (in-furnace or in- bed); (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",2,5,"Green","Continuous ",0,0,0.06,"Yearly",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","New","Coal and/or lignite ","≥ 1 000 MWth","Unspecified","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below.; (ii) Bag filter; (iii) Boiler sorbent injection (in-furnace or in- bed); (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",2,5,"Green","Continuous ",0,0,0.06,"Yearly",0]
["LCP","1. Energy industries","Unspecified","Unspecified","All","New","Coal and/or lignite ","≥ 1 000 MWth","Unspecified","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below.; (ii) Bag filter; (iii) Boiler sorbent injection (in-furnace or in- bed); (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",3,10,"Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","New","Coal and/or lignite ","≥ 1 000 MWth","Unspecified","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below.; (ii) Bag filter; (iii) Boiler sorbent injection (in-furnace or in- bed); (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",3,10,"Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ",0]
["LCP","1. Energy industries","Unspecified","Unspecified","All","New","Coal and/or lignite ","100-300 MWth","Unspecified","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below.; (ii) Bag filter; (iii) Boiler sorbent injection (in-furnace or in- bed); (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",2,5,"Green","Continuous ",0,0,0.06,"Yearly",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","New","Coal and/or lignite ","100-300 MWth","Unspecified","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below.; (ii) Bag filter; (iii) Boiler sorbent injection (in-furnace or in- bed); (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",2,5,"Green","Continuous ",0,0,0.06,"Yearly",0]
["LCP","1. Energy industries","Unspecified","Unspecified","All","New","Coal and/or lignite ","100-300 MWth","Unspecified","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below.; (ii) Bag filter; (iii) Boiler sorbent injection (in-furnace or in- bed); (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",3,15,"Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","New","Coal and/or lignite ","100-300 MWth","Unspecified","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below.; (ii) Bag filter; (iii) Boiler sorbent injection (in-furnace or in- bed); (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",3,15,"Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ",0]
["LCP","1. Energy industries","Unspecified","Unspecified","All","New","Coal and/or lignite ","300-1000 MWth","Unspecified","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below.; (ii) Bag filter; (iii) Boiler sorbent injection (in-furnace or in- bed); (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",2,5,"Green","Continuous ",0,0,0.06,"Yearly",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","New","Coal and/or lignite ","300-1000 MWth","Unspecified","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below.; (ii) Bag filter; (iii) Boiler sorbent injection (in-furnace or in- bed); (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",2,5,"Green","Continuous ",0,0,0.06,"Yearly",0]
["LCP","1. Energy industries","Unspecified","Unspecified","All","New","Coal and/or lignite ","300-1000 MWth","Unspecified","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below.; (ii) Bag filter; (iii) Boiler sorbent injection (in-furnace or in- bed); (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",3,10,"Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","New","Coal and/or lignite ","300-1000 MWth","Unspecified","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below.; (ii) Bag filter; (iii) Boiler sorbent injection (in-furnace or in- bed); (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",3,10,"Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ",0]
["LCP","1. Energy industries","Unspecified","Unspecified","All","New","Solid biomass and/or peat","< 100 MWth","Unspecified","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Dry or semi-dry FGD system; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Fuel choice","mg/Nm3",2,"5","Green","Continuous ",0,0,0.06,"Yearly ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","New","Solid biomass and/or peat","< 100 MWth","Unspecified","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Dry or semi-dry FGD system; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Fuel choice","mg/Nm3",2,"5","Green","Continuous ",0,0,0.06,"Yearly ",0]
["LCP","1. Energy industries","Unspecified","Unspecified","All","New","Solid biomass and/or peat","< 100 MWth","Unspecified","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Dry or semi-dry FGD system; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Fuel choice","mg/Nm3",2,"10","Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","New","Solid biomass and/or peat","< 100 MWth","Unspecified","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Dry or semi-dry FGD system; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Fuel choice","mg/Nm3",2,"10","Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ",0]
["LCP","1. Energy industries","Unspecified","Unspecified","All","New","Solid biomass and/or peat","≥ 300 MWth","Unspecified","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Dry or semi-dry FGD system; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Fuel choice","mg/Nm3",2,"5","Green","Continuous ",0,0,0.06,"Yearly ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","New","Solid biomass and/or peat","≥ 300 MWth","Unspecified","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Dry or semi-dry FGD system; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Fuel choice","mg/Nm3",2,"5","Green","Continuous ",0,0,0.06,"Yearly ",0]
["LCP","1. Energy industries","Unspecified","Unspecified","All","New","Solid biomass and/or peat","≥ 300 MWth","Unspecified","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Dry or semi-dry FGD system; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Fuel choice","mg/Nm3",2,"10","Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","New","Solid biomass and/or peat","≥ 300 MWth","Unspecified","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Dry or semi-dry FGD system; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Fuel choice","mg/Nm3",2,"10","Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ",0]
["LCP","1. Energy industries","Unspecified","Unspecified","All","New","Solid biomass and/or peat","100-300 MWth","Unspecified","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Dry or semi-dry FGD system; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Fuel choice","mg/Nm3",2,"5","Green","Continuous ",0,0,0.06,"Yearly ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","New","Solid biomass and/or peat","100-300 MWth","Unspecified","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Dry or semi-dry FGD system; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Fuel choice","mg/Nm3",2,"5","Green","Continuous ",0,0,0.06,"Yearly ",0]
["LCP","1. Energy industries","Unspecified","Unspecified","All","New","Solid biomass and/or peat","100-300 MWth","Unspecified","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Dry or semi-dry FGD system; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Fuel choice","mg/Nm3",2,"10","Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","New","Solid biomass and/or peat","100-300 MWth","Unspecified","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Dry or semi-dry FGD system; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Fuel choice","mg/Nm3",2,"10","Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ",0]
["LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Unspecified","100% iron and steel process gases ","Unspecified ","Unspecified","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust emissions to air from the combustion of iron and steel process gases, BAT is to use one or a combination of the techniques given below: (i) Fuel choice/management; (ii) Blast furnace gas pretreatment at the iron- and steel-works; (iii) Basic oxygen furnace gas pretreatment at the iron- and steel- works; (iv) Electrostatic precipitator (ESP); (v) Bag filter","mg/Nm3",2,"7","Green","Continuous ",0,0,0.03,"Yearly","For existing plants operated < 1 500 h/yr, these BAT-AELs do not apply.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Unspecified","100% iron and steel process gases ","Unspecified ","Unspecified","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust emissions to air from the combustion of iron and steel process gases, BAT is to use one or a combination of the techniques given below: (i) Fuel choice/management; (ii) Blast furnace gas pretreatment at the iron- and steel-works; (iii) Basic oxygen furnace gas pretreatment at the iron- and steel- works; (iv) Electrostatic precipitator (ESP); (v) Bag filter","mg/Nm3",2,"7","Green","Continuous ",0,0,0.03,"Yearly","For existing plants operated < 1 500 h/yr, these BAT-AELs do not apply."]
["LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Unspecified","100% iron and steel process gases ","Unspecified ","Unspecified","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust emissions to air from the combustion of iron and steel process gases, BAT is to use one or a combination of the techniques given below: (i) Fuel choice/management; (ii) Blast furnace gas pretreatment at the iron- and steel-works; (iii) Basic oxygen furnace gas pretreatment at the iron- and steel- works; (iv) Electrostatic precipitator (ESP); (v) Bag filter","mg/Nm3",2,"10","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ","For existing plants operated < 500 h/yr, these levels are indicative",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Unspecified","100% iron and steel process gases ","Unspecified ","Unspecified","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust emissions to air from the combustion of iron and steel process gases, BAT is to use one or a combination of the techniques given below: (i) Fuel choice/management; (ii) Blast furnace gas pretreatment at the iron- and steel-works; (iii) Basic oxygen furnace gas pretreatment at the iron- and steel- works; (iv) Electrostatic precipitator (ESP); (v) Bag filter","mg/Nm3",2,"10","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ","For existing plants operated < 500 h/yr, these levels are indicative"]
["LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Existing","100 % process fuels from the chemical industry in boilers","< 300 MWth ","Unspecified","Air","Particulates (PM10) (Annual Mean)","In order to reduce emissions to air of dust, particulate-bound metals, and trace species from the combustion of process fuels from the chemical industry in boilers, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Fuel choice; (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",2,"15","Green","Continuous ",0,0,0.03,"Yearly","For plants operated < 1 500 h/yr, these BAT-AELs do not apply.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Existing","100 % process fuels from the chemical industry in boilers","< 300 MWth ","Unspecified","Air","Particulates (PM10) (Annual Mean)","In order to reduce emissions to air of dust, particulate-bound metals, and trace species from the combustion of process fuels from the chemical industry in boilers, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Fuel choice; (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",2,"15","Green","Continuous ",0,0,0.03,"Yearly","For plants operated < 1 500 h/yr, these BAT-AELs do not apply."]
["LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Existing","100 % process fuels from the chemical industry in boilers","< 300 MWth ","Unspecified","Air","Particulates (PM10) (24 hr Mean)","In order to reduce emissions to air of dust, particulate-bound metals, and trace species from the combustion of process fuels from the chemical industry in boilers, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Fuel choice; (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",2,"22","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ","For plants operated < 500 h/yr, these levels are indicative.\n\nFor plants operated < 500 h/yr, these levels are indicative.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Existing","100 % process fuels from the chemical industry in boilers","< 300 MWth ","Unspecified","Air","Particulates (PM10) (24 hr Mean)","In order to reduce emissions to air of dust, particulate-bound metals, and trace species from the combustion of process fuels from the chemical industry in boilers, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Fuel choice; (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",2,"22","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ","For plants operated < 500 h/yr, these levels are indicative.\n\nFor plants operated < 500 h/yr, these levels are indicative."]
["LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Existing","100 % process fuels from the chemical industry in boilers","≥ 300 MWth","Unspecified","Air","Particulates (PM10) (Annual Mean)","In order to reduce emissions to air of dust, particulate-bound metals, and trace species from the combustion of process fuels from the chemical industry in boilers, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Fuel choice; (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",2,"10","Green","Continuous ",0,0,0.03,"Yearly","For plants operated < 1 500 h/yr, these BAT-AELs do not apply.\n\nFor plants put into operation no later than 7 January 2014, the higher end of the BAT-AEL range is 15 mg/Nm3.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Existing","100 % process fuels from the chemical industry in boilers","≥ 300 MWth","Unspecified","Air","Particulates (PM10) (Annual Mean)","In order to reduce emissions to air of dust, particulate-bound metals, and trace species from the combustion of process fuels from the chemical industry in boilers, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Fuel choice; (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",2,"10","Green","Continuous ",0,0,0.03,"Yearly","For plants operated < 1 500 h/yr, these BAT-AELs do not apply.\n\nFor plants put into operation no later than 7 January 2014, the higher end of the BAT-AEL range is 15 mg/Nm3."]
["LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Existing","100 % process fuels from the chemical industry in boilers","≥ 300 MWth","Unspecified","Air","Particulates (PM10) (24 hr Mean)","In order to reduce emissions to air of dust, particulate-bound metals, and trace species from the combustion of process fuels from the chemical industry in boilers, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Fuel choice; (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",2,"11","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ","For plants operated < 500 h/yr, these levels are indicative.\n\nFor plants put into operation no later than 7 January 2014, the higher end of the BAT-AEL range is 25 mg/Nm3.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Existing","100 % process fuels from the chemical industry in boilers","≥ 300 MWth","Unspecified","Air","Particulates (PM10) (24 hr Mean)","In order to reduce emissions to air of dust, particulate-bound metals, and trace species from the combustion of process fuels from the chemical industry in boilers, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Fuel choice; (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",2,"11","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ","For plants operated < 500 h/yr, these levels are indicative.\n\nFor plants put into operation no later than 7 January 2014, the higher end of the BAT-AEL range is 25 mg/Nm3."]
["LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Existing","HFO and/or gas oil in boilers","< 300 MWth ","Unspecified","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Multicyclones; (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD); (vi) Fuel choice","mg/Nm3",2,"20","Green","Continuous ",0,0,0.03,"Yearly","These BAT-AELs do not apply to plants operated < 1 500 h/yr.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Existing","HFO and/or gas oil in boilers","< 300 MWth ","Unspecified","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Multicyclones; (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD); (vi) Fuel choice","mg/Nm3",2,"20","Green","Continuous ",0,0,0.03,"Yearly","These BAT-AELs do not apply to plants operated < 1 500 h/yr."]
["LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Existing","HFO and/or gas oil in boilers","< 300 MWth ","Unspecified","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Multicyclones; (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD); (vi) Fuel choice","mg/Nm3",7,"22","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ","For plants operated < 500 h/yr, these levels are indicative.\n\nThe higher end of the BAT-AEL range is 25 mg/Nm3 for plants put into operation no later than 7 January 2014.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Existing","HFO and/or gas oil in boilers","< 300 MWth ","Unspecified","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Multicyclones; (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD); (vi) Fuel choice","mg/Nm3",7,"22","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ","For plants operated < 500 h/yr, these levels are indicative.\n\nThe higher end of the BAT-AEL range is 25 mg/Nm3 for plants put into operation no later than 7 January 2014."]
["LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Existing","HFO and/or gas oil in boilers","≥ 300 MWth","Unspecified","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Multicyclones; (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD); (vi) Fuel choice","mg/Nm3",2,"10","Green","Continuous ",0,0,0.03,"Yearly","These BAT-AELs do not apply to plants operated < 1 500 h/yr.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Existing","HFO and/or gas oil in boilers","≥ 300 MWth","Unspecified","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Multicyclones; (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD); (vi) Fuel choice","mg/Nm3",2,"10","Green","Continuous ",0,0,0.03,"Yearly","These BAT-AELs do not apply to plants operated < 1 500 h/yr."]
["LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Existing","HFO and/or gas oil in boilers","≥ 300 MWth","Unspecified","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Multicyclones; (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD); (vi) Fuel choice","mg/Nm3",7,"11","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ","For plants operated < 500 h/yr, these levels are indicative.\n\nThe higher end of the BAT-AEL range is 15 mg/Nm3 for plants put into operation no later than 7 January 2014.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Existing","HFO and/or gas oil in boilers","≥ 300 MWth","Unspecified","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Multicyclones; (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD); (vi) Fuel choice","mg/Nm3",7,"11","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ","For plants operated < 500 h/yr, these levels are indicative.\n\nThe higher end of the BAT-AEL range is 15 mg/Nm3 for plants put into operation no later than 7 January 2014."]
["LCP","1. Energy industries","Unspecified","Unspecified","Boilers","New","100 % process fuels from the chemical industry in boilers","< 300 MWth ","Unspecified","Air","Particulates (PM10) (Annual Mean)","In order to reduce emissions to air of dust, particulate-bound metals, and trace species from the combustion of process fuels from the chemical industry in boilers, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Fuel choice; (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",2,"5","Green","Continuous ",0,0,0.03,"Yearly",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","New","100 % process fuels from the chemical industry in boilers","< 300 MWth ","Unspecified","Air","Particulates (PM10) (Annual Mean)","In order to reduce emissions to air of dust, particulate-bound metals, and trace species from the combustion of process fuels from the chemical industry in boilers, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Fuel choice; (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",2,"5","Green","Continuous ",0,0,0.03,"Yearly",0]
["LCP","1. Energy industries","Unspecified","Unspecified","Boilers","New","100 % process fuels from the chemical industry in boilers","< 300 MWth ","Unspecified","Air","Particulates (PM10) (24 hr Mean)","In order to reduce emissions to air of dust, particulate-bound metals, and trace species from the combustion of process fuels from the chemical industry in boilers, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Fuel choice; (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",2,"10","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","New","100 % process fuels from the chemical industry in boilers","< 300 MWth ","Unspecified","Air","Particulates (PM10) (24 hr Mean)","In order to reduce emissions to air of dust, particulate-bound metals, and trace species from the combustion of process fuels from the chemical industry in boilers, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Fuel choice; (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",2,"10","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ",0]
["LCP","1. Energy industries","Unspecified","Unspecified","Boilers","New","100 % process fuels from the chemical industry in boilers","≥ 300 MWth","Unspecified","Air","Particulates (PM10) (Annual Mean)","In order to reduce emissions to air of dust, particulate-bound metals, and trace species from the combustion of process fuels from the chemical industry in boilers, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Fuel choice; (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",2,"5","Green","Continuous ",0,0,0.03,"Yearly",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","New","100 % process fuels from the chemical industry in boilers","≥ 300 MWth","Unspecified","Air","Particulates (PM10) (Annual Mean)","In order to reduce emissions to air of dust, particulate-bound metals, and trace species from the combustion of process fuels from the chemical industry in boilers, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Fuel choice; (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",2,"5","Green","Continuous ",0,0,0.03,"Yearly",0]
["LCP","1. Energy industries","Unspecified","Unspecified","Boilers","New","100 % process fuels from the chemical industry in boilers","≥ 300 MWth","Unspecified","Air","Particulates (PM10) (24 hr Mean)","In order to reduce emissions to air of dust, particulate-bound metals, and trace species from the combustion of process fuels from the chemical industry in boilers, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Fuel choice; (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",2,"10","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","New","100 % process fuels from the chemical industry in boilers","≥ 300 MWth","Unspecified","Air","Particulates (PM10) (24 hr Mean)","In order to reduce emissions to air of dust, particulate-bound metals, and trace species from the combustion of process fuels from the chemical industry in boilers, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Fuel choice; (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",2,"10","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ",0]
["LCP","1. Energy industries","Unspecified","Unspecified","Boilers","New","HFO and/or gas oil in boilers","< 300 MWth ","Unspecified","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Multicyclones; (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD); (vi) Fuel choice","mg/Nm3",2,"10","Green","Continuous ",0,0,0.03,"Yearly",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","New","HFO and/or gas oil in boilers","< 300 MWth ","Unspecified","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Multicyclones; (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD); (vi) Fuel choice","mg/Nm3",2,"10","Green","Continuous ",0,0,0.03,"Yearly",0]
["LCP","1. Energy industries","Unspecified","Unspecified","Boilers","New","HFO and/or gas oil in boilers","< 300 MWth ","Unspecified","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Multicyclones; (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD); (vi) Fuel choice","mg/Nm3",7,"18","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","New","HFO and/or gas oil in boilers","< 300 MWth ","Unspecified","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Multicyclones; (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD); (vi) Fuel choice","mg/Nm3",7,"18","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ",0]
["LCP","1. Energy industries","Unspecified","Unspecified","Boilers","New","HFO and/or gas oil in boilers","≥ 300 MWth","Unspecified","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Multicyclones; (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD); (vi) Fuel choice","mg/Nm3",2,"5","Green","Continuous ",0,0,0.03,"Yearly",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","New","HFO and/or gas oil in boilers","≥ 300 MWth","Unspecified","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Multicyclones; (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD); (vi) Fuel choice","mg/Nm3",2,"5","Green","Continuous ",0,0,0.03,"Yearly",0]
["LCP","1. Energy industries","Unspecified","Unspecified","Boilers","New","HFO and/or gas oil in boilers","≥ 300 MWth","Unspecified","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Multicyclones; (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD); (vi) Fuel choice","mg/Nm3",7,"10","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","New","HFO and/or gas oil in boilers","≥ 300 MWth","Unspecified","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and particulate-bound metal emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Multicyclones; (iv) Dry or semi-dry FGD system; (v) Wet flue-gas desulphurisation (wet FGD); (vi) Fuel choice","mg/Nm3",7,"10","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ",0]
["LCP","1. Energy industries","Unspecified","Unspecified","CCGT","Unspecified","100% iron and steel process gases ","Unspecified ","Unspecified","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust emissions to air from the combustion of iron and steel process gases, BAT is to use one or a combination of the techniques given below: (i) Fuel choice/management; (ii) Blast furnace gas pretreatment at the iron- and steel-works; (iii) Basic oxygen furnace gas pretreatment at the iron- and steel- works; (iv) Electrostatic precipitator (ESP); (v) Bag filter","mg/Nm3",2,"5","Amber","Continuous ",0,0,0,"Yearly","For existing plants operated < 1 500 h/yr, these BAT-AELs do not apply.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","CCGT","Unspecified","100% iron and steel process gases ","Unspecified ","Unspecified","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust emissions to air from the combustion of iron and steel process gases, BAT is to use one or a combination of the techniques given below: (i) Fuel choice/management; (ii) Blast furnace gas pretreatment at the iron- and steel-works; (iii) Basic oxygen furnace gas pretreatment at the iron- and steel- works; (iv) Electrostatic precipitator (ESP); (v) Bag filter","mg/Nm3",2,"5","Amber","Continuous ",0,0,0,"Yearly","For existing plants operated < 1 500 h/yr, these BAT-AELs do not apply."]
["LCP","1. Energy industries","Unspecified","Unspecified","CCGT","Unspecified","100% iron and steel process gases ","Unspecified ","Unspecified","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust emissions to air from the combustion of iron and steel process gases, BAT is to use one or a combination of the techniques given below: (i) Fuel choice/management; (ii) Blast furnace gas pretreatment at the iron- and steel-works; (iii) Basic oxygen furnace gas pretreatment at the iron- and steel- works; (iv) Electrostatic precipitator (ESP); (v) Bag filter","mg/Nm3",2,"5","Amber","Continuous ",0,0,0,"Daily average or average over the sampling period ","For existing plants operated < 500 h/yr, these levels are indicative",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","CCGT","Unspecified","100% iron and steel process gases ","Unspecified ","Unspecified","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust emissions to air from the combustion of iron and steel process gases, BAT is to use one or a combination of the techniques given below: (i) Fuel choice/management; (ii) Blast furnace gas pretreatment at the iron- and steel-works; (iii) Basic oxygen furnace gas pretreatment at the iron- and steel- works; (iv) Electrostatic precipitator (ESP); (v) Bag filter","mg/Nm3",2,"5","Amber","Continuous ",0,0,0,"Daily average or average over the sampling period ","For existing plants operated < 500 h/yr, these levels are indicative"]
["LCP","1. Energy industries","Unspecified","Unspecified","Fired engines ","Existing","HFO and/or gas oil in reciprocating engines","≥ 50 MWth","Unspecified","Air","Particulates (PM10) (Annual Mean)","In order to prevent or reduce dust and particulate-bound metal emissions from the combustion of HFO and/or gas oil in reciprocating engines, BAT is to use one or a combination of the techniques given below: (i) Fuel choice; (ii) Electrostatic precipitator (ESP); (iii) Bag filter ","mg/Nm3",5,"35","Green","Continuous ",0,0,0.15,"Yearly","These BAT-AELs do not apply to plants operated < 1 500 h/yr.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Fired engines ","Existing","HFO and/or gas oil in reciprocating engines","≥ 50 MWth","Unspecified","Air","Particulates (PM10) (Annual Mean)","In order to prevent or reduce dust and particulate-bound metal emissions from the combustion of HFO and/or gas oil in reciprocating engines, BAT is to use one or a combination of the techniques given below: (i) Fuel choice; (ii) Electrostatic precipitator (ESP); (iii) Bag filter ","mg/Nm3",5,"35","Green","Continuous ",0,0,0.15,"Yearly","These BAT-AELs do not apply to plants operated < 1 500 h/yr."]
["LCP","1. Energy industries","Unspecified","Unspecified","Fired engines ","Existing","HFO and/or gas oil in reciprocating engines","≥ 50 MWth","Unspecified","Air","Particulates (PM10) (24 hr Mean)","In order to prevent or reduce dust and particulate-bound metal emissions from the combustion of HFO and/or gas oil in reciprocating engines, BAT is to use one or a combination of the techniques given below: (i) Fuel choice; (ii) Electrostatic precipitator (ESP); (iii) Bag filter ","mg/Nm3",10,"45","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period ","For plants operated < 500 h/yr, these levels are indicative.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Fired engines ","Existing","HFO and/or gas oil in reciprocating engines","≥ 50 MWth","Unspecified","Air","Particulates (PM10) (24 hr Mean)","In order to prevent or reduce dust and particulate-bound metal emissions from the combustion of HFO and/or gas oil in reciprocating engines, BAT is to use one or a combination of the techniques given below: (i) Fuel choice; (ii) Electrostatic precipitator (ESP); (iii) Bag filter ","mg/Nm3",10,"45","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period ","For plants operated < 500 h/yr, these levels are indicative."]
["LCP","1. Energy industries","Unspecified","Unspecified","Fired engines ","New","HFO and/or gas oil in reciprocating engines","≥ 50 MWth","Unspecified","Air","Particulates (PM10) (Annual Mean)","In order to prevent or reduce dust and particulate-bound metal emissions from the combustion of HFO and/or gas oil in reciprocating engines, BAT is to use one or a combination of the techniques given below: (i) Fuel choice; (ii) Electrostatic precipitator (ESP); (iii) Bag filter ","mg/Nm3",5,"10","Green","Continuous ",0,0,0.15,"Yearly",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Fired engines ","New","HFO and/or gas oil in reciprocating engines","≥ 50 MWth","Unspecified","Air","Particulates (PM10) (Annual Mean)","In order to prevent or reduce dust and particulate-bound metal emissions from the combustion of HFO and/or gas oil in reciprocating engines, BAT is to use one or a combination of the techniques given below: (i) Fuel choice; (ii) Electrostatic precipitator (ESP); (iii) Bag filter ","mg/Nm3",5,"10","Green","Continuous ",0,0,0.15,"Yearly",0]
["LCP","1. Energy industries","Unspecified","Unspecified","Fired engines ","New","HFO and/or gas oil in reciprocating engines","≥ 50 MWth","Unspecified","Air","Particulates (PM10) (24 hr Mean)","In order to prevent or reduce dust and particulate-bound metal emissions from the combustion of HFO and/or gas oil in reciprocating engines, BAT is to use one or a combination of the techniques given below: (i) Fuel choice; (ii) Electrostatic precipitator (ESP); (iii) Bag filter ","mg/Nm3",10,"20","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Fired engines ","New","HFO and/or gas oil in reciprocating engines","≥ 50 MWth","Unspecified","Air","Particulates (PM10) (24 hr Mean)","In order to prevent or reduce dust and particulate-bound metal emissions from the combustion of HFO and/or gas oil in reciprocating engines, BAT is to use one or a combination of the techniques given below: (i) Fuel choice; (ii) Electrostatic precipitator (ESP); (iii) Bag filter ","mg/Nm3",10,"20","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period ",0]
["LCP","1. Energy industries","Unspecified","Unspecified","IGCC","Unspecified","Unspecified","≥ 100 MWth","Unspecified","Air","Particulates (PM10) (24 hr Mean)",0,"mg/Nm3","N/A","0.025","Green","Continuous",0,0,0.15,"Average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","IGCC","Unspecified","Unspecified","≥ 100 MWth","Unspecified","Air","Particulates (PM10) (24 hr Mean)",0,"mg/Nm3","N/A","0.025","Green","Continuous",0,0,0.15,"Average over the sampling period",0]
["LCP","1. Energy industries","Unspecified","Unspecified","IGCC","Unspecified","Unspecified","≥ 100 MWth","Unspecified","Air","Particulates (PM10) (24 hr Mean)",0,"ug/Nm3","N/A","1","Green","Continuous",0,0,0.15,"Average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","IGCC","Unspecified","Unspecified","≥ 100 MWth","Unspecified","Air","Particulates (PM10) (24 hr Mean)",0,"ug/Nm3","N/A","1","Green","Continuous",0,0,0.15,"Average over the sampling period",0]
["LCP","1. Energy industries","Unspecified","Unspecified","IGCC","Unspecified","Unspecified","≥ 100 MWth","Unspecified","Air","Particulates (PM10) (Annual Mean)",0,"mg/Nm3","N/A","2.5","Green","Continuous",0,0,0.15,"Yearly average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","IGCC","Unspecified","Unspecified","≥ 100 MWth","Unspecified","Air","Particulates (PM10) (Annual Mean)",0,"mg/Nm3","N/A","2.5","Green","Continuous",0,0,0.15,"Yearly average",0]
["LCP","1. Energy industries","Unspecified","Unspecified","Spark-ignited lean-burn gas engine","Unspecified","Natural gas ","≥ 50 MWth","Unspecified","Air","Formaldehyde and CH4",0,"mg/Nm3",5,"15","Green","Once every year",0,0,0.15,"Average over the sampling period","For existing plants operated < 500 h/yr, these levels are indicative.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Spark-ignited lean-burn gas engine","Unspecified","Natural gas ","≥ 50 MWth","Unspecified","Air","Formaldehyde and CH4",0,"mg/Nm3",5,"15","Green","Once every year",0,0,0.15,"Average over the sampling period","For existing plants operated < 500 h/yr, these levels are indicative."]
["LCP","1. Energy industries","Unspecified","Unspecified","Spark-ignited lean-burn gas engine","New","Natural gas ","≥ 50 MWth","Unspecified","Air","Formaldehyde and CH4",0,"mg/Nm3",215,"500","Green","Once every year",0,0,0.15,"Average over the sampling period","This BAT-AEL is expressed as C at full load operation.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Spark-ignited lean-burn gas engine","New","Natural gas ","≥ 50 MWth","Unspecified","Air","Formaldehyde and CH4",0,"mg/Nm3",215,"500","Green","Once every year",0,0,0.15,"Average over the sampling period","This BAT-AEL is expressed as C at full load operation."]
["LCP","1. Energy industries","Unspecified","Unspecified","Spark-ignited lean-burn gas engine","Existing","Natural gas ","≥ 50 MWth","Unspecified","Air","Formaldehyde and CH4",0,"mg/Nm3",215,"560","Green","Once every year",0,0,0.15,"Average over the sampling period","For existing plants operated < 500 h/yr, these levels are indicative.\n\nThis BAT-AEL is expressed as C at full load operation.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Spark-ignited lean-burn gas engine","Existing","Natural gas ","≥ 50 MWth","Unspecified","Air","Formaldehyde and CH4",0,"mg/Nm3",215,"560","Green","Once every year",0,0,0.15,"Average over the sampling period","For existing plants operated < 500 h/yr, these levels are indicative.\n\nThis BAT-AEL is expressed as C at full load operation."]
["LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Coal and/or lignite ","< 100 MWth","Unspecified","Air","Hydrogen chloride","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD; (viii) Combined techniques for NOX and SOX reduction; (ix) Replacement or removal of the gas- gas heater located downstream of the wet FGD; (x) Fuel choice","mg/Nm3",2,10,"Green","Once every three months ",0,0,0.06,"Yearly average or average of samples obtained during one year ","The lower end of these BAT-AEL ranges may be difficult to achieve in the case of plants fitted with wet FGD and a downstream gas-gas heater.\n\nThe higher end of the BAT-AEL range is 20 mg/Nm3 in the following cases: plants combusting fuels where the average chlorine content is 1 000 mg/kg (dry) or higher; plants operated < 1 500 h/yr; FBC boilers. For plants operated < 500 h/yr, these levels are indicative.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Coal and/or lignite ","< 100 MWth","Unspecified","Air","Hydrogen chloride","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD; (viii) Combined techniques for NOX and SOX reduction; (ix) Replacement or removal of the gas- gas heater located downstream of the wet FGD; (x) Fuel choice","mg/Nm3",2,10,"Green","Once every three months ",0,0,0.06,"Yearly average or average of samples obtained during one year ","The lower end of these BAT-AEL ranges may be difficult to achieve in the case of plants fitted with wet FGD and a downstream gas-gas heater.\n\nThe higher end of the BAT-AEL range is 20 mg/Nm3 in the following cases: plants combusting fuels where the average chlorine content is 1 000 mg/kg (dry) or higher; plants operated < 1 500 h/yr; FBC boilers. For plants operated < 500 h/yr, these levels are indicative."]
["LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Coal and/or lignite ","≥ 100 MWth","Unspecified","Air","Hydrogen chloride","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD; (viii) Combined techniques for NOX and SOX reduction; (ix) Replacement or removal of the gas- gas heater located downstream of the wet FGD; (x) Fuel choice","mg/Nm3",1,5,"Green","Once every three months ",0,0,0.06,"Yearly average or average of samples obtained during one year ","The lower end of these BAT-AEL ranges may be difficult to achieve in the case of plants fitted with wet FGD and a downstream gas-gas heater.\n\nThe higher end of the BAT-AEL range is 20 mg/Nm3 in the following cases: plants combusting fuels where the average chlorine content is 1 000 mg/kg (dry) or higher; plants operated < 1 500 h/yr; FBC boilers. For plants operated < 500 h/yr, these levels are indicative.\n\nIn the case of plants fitted with wet FGD with a downstream gas-gas heater, the higher end of the BAT-AEL range is 7 mg/Nm3.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Coal and/or lignite ","≥ 100 MWth","Unspecified","Air","Hydrogen chloride","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD; (viii) Combined techniques for NOX and SOX reduction; (ix) Replacement or removal of the gas- gas heater located downstream of the wet FGD; (x) Fuel choice","mg/Nm3",1,5,"Green","Once every three months ",0,0,0.06,"Yearly average or average of samples obtained during one year ","The lower end of these BAT-AEL ranges may be difficult to achieve in the case of plants fitted with wet FGD and a downstream gas-gas heater.\n\nThe higher end of the BAT-AEL range is 20 mg/Nm3 in the following cases: plants combusting fuels where the average chlorine content is 1 000 mg/kg (dry) or higher; plants operated < 1 500 h/yr; FBC boilers. For plants operated < 500 h/yr, these levels are indicative.\n\nIn the case of plants fitted with wet FGD with a downstream gas-gas heater, the higher end of the BAT-AEL range is 7 mg/Nm3."]
["LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Solid biomass and/or peat","< 100 MWth ","Unspecified","Air","Hydrogen chloride","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3",1,"15","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ","For plants burning fuels where the average chlorine content is ≥ 0,1 wt-% (dry), or for existing plants co-combusting biomass with sulphur-rich fuel (e.g. peat) or using alkali chloride-converting additives (e.g. elemental sulphur), the higher end of the BAT-AEL range for the yearly average for new plants is 15 mg/Nm3, the higher end of the BAT-AEL range for the yearly average for existing plants is 25 mg/Nm3. The daily average BAT-AEL range does not apply to these plants.\n\nThe daily average BAT-AEL range does not apply to plants operated < 1 500 h/yr. The higher end of the BAT-AEL range for the yearly average for new plants operated < 1 500 h/yr is 15 mg/Nm3.\n\nThese BAT-AELs do not apply to plants operated < 1 500 h/yr.\n\nThe lower end of these BAT-AEL ranges may be difficult to achieve in the case of plants fitted with wet FGD and a downstream gas-gas heater.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Solid biomass and/or peat","< 100 MWth ","Unspecified","Air","Hydrogen chloride","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3",1,"15","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ","For plants burning fuels where the average chlorine content is ≥ 0,1 wt-% (dry), or for existing plants co-combusting biomass with sulphur-rich fuel (e.g. peat) or using alkali chloride-converting additives (e.g. elemental sulphur), the higher end of the BAT-AEL range for the yearly average for new plants is 15 mg/Nm3, the higher end of the BAT-AEL range for the yearly average for existing plants is 25 mg/Nm3. The daily average BAT-AEL range does not apply to these plants.\n\nThe daily average BAT-AEL range does not apply to plants operated < 1 500 h/yr. The higher end of the BAT-AEL range for the yearly average for new plants operated < 1 500 h/yr is 15 mg/Nm3.\n\nThese BAT-AELs do not apply to plants operated < 1 500 h/yr.\n\nThe lower end of these BAT-AEL ranges may be difficult to achieve in the case of plants fitted with wet FGD and a downstream gas-gas heater."]
["LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Solid biomass and/or peat","< 100 MWth ","Unspecified","Air","Hydrogen chloride","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3",1,"35","Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ","For plants burning fuels where the average chlorine content is ≥ 0,1 wt-% (dry), or for existing plants co-combusting biomass with sulphur-rich fuel (e.g. peat) or using alkali chloride-converting additives (e.g. elemental sulphur), the higher end of the BAT-AEL range for the yearly average for new plants is 15 mg/Nm3, the higher end of the BAT-AEL range for the yearly average for existing plants is 25 mg/Nm3. The daily average BAT-AEL range does not apply to these plants.\n\nThe daily average BAT-AEL range does not apply to plants operated < 1 500 h/yr. The higher end of the BAT-AEL range for the yearly average for new plants operated < 1 500 h/yr is 15 mg/Nm3.\n\nFor plants operated < 500 h/yr, these levels are indicative",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Solid biomass and/or peat","< 100 MWth ","Unspecified","Air","Hydrogen chloride","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3",1,"35","Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ","For plants burning fuels where the average chlorine content is ≥ 0,1 wt-% (dry), or for existing plants co-combusting biomass with sulphur-rich fuel (e.g. peat) or using alkali chloride-converting additives (e.g. elemental sulphur), the higher end of the BAT-AEL range for the yearly average for new plants is 15 mg/Nm3, the higher end of the BAT-AEL range for the yearly average for existing plants is 25 mg/Nm3. The daily average BAT-AEL range does not apply to these plants.\n\nThe daily average BAT-AEL range does not apply to plants operated < 1 500 h/yr. The higher end of the BAT-AEL range for the yearly average for new plants operated < 1 500 h/yr is 15 mg/Nm3.\n\nFor plants operated < 500 h/yr, these levels are indicative"]
["LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Solid biomass and/or peat","≥ 300 MWth","Unspecified","Air","Hydrogen chloride","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3",1,"5","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ","For plants burning fuels where the average chlorine content is ≥ 0,1 wt-% (dry), or for existing plants co-combusting biomass with sulphur-rich fuel (e.g. peat) or using alkali chloride-converting additives (e.g. elemental sulphur), the higher end of the BAT-AEL range for the yearly average for new plants is 15 mg/Nm3, the higher end of the BAT-AEL range for the yearly average for existing plants is 25 mg/Nm3. The daily average BAT-AEL range does not apply to these plants.\n\nThe daily average BAT-AEL range does not apply to plants operated < 1 500 h/yr. The higher end of the BAT-AEL range for the yearly average for new plants operated < 1 500 h/yr is 15 mg/Nm3.\n\nThese BAT-AELs do not apply to plants operated < 1 500 h/yr.\n\nThe lower end of these BAT-AEL ranges may be difficult to achieve in the case of plants fitted with wet FGD and a downstream gas-gas heater.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Solid biomass and/or peat","≥ 300 MWth","Unspecified","Air","Hydrogen chloride","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3",1,"5","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ","For plants burning fuels where the average chlorine content is ≥ 0,1 wt-% (dry), or for existing plants co-combusting biomass with sulphur-rich fuel (e.g. peat) or using alkali chloride-converting additives (e.g. elemental sulphur), the higher end of the BAT-AEL range for the yearly average for new plants is 15 mg/Nm3, the higher end of the BAT-AEL range for the yearly average for existing plants is 25 mg/Nm3. The daily average BAT-AEL range does not apply to these plants.\n\nThe daily average BAT-AEL range does not apply to plants operated < 1 500 h/yr. The higher end of the BAT-AEL range for the yearly average for new plants operated < 1 500 h/yr is 15 mg/Nm3.\n\nThese BAT-AELs do not apply to plants operated < 1 500 h/yr.\n\nThe lower end of these BAT-AEL ranges may be difficult to achieve in the case of plants fitted with wet FGD and a downstream gas-gas heater."]
["LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Solid biomass and/or peat","≥ 300 MWth","Unspecified","Air","Hydrogen chloride","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3",1,"12","Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ","For plants burning fuels where the average chlorine content is ≥ 0,1 wt-% (dry), or for existing plants co-combusting biomass with sulphur-rich fuel (e.g. peat) or using alkali chloride-converting additives (e.g. elemental sulphur), the higher end of the BAT-AEL range for the yearly average for new plants is 15 mg/Nm3, the higher end of the BAT-AEL range for the yearly average for existing plants is 25 mg/Nm3. The daily average BAT-AEL range does not apply to these plants.\n\nThe daily average BAT-AEL range does not apply to plants operated < 1 500 h/yr. The higher end of the BAT-AEL range for the yearly average for new plants operated < 1 500 h/yr is 15 mg/Nm3.\n\nFor plants operated < 500 h/yr, these levels are indicative",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Solid biomass and/or peat","≥ 300 MWth","Unspecified","Air","Hydrogen chloride","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3",1,"12","Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ","For plants burning fuels where the average chlorine content is ≥ 0,1 wt-% (dry), or for existing plants co-combusting biomass with sulphur-rich fuel (e.g. peat) or using alkali chloride-converting additives (e.g. elemental sulphur), the higher end of the BAT-AEL range for the yearly average for new plants is 15 mg/Nm3, the higher end of the BAT-AEL range for the yearly average for existing plants is 25 mg/Nm3. The daily average BAT-AEL range does not apply to these plants.\n\nThe daily average BAT-AEL range does not apply to plants operated < 1 500 h/yr. The higher end of the BAT-AEL range for the yearly average for new plants operated < 1 500 h/yr is 15 mg/Nm3.\n\nFor plants operated < 500 h/yr, these levels are indicative"]
["LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Solid biomass and/or peat","100-300 MWth","Unspecified","Air","Hydrogen chloride","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3",1,"9","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ","For plants burning fuels where the average chlorine content is ≥ 0,1 wt-% (dry), or for existing plants co-combusting biomass with sulphur-rich fuel (e.g. peat) or using alkali chloride-converting additives (e.g. elemental sulphur), the higher end of the BAT-AEL range for the yearly average for new plants is 15 mg/Nm3, the higher end of the BAT-AEL range for the yearly average for existing plants is 25 mg/Nm3. The daily average BAT-AEL range does not apply to these plants.\n\nThe daily average BAT-AEL range does not apply to plants operated < 1 500 h/yr. The higher end of the BAT-AEL range for the yearly average for new plants operated < 1 500 h/yr is 15 mg/Nm3.\n\nThese BAT-AELs do not apply to plants operated < 1 500 h/yr.\n\nThe lower end of these BAT-AEL ranges may be difficult to achieve in the case of plants fitted with wet FGD and a downstream gas-gas heater.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Solid biomass and/or peat","100-300 MWth","Unspecified","Air","Hydrogen chloride","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3",1,"9","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ","For plants burning fuels where the average chlorine content is ≥ 0,1 wt-% (dry), or for existing plants co-combusting biomass with sulphur-rich fuel (e.g. peat) or using alkali chloride-converting additives (e.g. elemental sulphur), the higher end of the BAT-AEL range for the yearly average for new plants is 15 mg/Nm3, the higher end of the BAT-AEL range for the yearly average for existing plants is 25 mg/Nm3. The daily average BAT-AEL range does not apply to these plants.\n\nThe daily average BAT-AEL range does not apply to plants operated < 1 500 h/yr. The higher end of the BAT-AEL range for the yearly average for new plants operated < 1 500 h/yr is 15 mg/Nm3.\n\nThese BAT-AELs do not apply to plants operated < 1 500 h/yr.\n\nThe lower end of these BAT-AEL ranges may be difficult to achieve in the case of plants fitted with wet FGD and a downstream gas-gas heater."]
["LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Solid biomass and/or peat","100-300 MWth","Unspecified","Air","Hydrogen chloride","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3",1,"12","Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ","For plants burning fuels where the average chlorine content is ≥ 0,1 wt-% (dry), or for existing plants co-combusting biomass with sulphur-rich fuel (e.g. peat) or using alkali chloride-converting additives (e.g. elemental sulphur), the higher end of the BAT-AEL range for the yearly average for new plants is 15 mg/Nm3, the higher end of the BAT-AEL range for the yearly average for existing plants is 25 mg/Nm3. The daily average BAT-AEL range does not apply to these plants.\n\nThe daily average BAT-AEL range does not apply to plants operated < 1 500 h/yr. The higher end of the BAT-AEL range for the yearly average for new plants operated < 1 500 h/yr is 15 mg/Nm3.\n\nFor plants operated < 500 h/yr, these levels are indicative",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Solid biomass and/or peat","100-300 MWth","Unspecified","Air","Hydrogen chloride","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3",1,"12","Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ","For plants burning fuels where the average chlorine content is ≥ 0,1 wt-% (dry), or for existing plants co-combusting biomass with sulphur-rich fuel (e.g. peat) or using alkali chloride-converting additives (e.g. elemental sulphur), the higher end of the BAT-AEL range for the yearly average for new plants is 15 mg/Nm3, the higher end of the BAT-AEL range for the yearly average for existing plants is 25 mg/Nm3. The daily average BAT-AEL range does not apply to these plants.\n\nThe daily average BAT-AEL range does not apply to plants operated < 1 500 h/yr. The higher end of the BAT-AEL range for the yearly average for new plants operated < 1 500 h/yr is 15 mg/Nm3.\n\nFor plants operated < 500 h/yr, these levels are indicative"]
["LCP","1. Energy industries","Unspecified","Unspecified","All","New","Coal and/or lignite ","< 100 MWth","Unspecified","Air","Hydrogen chloride","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD; (viii) Combined techniques for NOX and SOX reduction; (ix) Replacement or removal of the gas- gas heater located downstream of the wet FGD; (x) Fuel choice","mg/Nm3",1,6,"Green","Once every three months ",0,0,0.06,"Yearly average or average of samples obtained during one year ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","New","Coal and/or lignite ","< 100 MWth","Unspecified","Air","Hydrogen chloride","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD; (viii) Combined techniques for NOX and SOX reduction; (ix) Replacement or removal of the gas- gas heater located downstream of the wet FGD; (x) Fuel choice","mg/Nm3",1,6,"Green","Once every three months ",0,0,0.06,"Yearly average or average of samples obtained during one year ",0]
["LCP","1. Energy industries","Unspecified","Unspecified","All","New","Coal and/or lignite ","≥ 100 MWth","Unspecified","Air","Hydrogen chloride","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD; (viii) Combined techniques for NOX and SOX reduction; (ix) Replacement or removal of the gas- gas heater located downstream of the wet FGD; (x) Fuel choice","mg/Nm3",1,3,"Green","Once every three months ",0,0,0.06,"Yearly average or average of samples obtained during one year ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","New","Coal and/or lignite ","≥ 100 MWth","Unspecified","Air","Hydrogen chloride","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD; (viii) Combined techniques for NOX and SOX reduction; (ix) Replacement or removal of the gas- gas heater located downstream of the wet FGD; (x) Fuel choice","mg/Nm3",1,3,"Green","Once every three months ",0,0,0.06,"Yearly average or average of samples obtained during one year ",0]
["LCP","1. Energy industries","Unspecified","Unspecified","All","New","Solid biomass and/or peat","< 100 MWth ","Unspecified","Air","Hydrogen chloride","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3",1,"7","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ","For plants burning fuels where the average chlorine content is ≥ 0,1 wt-% (dry), or for existing plants co-combusting biomass with sulphur-rich fuel (e.g. peat) or using alkali chloride-converting additives (e.g. elemental sulphur), the higher end of the BAT-AEL range for the yearly average for new plants is 15 mg/Nm3, the higher end of the BAT-AEL range for the yearly average for existing plants is 25 mg/Nm3. The daily average BAT-AEL range does not apply to these plants.\n\nThe daily average BAT-AEL range does not apply to plants operated < 1 500 h/yr. The higher end of the BAT-AEL range for the yearly average for new plants operated < 1 500 h/yr is 15 mg/Nm3.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","New","Solid biomass and/or peat","< 100 MWth ","Unspecified","Air","Hydrogen chloride","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3",1,"7","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ","For plants burning fuels where the average chlorine content is ≥ 0,1 wt-% (dry), or for existing plants co-combusting biomass with sulphur-rich fuel (e.g. peat) or using alkali chloride-converting additives (e.g. elemental sulphur), the higher end of the BAT-AEL range for the yearly average for new plants is 15 mg/Nm3, the higher end of the BAT-AEL range for the yearly average for existing plants is 25 mg/Nm3. The daily average BAT-AEL range does not apply to these plants.\n\nThe daily average BAT-AEL range does not apply to plants operated < 1 500 h/yr. The higher end of the BAT-AEL range for the yearly average for new plants operated < 1 500 h/yr is 15 mg/Nm3."]
["LCP","1. Energy industries","Unspecified","Unspecified","All","New","Solid biomass and/or peat","< 100 MWth ","Unspecified","Air","Hydrogen chloride","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3",1,"12","Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ","For plants burning fuels where the average chlorine content is ≥ 0,1 wt-% (dry), or for existing plants co-combusting biomass with sulphur-rich fuel (e.g. peat) or using alkali chloride-converting additives (e.g. elemental sulphur), the higher end of the BAT-AEL range for the yearly average for new plants is 15 mg/Nm3, the higher end of the BAT-AEL range for the yearly average for existing plants is 25 mg/Nm3. The daily average BAT-AEL range does not apply to these plants.\n\nThe daily average BAT-AEL range does not apply to plants operated < 1 500 h/yr. The higher end of the BAT-AEL range for the yearly average for new plants operated < 1 500 h/yr is 15 mg/Nm3.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","New","Solid biomass and/or peat","< 100 MWth ","Unspecified","Air","Hydrogen chloride","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3",1,"12","Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ","For plants burning fuels where the average chlorine content is ≥ 0,1 wt-% (dry), or for existing plants co-combusting biomass with sulphur-rich fuel (e.g. peat) or using alkali chloride-converting additives (e.g. elemental sulphur), the higher end of the BAT-AEL range for the yearly average for new plants is 15 mg/Nm3, the higher end of the BAT-AEL range for the yearly average for existing plants is 25 mg/Nm3. The daily average BAT-AEL range does not apply to these plants.\n\nThe daily average BAT-AEL range does not apply to plants operated < 1 500 h/yr. The higher end of the BAT-AEL range for the yearly average for new plants operated < 1 500 h/yr is 15 mg/Nm3."]
["LCP","1. Energy industries","Unspecified","Unspecified","All","New","Solid biomass and/or peat","≥ 300 MWth","Unspecified","Air","Hydrogen chloride","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3",1,"5","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ","For plants burning fuels where the average chlorine content is ≥ 0,1 wt-% (dry), or for existing plants co-combusting biomass with sulphur-rich fuel (e.g. peat) or using alkali chloride-converting additives (e.g. elemental sulphur), the higher end of the BAT-AEL range for the yearly average for new plants is 15 mg/Nm3, the higher end of the BAT-AEL range for the yearly average for existing plants is 25 mg/Nm3. The daily average BAT-AEL range does not apply to these plants.\n\nThe daily average BAT-AEL range does not apply to plants operated < 1 500 h/yr. The higher end of the BAT-AEL range for the yearly average for new plants operated < 1 500 h/yr is 15 mg/Nm3.\n\nThese BAT-AELs do not apply to plants operated < 1 500 h/yr.\n\nThe lower end of these BAT-AEL ranges may be difficult to achieve in the case of plants fitted with wet FGD and a downstream gas-gas heater.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","New","Solid biomass and/or peat","≥ 300 MWth","Unspecified","Air","Hydrogen chloride","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3",1,"5","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ","For plants burning fuels where the average chlorine content is ≥ 0,1 wt-% (dry), or for existing plants co-combusting biomass with sulphur-rich fuel (e.g. peat) or using alkali chloride-converting additives (e.g. elemental sulphur), the higher end of the BAT-AEL range for the yearly average for new plants is 15 mg/Nm3, the higher end of the BAT-AEL range for the yearly average for existing plants is 25 mg/Nm3. The daily average BAT-AEL range does not apply to these plants.\n\nThe daily average BAT-AEL range does not apply to plants operated < 1 500 h/yr. The higher end of the BAT-AEL range for the yearly average for new plants operated < 1 500 h/yr is 15 mg/Nm3.\n\nThese BAT-AELs do not apply to plants operated < 1 500 h/yr.\n\nThe lower end of these BAT-AEL ranges may be difficult to achieve in the case of plants fitted with wet FGD and a downstream gas-gas heater."]
["LCP","1. Energy industries","Unspecified","Unspecified","All","New","Solid biomass and/or peat","≥ 300 MWth","Unspecified","Air","Hydrogen chloride","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3",1,"12","Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ","For plants burning fuels where the average chlorine content is ≥ 0,1 wt-% (dry), or for existing plants co-combusting biomass with sulphur-rich fuel (e.g. peat) or using alkali chloride-converting additives (e.g. elemental sulphur), the higher end of the BAT-AEL range for the yearly average for new plants is 15 mg/Nm3, the higher end of the BAT-AEL range for the yearly average for existing plants is 25 mg/Nm3. The daily average BAT-AEL range does not apply to these plants.\n\nThe daily average BAT-AEL range does not apply to plants operated < 1 500 h/yr. The higher end of the BAT-AEL range for the yearly average for new plants operated < 1 500 h/yr is 15 mg/Nm3.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","New","Solid biomass and/or peat","≥ 300 MWth","Unspecified","Air","Hydrogen chloride","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3",1,"12","Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ","For plants burning fuels where the average chlorine content is ≥ 0,1 wt-% (dry), or for existing plants co-combusting biomass with sulphur-rich fuel (e.g. peat) or using alkali chloride-converting additives (e.g. elemental sulphur), the higher end of the BAT-AEL range for the yearly average for new plants is 15 mg/Nm3, the higher end of the BAT-AEL range for the yearly average for existing plants is 25 mg/Nm3. The daily average BAT-AEL range does not apply to these plants.\n\nThe daily average BAT-AEL range does not apply to plants operated < 1 500 h/yr. The higher end of the BAT-AEL range for the yearly average for new plants operated < 1 500 h/yr is 15 mg/Nm3."]
["LCP","1. Energy industries","Unspecified","Unspecified","All","New","Solid biomass and/or peat","100-300 MWth","Unspecified","Air","Hydrogen chloride","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3",1,"5","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ","For plants burning fuels where the average chlorine content is ≥ 0,1 wt-% (dry), or for existing plants co-combusting biomass with sulphur-rich fuel (e.g. peat) or using alkali chloride-converting additives (e.g. elemental sulphur), the higher end of the BAT-AEL range for the yearly average for new plants is 15 mg/Nm3, the higher end of the BAT-AEL range for the yearly average for existing plants is 25 mg/Nm3. The daily average BAT-AEL range does not apply to these plants.\n\nThe daily average BAT-AEL range does not apply to plants operated < 1 500 h/yr. The higher end of the BAT-AEL range for the yearly average for new plants operated < 1 500 h/yr is 15 mg/Nm3.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","New","Solid biomass and/or peat","100-300 MWth","Unspecified","Air","Hydrogen chloride","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3",1,"5","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ","For plants burning fuels where the average chlorine content is ≥ 0,1 wt-% (dry), or for existing plants co-combusting biomass with sulphur-rich fuel (e.g. peat) or using alkali chloride-converting additives (e.g. elemental sulphur), the higher end of the BAT-AEL range for the yearly average for new plants is 15 mg/Nm3, the higher end of the BAT-AEL range for the yearly average for existing plants is 25 mg/Nm3. The daily average BAT-AEL range does not apply to these plants.\n\nThe daily average BAT-AEL range does not apply to plants operated < 1 500 h/yr. The higher end of the BAT-AEL range for the yearly average for new plants operated < 1 500 h/yr is 15 mg/Nm3."]
["LCP","1. Energy industries","Unspecified","Unspecified","All","New","Solid biomass and/or peat","100-300 MWth","Unspecified","Air","Hydrogen chloride","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3",1,"12","Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ","For plants burning fuels where the average chlorine content is ≥ 0,1 wt-% (dry), or for existing plants co-combusting biomass with sulphur-rich fuel (e.g. peat) or using alkali chloride-converting additives (e.g. elemental sulphur), the higher end of the BAT-AEL range for the yearly average for new plants is 15 mg/Nm3, the higher end of the BAT-AEL range for the yearly average for existing plants is 25 mg/Nm3. The daily average BAT-AEL range does not apply to these plants.\n\nThe daily average BAT-AEL range does not apply to plants operated < 1 500 h/yr. The higher end of the BAT-AEL range for the yearly average for new plants operated < 1 500 h/yr is 15 mg/Nm3.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","New","Solid biomass and/or peat","100-300 MWth","Unspecified","Air","Hydrogen chloride","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3",1,"12","Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ","For plants burning fuels where the average chlorine content is ≥ 0,1 wt-% (dry), or for existing plants co-combusting biomass with sulphur-rich fuel (e.g. peat) or using alkali chloride-converting additives (e.g. elemental sulphur), the higher end of the BAT-AEL range for the yearly average for new plants is 15 mg/Nm3, the higher end of the BAT-AEL range for the yearly average for existing plants is 25 mg/Nm3. The daily average BAT-AEL range does not apply to these plants.\n\nThe daily average BAT-AEL range does not apply to plants operated < 1 500 h/yr. The higher end of the BAT-AEL range for the yearly average for new plants operated < 1 500 h/yr is 15 mg/Nm3."]
["LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Existing","Process fuels from the chemical industry","< 100 MWth","Unspecified","Air","Hydrogen chloride","In order to reduce SOX, HCl and HF emissions to air from the combustion of process fuels from the chemical industry in boilers, BAT is to use one or a combination of the techniques given below: (i) Fuel choice; (ii) Boiler sorbent injection (in-furnace or in-bed); (iii) Duct sorbent injection (DSI); (iv) Spray dry absorber (SDA); (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD Table","mg/Nm3",2,"15","Green","Once every three months ",0,0,0.03,"Average of samples obtained during one year","For plants operated < 500 h/yr, these levels are indicative.\n\nIn the case of plants operated < 1 500 h/yr, the higher end of the BAT-AEL range is 20 mg/Nm3.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Existing","Process fuels from the chemical industry","< 100 MWth","Unspecified","Air","Hydrogen chloride","In order to reduce SOX, HCl and HF emissions to air from the combustion of process fuels from the chemical industry in boilers, BAT is to use one or a combination of the techniques given below: (i) Fuel choice; (ii) Boiler sorbent injection (in-furnace or in-bed); (iii) Duct sorbent injection (DSI); (iv) Spray dry absorber (SDA); (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD Table","mg/Nm3",2,"15","Green","Once every three months ",0,0,0.03,"Average of samples obtained during one year","For plants operated < 500 h/yr, these levels are indicative.\n\nIn the case of plants operated < 1 500 h/yr, the higher end of the BAT-AEL range is 20 mg/Nm3."]
["LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Existing","Process fuels from the chemical industry","≥ 100 MWth","Unspecified","Air","Hydrogen chloride","In order to reduce SOX, HCl and HF emissions to air from the combustion of process fuels from the chemical industry in boilers, BAT is to use one or a combination of the techniques given below: (i) Fuel choice; (ii) Boiler sorbent injection (in-furnace or in-bed); (iii) Duct sorbent injection (DSI); (iv) Spray dry absorber (SDA); (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD Table","mg/Nm3",1,"9","Green","Once every three months ",0,0,0.03,"Average of samples obtained during one year","For plants operated < 500 h/yr, these levels are indicative.\n\nIn the case of plants operated < 1 500 h/yr, the higher end of the BAT-AEL range is 20 mg/Nm3.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Existing","Process fuels from the chemical industry","≥ 100 MWth","Unspecified","Air","Hydrogen chloride","In order to reduce SOX, HCl and HF emissions to air from the combustion of process fuels from the chemical industry in boilers, BAT is to use one or a combination of the techniques given below: (i) Fuel choice; (ii) Boiler sorbent injection (in-furnace or in-bed); (iii) Duct sorbent injection (DSI); (iv) Spray dry absorber (SDA); (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD Table","mg/Nm3",1,"9","Green","Once every three months ",0,0,0.03,"Average of samples obtained during one year","For plants operated < 500 h/yr, these levels are indicative.\n\nIn the case of plants operated < 1 500 h/yr, the higher end of the BAT-AEL range is 20 mg/Nm3."]
["LCP","1. Energy industries","Unspecified","Unspecified","Boilers","New","Process fuels from the chemical industry","< 100 MWth","Unspecified","Air","Hydrogen chloride","In order to reduce SOX, HCl and HF emissions to air from the combustion of process fuels from the chemical industry in boilers, BAT is to use one or a combination of the techniques given below: (i) Fuel choice; (ii) Boiler sorbent injection (in-furnace or in-bed); (iii) Duct sorbent injection (DSI); (iv) Spray dry absorber (SDA); (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD Table","mg/Nm3",1,"7","Green","Once every three months ",0,0,0.03,"Average of samples obtained during one year",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","New","Process fuels from the chemical industry","< 100 MWth","Unspecified","Air","Hydrogen chloride","In order to reduce SOX, HCl and HF emissions to air from the combustion of process fuels from the chemical industry in boilers, BAT is to use one or a combination of the techniques given below: (i) Fuel choice; (ii) Boiler sorbent injection (in-furnace or in-bed); (iii) Duct sorbent injection (DSI); (iv) Spray dry absorber (SDA); (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD Table","mg/Nm3",1,"7","Green","Once every three months ",0,0,0.03,"Average of samples obtained during one year",0]
["LCP","1. Energy industries","Unspecified","Unspecified","Boilers","New","Process fuels from the chemical industry","≥ 100 MWth","Unspecified","Air","Hydrogen chloride","In order to reduce SOX, HCl and HF emissions to air from the combustion of process fuels from the chemical industry in boilers, BAT is to use one or a combination of the techniques given below: (i) Fuel choice; (ii) Boiler sorbent injection (in-furnace or in-bed); (iii) Duct sorbent injection (DSI); (iv) Spray dry absorber (SDA); (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD Table","mg/Nm3",1,"5","Green","Once every three months ",0,0,0.03,"Average of samples obtained during one year",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","New","Process fuels from the chemical industry","≥ 100 MWth","Unspecified","Air","Hydrogen chloride","In order to reduce SOX, HCl and HF emissions to air from the combustion of process fuels from the chemical industry in boilers, BAT is to use one or a combination of the techniques given below: (i) Fuel choice; (ii) Boiler sorbent injection (in-furnace or in-bed); (iii) Duct sorbent injection (DSI); (iv) Spray dry absorber (SDA); (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD Table","mg/Nm3",1,"5","Green","Once every three months ",0,0,0.03,"Average of samples obtained during one year",0]
["LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Coal and/or lignite ","< 100 MWth","Unspecified","Air","Hydrogen fluoride (as F) (Ecological - Daily Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD; (viii) Combined techniques for NOX and SOX reduction; (ix) Replacement or removal of the gas- gas heater located downstream of the wet FGD; (x) Fuel choice","mg/Nm3",1,6,"Green","Once every three months ",0,0,0.06,"Yearly average or average of samples obtained during one year ","The higher end of the BAT-AEL range is 7 mg/Nm3 in the following cases: plants fitted with wet FGD with a downstream gas-gas heater; plants operated < 1 500 h/yr; FBC boilers. For plants operated < 500 h/yr, these levels are indicative.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Coal and/or lignite ","< 100 MWth","Unspecified","Air","Hydrogen fluoride (as F) (Ecological - Daily Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD; (viii) Combined techniques for NOX and SOX reduction; (ix) Replacement or removal of the gas- gas heater located downstream of the wet FGD; (x) Fuel choice","mg/Nm3",1,6,"Green","Once every three months ",0,0,0.06,"Yearly average or average of samples obtained during one year ","The higher end of the BAT-AEL range is 7 mg/Nm3 in the following cases: plants fitted with wet FGD with a downstream gas-gas heater; plants operated < 1 500 h/yr; FBC boilers. For plants operated < 500 h/yr, these levels are indicative."]
["LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Solid biomass and/or peat","< 100 MWth","Unspecified","Air","Hydrogen fluoride (as F) (Ecological - Daily Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3","N/A","1.5","Green","Once every year",0,0,0.06,"Average over sampling period ","For plants operated < 500 h/yr, these levels are indicative.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Solid biomass and/or peat","< 100 MWth","Unspecified","Air","Hydrogen fluoride (as F) (Ecological - Daily Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3","N/A","1.5","Green","Once every year",0,0,0.06,"Average over sampling period ","For plants operated < 500 h/yr, these levels are indicative."]
["LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Solid biomass and/or peat","≥ 300 MWth","Unspecified","Air","Hydrogen fluoride (as F) (Ecological - Daily Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3","N/A","1","Green","Once every year",0,0,0.06,"Average over sampling period ","For plants operated < 500 h/yr, these levels are indicative.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Solid biomass and/or peat","≥ 300 MWth","Unspecified","Air","Hydrogen fluoride (as F) (Ecological - Daily Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3","N/A","1","Green","Once every year",0,0,0.06,"Average over sampling period ","For plants operated < 500 h/yr, these levels are indicative."]
["LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Solid biomass and/or peat","100-300 MWth","Unspecified","Air","Hydrogen fluoride (as F) (Ecological - Daily Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3","N/A","1","Green","Once every year",0,0,0.06,"Average over sampling period ","For plants operated < 500 h/yr, these levels are indicative.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Solid biomass and/or peat","100-300 MWth","Unspecified","Air","Hydrogen fluoride (as F) (Ecological - Daily Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3","N/A","1","Green","Once every year",0,0,0.06,"Average over sampling period ","For plants operated < 500 h/yr, these levels are indicative."]
["LCP","1. Energy industries","Unspecified","Unspecified","All","New","Coal and/or lignite ","< 100 MWth","Unspecified","Air","Hydrogen fluoride (as F) (Ecological - Daily Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD; (viii) Combined techniques for NOX and SOX reduction; (ix) Replacement or removal of the gas- gas heater located downstream of the wet FGD; (x) Fuel choice","mg/Nm3",1,3,"Green","Once every three months ",0,0,0.06,"Yearly average or average of samples obtained during one year ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","New","Coal and/or lignite ","< 100 MWth","Unspecified","Air","Hydrogen fluoride (as F) (Ecological - Daily Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD; (viii) Combined techniques for NOX and SOX reduction; (ix) Replacement or removal of the gas- gas heater located downstream of the wet FGD; (x) Fuel choice","mg/Nm3",1,3,"Green","Once every three months ",0,0,0.06,"Yearly average or average of samples obtained during one year ",0]
["LCP","1. Energy industries","Unspecified","Unspecified","All","New","Coal and/or lignite ","≥ 100 MWth","Unspecified","Air","Hydrogen fluoride (as F) (Ecological - Daily Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD; (viii) Combined techniques for NOX and SOX reduction; (ix) Replacement or removal of the gas- gas heater located downstream of the wet FGD; (x) Fuel choice","mg/Nm3",1,2,"Green","Once every three months ",0,0,0.06,"Yearly average or average of samples obtained during one year ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","New","Coal and/or lignite ","≥ 100 MWth","Unspecified","Air","Hydrogen fluoride (as F) (Ecological - Daily Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD; (viii) Combined techniques for NOX and SOX reduction; (ix) Replacement or removal of the gas- gas heater located downstream of the wet FGD; (x) Fuel choice","mg/Nm3",1,2,"Green","Once every three months ",0,0,0.06,"Yearly average or average of samples obtained during one year ",0]
["LCP","1. Energy industries","Unspecified","Unspecified","All","New","Solid biomass and/or peat","< 100 MWth","Unspecified","Air","Hydrogen fluoride (as F) (Ecological - Daily Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3","N/A","1","Green","Once every year",0,0,0.06,"Average over sampling period ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","New","Solid biomass and/or peat","< 100 MWth","Unspecified","Air","Hydrogen fluoride (as F) (Ecological - Daily Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3","N/A","1","Green","Once every year",0,0,0.06,"Average over sampling period ",0]
["LCP","1. Energy industries","Unspecified","Unspecified","All","New","Solid biomass and/or peat","≥ 300 MWth","Unspecified","Air","Hydrogen fluoride (as F) (Ecological - Daily Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3","N/A","1","Green","Once every year",0,0,0.06,"Average over sampling period ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","New","Solid biomass and/or peat","≥ 300 MWth","Unspecified","Air","Hydrogen fluoride (as F) (Ecological - Daily Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3","N/A","1","Green","Once every year",0,0,0.06,"Average over sampling period ",0]
["LCP","1. Energy industries","Unspecified","Unspecified","All","New","Solid biomass and/or peat","100-300 MWth","Unspecified","Air","Hydrogen fluoride (as F) (Ecological - Daily Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3","N/A","1","Green","Once every year",0,0,0.06,"Average over sampling period ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","New","Solid biomass and/or peat","100-300 MWth","Unspecified","Air","Hydrogen fluoride (as F) (Ecological - Daily Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3","N/A","1","Green","Once every year",0,0,0.06,"Average over sampling period ",0]
["LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Existing","Process fuels from the chemical industry","< 100 MWth","Unspecified","Air","Hydrogen fluoride (as F) (Ecological - Daily Mean)","In order to reduce SOX, HCl and HF emissions to air from the combustion of process fuels from the chemical industry in boilers, BAT is to use one or a combination of the techniques given below: (i) Fuel choice; (ii) Boiler sorbent injection (in-furnace or in-bed); (iii) Duct sorbent injection (DSI); (iv) Spray dry absorber (SDA); (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD Table","mg/Nm3",1,"6","Green","Once every three months ",0,0,0.03,"Average of samples obtained during one year","For plants operated < 500 h/yr, these levels are indicative.\n\nIn the case of plants operated < 1 500 h/yr, the higher end of the BAT-AEL range is 7 mg/Nm3.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Existing","Process fuels from the chemical industry","< 100 MWth","Unspecified","Air","Hydrogen fluoride (as F) (Ecological - Daily Mean)","In order to reduce SOX, HCl and HF emissions to air from the combustion of process fuels from the chemical industry in boilers, BAT is to use one or a combination of the techniques given below: (i) Fuel choice; (ii) Boiler sorbent injection (in-furnace or in-bed); (iii) Duct sorbent injection (DSI); (iv) Spray dry absorber (SDA); (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD Table","mg/Nm3",1,"6","Green","Once every three months ",0,0,0.03,"Average of samples obtained during one year","For plants operated < 500 h/yr, these levels are indicative.\n\nIn the case of plants operated < 1 500 h/yr, the higher end of the BAT-AEL range is 7 mg/Nm3."]
["LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Existing","Process fuels from the chemical industry","≥ 100 MWth","Unspecified","Air","Hydrogen fluoride (as F) (Ecological - Daily Mean)","In order to reduce SOX, HCl and HF emissions to air from the combustion of process fuels from the chemical industry in boilers, BAT is to use one or a combination of the techniques given below: (i) Fuel choice; (ii) Boiler sorbent injection (in-furnace or in-bed); (iii) Duct sorbent injection (DSI); (iv) Spray dry absorber (SDA); (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD Table","mg/Nm3",1,"3","Green","Once every three months ",0,0,0.03,"Average of samples obtained during one year","For plants operated < 500 h/yr, these levels are indicative.\n\nIn the case of plants operated < 1 500 h/yr, the higher end of the BAT-AEL range is 7 mg/Nm3.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Existing","Process fuels from the chemical industry","≥ 100 MWth","Unspecified","Air","Hydrogen fluoride (as F) (Ecological - Daily Mean)","In order to reduce SOX, HCl and HF emissions to air from the combustion of process fuels from the chemical industry in boilers, BAT is to use one or a combination of the techniques given below: (i) Fuel choice; (ii) Boiler sorbent injection (in-furnace or in-bed); (iii) Duct sorbent injection (DSI); (iv) Spray dry absorber (SDA); (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD Table","mg/Nm3",1,"3","Green","Once every three months ",0,0,0.03,"Average of samples obtained during one year","For plants operated < 500 h/yr, these levels are indicative.\n\nIn the case of plants operated < 1 500 h/yr, the higher end of the BAT-AEL range is 7 mg/Nm3."]
["LCP","1. Energy industries","Unspecified","Unspecified","Boilers","New","Process fuels from the chemical industry","< 100 MWth","Unspecified","Air","Hydrogen fluoride (as F) (Ecological - Daily Mean)","In order to reduce SOX, HCl and HF emissions to air from the combustion of process fuels from the chemical industry in boilers, BAT is to use one or a combination of the techniques given below: (i) Fuel choice; (ii) Boiler sorbent injection (in-furnace or in-bed); (iii) Duct sorbent injection (DSI); (iv) Spray dry absorber (SDA); (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD Table","mg/Nm3","N/A","1-3","Green","Once every three months ",0,0,0.03,"Average of samples obtained during one year",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","New","Process fuels from the chemical industry","< 100 MWth","Unspecified","Air","Hydrogen fluoride (as F) (Ecological - Daily Mean)","In order to reduce SOX, HCl and HF emissions to air from the combustion of process fuels from the chemical industry in boilers, BAT is to use one or a combination of the techniques given below: (i) Fuel choice; (ii) Boiler sorbent injection (in-furnace or in-bed); (iii) Duct sorbent injection (DSI); (iv) Spray dry absorber (SDA); (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD Table","mg/Nm3","N/A","1-3","Green","Once every three months ",0,0,0.03,"Average of samples obtained during one year",0]
["LCP","1. Energy industries","Unspecified","Unspecified","Boilers","New","Process fuels from the chemical industry","≥ 100 MWth","Unspecified","Air","Hydrogen fluoride (as F) (Ecological - Daily Mean)","In order to reduce SOX, HCl and HF emissions to air from the combustion of process fuels from the chemical industry in boilers, BAT is to use one or a combination of the techniques given below: (i) Fuel choice; (ii) Boiler sorbent injection (in-furnace or in-bed); (iii) Duct sorbent injection (DSI); (iv) Spray dry absorber (SDA); (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD Table","mg/Nm3",1,"2","Green","Once every three months ",0,0,0.03,"Average of samples obtained during one year",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","New","Process fuels from the chemical industry","≥ 100 MWth","Unspecified","Air","Hydrogen fluoride (as F) (Ecological - Daily Mean)","In order to reduce SOX, HCl and HF emissions to air from the combustion of process fuels from the chemical industry in boilers, BAT is to use one or a combination of the techniques given below: (i) Fuel choice; (ii) Boiler sorbent injection (in-furnace or in-bed); (iii) Duct sorbent injection (DSI); (iv) Spray dry absorber (SDA); (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD Table","mg/Nm3",1,"2","Green","Once every three months ",0,0,0.03,"Average of samples obtained during one year",0]
["LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Coal and/or lignite ","≥ 100 MWth","Unspecified","Air","Hydrogen fluoride (as F) (Ecological - Daily Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD; (viii) Combined techniques for NOX and SOX reduction; (ix) Replacement or removal of the gas- gas heater located downstream of the wet FGD; (x) Fuel choice","mg/Nm3",1,3,"Green","Once every three months ",0,0,0.06,"Yearly average or average of samples obtained during one year ","The higher end of the BAT-AEL range is 7 mg/Nm3 in the following cases: plants fitted with wet FGD with a downstream gas-gas heater; plants operated < 1 500 h/yr; FBC boilers. For plants operated < 500 h/yr, these levels are indicative.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Coal and/or lignite ","≥ 100 MWth","Unspecified","Air","Hydrogen fluoride (as F) (Ecological - Daily Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD; (viii) Combined techniques for NOX and SOX reduction; (ix) Replacement or removal of the gas- gas heater located downstream of the wet FGD; (x) Fuel choice","mg/Nm3",1,3,"Green","Once every three months ",0,0,0.06,"Yearly average or average of samples obtained during one year ","The higher end of the BAT-AEL range is 7 mg/Nm3 in the following cases: plants fitted with wet FGD with a downstream gas-gas heater; plants operated < 1 500 h/yr; FBC boilers. For plants operated < 500 h/yr, these levels are indicative."]
["LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Coal","< 300 MWth ","Unspecified","Air","Mercury and compounds, except mercury alkyls, (as","In order to prevent or reduce mercury emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Dry or semi-dry FGD system; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Selective catalytic reduction (SCR); (vi) Carbon sorbent (e.g. activated carbon or halogenated activated carbon) injection in the flue- gas; (vii) Use of halogenated additives in the fuel or injected in the furnace; (viii) Fuel pretreatment; (ix) Fuel choice ","ug/Nm3",1,"9","Green","Once every three months ",0,0,0.06,"Yearly average or average of samples obtained during one year ","The lower end of the BAT-AEL range can be achieved with specific mercury abatement techniques.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Coal","< 300 MWth ","Unspecified","Air","Mercury and compounds, except mercury alkyls, (as","In order to prevent or reduce mercury emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Dry or semi-dry FGD system; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Selective catalytic reduction (SCR); (vi) Carbon sorbent (e.g. activated carbon or halogenated activated carbon) injection in the flue- gas; (vii) Use of halogenated additives in the fuel or injected in the furnace; (viii) Fuel pretreatment; (ix) Fuel choice ","ug/Nm3",1,"9","Green","Once every three months ",0,0,0.06,"Yearly average or average of samples obtained during one year ","The lower end of the BAT-AEL range can be achieved with specific mercury abatement techniques."]
["LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Coal","≥ 300 MWth","Unspecified","Air","Mercury and compounds, except mercury alkyls, (as","In order to prevent or reduce mercury emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Dry or semi-dry FGD system; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Selective catalytic reduction (SCR); (vi) Carbon sorbent (e.g. activated carbon or halogenated activated carbon) injection in the flue- gas; (vii) Use of halogenated additives in the fuel or injected in the furnace; (viii) Fuel pretreatment; (ix) Fuel choice ","ug/Nm3",1,"4","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ","The lower end of the BAT-AEL range can be achieved with specific mercury abatement techniques.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Coal","≥ 300 MWth","Unspecified","Air","Mercury and compounds, except mercury alkyls, (as","In order to prevent or reduce mercury emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Dry or semi-dry FGD system; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Selective catalytic reduction (SCR); (vi) Carbon sorbent (e.g. activated carbon or halogenated activated carbon) injection in the flue- gas; (vii) Use of halogenated additives in the fuel or injected in the furnace; (viii) Fuel pretreatment; (ix) Fuel choice ","ug/Nm3",1,"4","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ","The lower end of the BAT-AEL range can be achieved with specific mercury abatement techniques."]
["LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Lignite","< 300 MWth ","Unspecified","Air","Mercury and compounds, except mercury alkyls, (as","In order to prevent or reduce mercury emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Dry or semi-dry FGD system; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Selective catalytic reduction (SCR); (vi) Carbon sorbent (e.g. activated carbon or halogenated activated carbon) injection in the flue- gas; (vii) Use of halogenated additives in the fuel or injected in the furnace; (viii) Fuel pretreatment; (ix) Fuel choice ","ug/Nm3",1,"10","Green","Once every three months ",0,0,0.06,"Yearly average or average of samples obtained during one year ","The lower end of the BAT-AEL range can be achieved with specific mercury abatement techniques.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Lignite","< 300 MWth ","Unspecified","Air","Mercury and compounds, except mercury alkyls, (as","In order to prevent or reduce mercury emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Dry or semi-dry FGD system; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Selective catalytic reduction (SCR); (vi) Carbon sorbent (e.g. activated carbon or halogenated activated carbon) injection in the flue- gas; (vii) Use of halogenated additives in the fuel or injected in the furnace; (viii) Fuel pretreatment; (ix) Fuel choice ","ug/Nm3",1,"10","Green","Once every three months ",0,0,0.06,"Yearly average or average of samples obtained during one year ","The lower end of the BAT-AEL range can be achieved with specific mercury abatement techniques."]
["LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Lignite","≥ 300 MWth","Unspecified","Air","Mercury and compounds, except mercury alkyls, (as","In order to prevent or reduce mercury emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Dry or semi-dry FGD system; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Selective catalytic reduction (SCR); (vi) Carbon sorbent (e.g. activated carbon or halogenated activated carbon) injection in the flue- gas; (vii) Use of halogenated additives in the fuel or injected in the furnace; (viii) Fuel pretreatment; (ix) Fuel choice ","ug/Nm3",1,"7","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ","The lower end of the BAT-AEL range can be achieved with specific mercury abatement techniques.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Lignite","≥ 300 MWth","Unspecified","Air","Mercury and compounds, except mercury alkyls, (as","In order to prevent or reduce mercury emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Dry or semi-dry FGD system; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Selective catalytic reduction (SCR); (vi) Carbon sorbent (e.g. activated carbon or halogenated activated carbon) injection in the flue- gas; (vii) Use of halogenated additives in the fuel or injected in the furnace; (viii) Fuel pretreatment; (ix) Fuel choice ","ug/Nm3",1,"7","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ","The lower end of the BAT-AEL range can be achieved with specific mercury abatement techniques."]
["LCP","1. Energy industries","Unspecified","Unspecified","All","New","Coal","< 300 MWth ","Unspecified","Air","Mercury and compounds, except mercury alkyls, (as","In order to prevent or reduce mercury emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Dry or semi-dry FGD system; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Selective catalytic reduction (SCR); (vi) Carbon sorbent (e.g. activated carbon or halogenated activated carbon) injection in the flue- gas; (vii) Use of halogenated additives in the fuel or injected in the furnace; (viii) Fuel pretreatment; (ix) Fuel choice ","ug/Nm3",1,"3","Green","Once every three months ",0,0,0.06,"Yearly average or average of samples obtained during one year ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","New","Coal","< 300 MWth ","Unspecified","Air","Mercury and compounds, except mercury alkyls, (as","In order to prevent or reduce mercury emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Dry or semi-dry FGD system; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Selective catalytic reduction (SCR); (vi) Carbon sorbent (e.g. activated carbon or halogenated activated carbon) injection in the flue- gas; (vii) Use of halogenated additives in the fuel or injected in the furnace; (viii) Fuel pretreatment; (ix) Fuel choice ","ug/Nm3",1,"3","Green","Once every three months ",0,0,0.06,"Yearly average or average of samples obtained during one year ",0]
["LCP","1. Energy industries","Unspecified","Unspecified","All","New","Coal","≥ 300 MWth","Unspecified","Air","Mercury and compounds, except mercury alkyls, (as","In order to prevent or reduce mercury emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Dry or semi-dry FGD system; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Selective catalytic reduction (SCR); (vi) Carbon sorbent (e.g. activated carbon or halogenated activated carbon) injection in the flue- gas; (vii) Use of halogenated additives in the fuel or injected in the furnace; (viii) Fuel pretreatment; (ix) Fuel choice ","ug/Nm3",1,"2","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","New","Coal","≥ 300 MWth","Unspecified","Air","Mercury and compounds, except mercury alkyls, (as","In order to prevent or reduce mercury emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Dry or semi-dry FGD system; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Selective catalytic reduction (SCR); (vi) Carbon sorbent (e.g. activated carbon or halogenated activated carbon) injection in the flue- gas; (vii) Use of halogenated additives in the fuel or injected in the furnace; (viii) Fuel pretreatment; (ix) Fuel choice ","ug/Nm3",1,"2","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ",0]
["LCP","1. Energy industries","Unspecified","Unspecified","All","New","Lignite","< 300 MWth ","Unspecified","Air","Mercury and compounds, except mercury alkyls, (as","In order to prevent or reduce mercury emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Dry or semi-dry FGD system; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Selective catalytic reduction (SCR); (vi) Carbon sorbent (e.g. activated carbon or halogenated activated carbon) injection in the flue- gas; (vii) Use of halogenated additives in the fuel or injected in the furnace; (viii) Fuel pretreatment; (ix) Fuel choice ","ug/Nm3",1,"5","Green","Once every three months ",0,0,0.06,"Yearly average or average of samples obtained during one year ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","New","Lignite","< 300 MWth ","Unspecified","Air","Mercury and compounds, except mercury alkyls, (as","In order to prevent or reduce mercury emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Dry or semi-dry FGD system; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Selective catalytic reduction (SCR); (vi) Carbon sorbent (e.g. activated carbon or halogenated activated carbon) injection in the flue- gas; (vii) Use of halogenated additives in the fuel or injected in the furnace; (viii) Fuel pretreatment; (ix) Fuel choice ","ug/Nm3",1,"5","Green","Once every three months ",0,0,0.06,"Yearly average or average of samples obtained during one year ",0]
["LCP","1. Energy industries","Unspecified","Unspecified","All","New","Lignite","≥ 300 MWth","Unspecified","Air","Mercury and compounds, except mercury alkyls, (as","In order to prevent or reduce mercury emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Dry or semi-dry FGD system; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Selective catalytic reduction (SCR); (vi) Carbon sorbent (e.g. activated carbon or halogenated activated carbon) injection in the flue- gas; (vii) Use of halogenated additives in the fuel or injected in the furnace; (viii) Fuel pretreatment; (ix) Fuel choice ","ug/Nm3",1,"4","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","New","Lignite","≥ 300 MWth","Unspecified","Air","Mercury and compounds, except mercury alkyls, (as","In order to prevent or reduce mercury emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Bag filter; (iii) Dry or semi-dry FGD system; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Selective catalytic reduction (SCR); (vi) Carbon sorbent (e.g. activated carbon or halogenated activated carbon) injection in the flue- gas; (vii) Use of halogenated additives in the fuel or injected in the furnace; (viii) Fuel pretreatment; (ix) Fuel choice ","ug/Nm3",1,"4","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ",0]
["LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Solid biomass and/or peat","Unspecified ","Unspecified","Air","Mercury and compounds, except mercury alkyls, (as","In order to prevent or reduce mercury emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Carbon sorbent (e.g. activated carbon or halogenated activated carbon) injection in the flue- gas; (ii) Use of halogenated additives in the fuel or injected in the furnace; (iii) Fuel choice; (iv) Electrostatic precipitator (ESP); (v) Bag filter; (vi) Dry or semi-dry FGD system; (vii) Wet flue-gas desulphurisation (wet FGD)","ug/Nm3",1,"5","Green","Once every year",0,0,0.06,"Average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Solid biomass and/or peat","Unspecified ","Unspecified","Air","Mercury and compounds, except mercury alkyls, (as","In order to prevent or reduce mercury emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Carbon sorbent (e.g. activated carbon or halogenated activated carbon) injection in the flue- gas; (ii) Use of halogenated additives in the fuel or injected in the furnace; (iii) Fuel choice; (iv) Electrostatic precipitator (ESP); (v) Bag filter; (vi) Dry or semi-dry FGD system; (vii) Wet flue-gas desulphurisation (wet FGD)","ug/Nm3",1,"5","Green","Once every year",0,0,0.06,"Average over the sampling period",0]
["LCP","1. Energy industries","Unspecified","Unspecified","CCGT with a net total fuel utilisation of < 75 %","Existing","Natural gas ","50-600 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",10,"45","Green","Continuous ",0,0,0.15,"Yearly","These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines\n\nIn the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective.\n\nThese BAT-AELs do not apply to existing plants operated < 1 500 h/yr.\n\nOptimising the functioning of an existing technique to reduce NOX emissions further may lead to levels of CO emissions at the higher end of the indicative range for CO emissions given after this table.\n\nThese BAT-AELs do not apply to existing turbines for mechanical drive applications or to plants operated < 500 h/yr.\n\nFor plants with a net electrical efficiency (EE) greater than 55 %, a correction factor may be applied to the higher end of the BAT-AEL range, corresponding to [higher end] × EE/55, where EE is the net electrical efficiency of the plant determined at ISO baseload conditions.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","CCGT with a net total fuel utilisation of < 75 %","Existing","Natural gas ","50-600 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",10,"45","Green","Continuous ",0,0,0.15,"Yearly","These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines\n\nIn the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective.\n\nThese BAT-AELs do not apply to existing plants operated < 1 500 h/yr.\n\nOptimising the functioning of an existing technique to reduce NOX emissions further may lead to levels of CO emissions at the higher end of the indicative range for CO emissions given after this table.\n\nThese BAT-AELs do not apply to existing turbines for mechanical drive applications or to plants operated < 500 h/yr.\n\nFor plants with a net electrical efficiency (EE) greater than 55 %, a correction factor may be applied to the higher end of the BAT-AEL range, corresponding to [higher end] × EE/55, where EE is the net electrical efficiency of the plant determined at ISO baseload conditions."]
["LCP","1. Energy industries","Unspecified","Unspecified","CCGT with a net total fuel utilisation of < 75 %","Existing","Natural gas ","50-600 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",35,"55","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period ","These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines\n\nIn the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective.\n\nThese BAT-AELs do not apply to existing turbines for mechanical drive applications or to plants operated < 500 h/yr.\n\nFor plants with a net electrical efficiency (EE) greater than 55 %, a correction factor may be applied to the higher end of the BAT-AEL range, corresponding to [higher end] × EE/55, where EE is the net electrical efficiency of the plant determined at ISO baseload conditions.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","CCGT with a net total fuel utilisation of < 75 %","Existing","Natural gas ","50-600 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",35,"55","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period ","These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines\n\nIn the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective.\n\nThese BAT-AELs do not apply to existing turbines for mechanical drive applications or to plants operated < 500 h/yr.\n\nFor plants with a net electrical efficiency (EE) greater than 55 %, a correction factor may be applied to the higher end of the BAT-AEL range, corresponding to [higher end] × EE/55, where EE is the net electrical efficiency of the plant determined at ISO baseload conditions."]
["LCP","1. Energy industries","Unspecified","Unspecified","CCGT with a net total fuel utilisation of ≥ 75 %","Existing","Natural gas ","50-600 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",25,"50","Green","Continuous ",0,0,0.15,"Yearly","These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines\n\nIn the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective.\n\nThese BAT-AELs do not apply to existing plants operated < 1 500 h/yr.\n\nOptimising the functioning of an existing technique to reduce NOX emissions further may lead to levels of CO emissions at the higher end of the indicative range for CO emissions given after this table.\n\nThese BAT-AELs do not apply to existing turbines for mechanical drive applications or to plants operated < 500 h/yr.\n\nFor plants with a net electrical efficiency (EE) greater than 55 %, a correction factor may be applied to the higher end of the BAT-AEL range, corresponding to [higher end] × EE/55, where EE is the net electrical efficiency of the plant determined at ISO baseload conditions.\n\nFor existing plants put into operation no later than 7 January 2014, the higher end of the BAT-AEL range is 55 mg/Nm3.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","CCGT with a net total fuel utilisation of ≥ 75 %","Existing","Natural gas ","50-600 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",25,"50","Green","Continuous ",0,0,0.15,"Yearly","These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines\n\nIn the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective.\n\nThese BAT-AELs do not apply to existing plants operated < 1 500 h/yr.\n\nOptimising the functioning of an existing technique to reduce NOX emissions further may lead to levels of CO emissions at the higher end of the indicative range for CO emissions given after this table.\n\nThese BAT-AELs do not apply to existing turbines for mechanical drive applications or to plants operated < 500 h/yr.\n\nFor plants with a net electrical efficiency (EE) greater than 55 %, a correction factor may be applied to the higher end of the BAT-AEL range, corresponding to [higher end] × EE/55, where EE is the net electrical efficiency of the plant determined at ISO baseload conditions.\n\nFor existing plants put into operation no later than 7 January 2014, the higher end of the BAT-AEL range is 55 mg/Nm3."]
["LCP","1. Energy industries","Unspecified","Unspecified","CCGT with a net total fuel utilisation of ≥ 75 %","Existing","Natural gas ","50-600 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",35,"55","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period ","These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines\n\nIn the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective.\n\nThese BAT-AELs do not apply to existing turbines for mechanical drive applications or to plants operated < 500 h/yr.\n\nFor plants with a net electrical efficiency (EE) greater than 55 %, a correction factor may be applied to the higher end of the BAT-AEL range, corresponding to [higher end] × EE/55, where EE is the net electrical efficiency of the plant determined at ISO baseload conditions.\n\nFor existing plants put into operation no later than 7 January 2014, the higher end of the BAT-AEL range is 80 mg/Nm3.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","CCGT with a net total fuel utilisation of ≥ 75 %","Existing","Natural gas ","50-600 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",35,"55","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period ","These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines\n\nIn the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective.\n\nThese BAT-AELs do not apply to existing turbines for mechanical drive applications or to plants operated < 500 h/yr.\n\nFor plants with a net electrical efficiency (EE) greater than 55 %, a correction factor may be applied to the higher end of the BAT-AEL range, corresponding to [higher end] × EE/55, where EE is the net electrical efficiency of the plant determined at ISO baseload conditions.\n\nFor existing plants put into operation no later than 7 January 2014, the higher end of the BAT-AEL range is 80 mg/Nm3."]
["LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Coal and/or lignite ","< 100 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Combination of other primary techniques for NOX reduction (e.g. air staging, fuel staging, flue-gas recirculation, low- NOX burners (LNB)); (iii) Selective non- catalytic reduction (SNCR); (iv) Selective catalytic reduction (SCR); (v) Combined techniques for NOX and SOX reduction","mg/Nm3",165,330,"Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ","In the case of coal-fired PC boiler plants put into operation no later than 1 July 1987, which are operated < 1 500 h/yr and for which SCR and/or SNCR is not applicable, the higher end of the range is 340 mg/Nm3.\n\nFor plants operated < 500 h/yr, these levels are indicative.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Coal and/or lignite ","< 100 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Combination of other primary techniques for NOX reduction (e.g. air staging, fuel staging, flue-gas recirculation, low- NOX burners (LNB)); (iii) Selective non- catalytic reduction (SNCR); (iv) Selective catalytic reduction (SCR); (v) Combined techniques for NOX and SOX reduction","mg/Nm3",165,330,"Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ","In the case of coal-fired PC boiler plants put into operation no later than 1 July 1987, which are operated < 1 500 h/yr and for which SCR and/or SNCR is not applicable, the higher end of the range is 340 mg/Nm3.\n\nFor plants operated < 500 h/yr, these levels are indicative."]
["LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Coal and/or lignite ","100-300 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Combination of other primary techniques for NOX reduction (e.g. air staging, fuel staging, flue-gas recirculation, low- NOX burners (LNB)); (iii) Selective non- catalytic reduction (SNCR); (iv) Selective catalytic reduction (SCR); (v) Combined techniques for NOX and SOX reduction","mg/Nm3",155,210,"Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Coal and/or lignite ","100-300 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Combination of other primary techniques for NOX reduction (e.g. air staging, fuel staging, flue-gas recirculation, low- NOX burners (LNB)); (iii) Selective non- catalytic reduction (SNCR); (iv) Selective catalytic reduction (SCR); (v) Combined techniques for NOX and SOX reduction","mg/Nm3",155,210,"Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ",0]
["LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Coal and/or lignite ","< 100 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Combination of other primary techniques for NOX reduction (e.g. air staging, fuel staging, flue-gas recirculation, low- NOX burners (LNB)); (iii) Selective non- catalytic reduction (SNCR); (iv) Selective catalytic reduction (SCR); (v) Combined techniques for NOX and SOX reduction","mg/Nm3",100,270,"Green","Continuous ",0,0,0.06,"Yearly","These BAT-AELs do not apply to plants operated < 1 500 h/yr.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Coal and/or lignite ","< 100 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Combination of other primary techniques for NOX reduction (e.g. air staging, fuel staging, flue-gas recirculation, low- NOX burners (LNB)); (iii) Selective non- catalytic reduction (SNCR); (iv) Selective catalytic reduction (SCR); (v) Combined techniques for NOX and SOX reduction","mg/Nm3",100,270,"Green","Continuous ",0,0,0.06,"Yearly","These BAT-AELs do not apply to plants operated < 1 500 h/yr."]
["LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Coal and/or lignite ","100-300 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Combination of other primary techniques for NOX reduction (e.g. air staging, fuel staging, flue-gas recirculation, low- NOX burners (LNB)); (iii) Selective non- catalytic reduction (SNCR); (iv) Selective catalytic reduction (SCR); (v) Combined techniques for NOX and SOX reduction","mg/Nm3",100,180,"Green","Continuous ",0,0,0.06,"Yearly",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Coal and/or lignite ","100-300 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Combination of other primary techniques for NOX reduction (e.g. air staging, fuel staging, flue-gas recirculation, low- NOX burners (LNB)); (iii) Selective non- catalytic reduction (SNCR); (iv) Selective catalytic reduction (SCR); (v) Combined techniques for NOX and SOX reduction","mg/Nm3",100,180,"Green","Continuous ",0,0,0.06,"Yearly",0]
["LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Solid biomass and/or peat","≥ 300 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Low-NOX burners (LNB); (iii) Air staging; (iv) Fuel staging, (v) Flue-gas recirculation; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR)","mg/Nm3",40,"150","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ","The higher end of the BAT-AEL range is 160 mg/Nm3 for plants put into operation no later than 7 January 2014.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Solid biomass and/or peat","≥ 300 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Low-NOX burners (LNB); (iii) Air staging; (iv) Fuel staging, (v) Flue-gas recirculation; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR)","mg/Nm3",40,"150","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ","The higher end of the BAT-AEL range is 160 mg/Nm3 for plants put into operation no later than 7 January 2014."]
["LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Solid biomass and/or peat","≥ 300 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Low-NOX burners (LNB); (iii) Air staging; (iv) Fuel staging, (v) Flue-gas recirculation; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR)","mg/Nm3",95,"165","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ","The higher end of the BAT-AEL range is 200 mg/Nm3 for plants put into operation no later than 7 January 2014.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Solid biomass and/or peat","≥ 300 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Low-NOX burners (LNB); (iii) Air staging; (iv) Fuel staging, (v) Flue-gas recirculation; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR)","mg/Nm3",95,"165","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ","The higher end of the BAT-AEL range is 200 mg/Nm3 for plants put into operation no later than 7 January 2014."]
["LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Solid biomass and/or peat","100-300 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Low-NOX burners (LNB); (iii) Air staging; (iv) Fuel staging, (v) Flue-gas recirculation; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR)","mg/Nm3",50,"180","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Solid biomass and/or peat","100-300 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Low-NOX burners (LNB); (iii) Air staging; (iv) Fuel staging, (v) Flue-gas recirculation; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR)","mg/Nm3",50,"180","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ",0]
["LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Solid biomass and/or peat","100-300 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Low-NOX burners (LNB); (iii) Air staging; (iv) Fuel staging, (v) Flue-gas recirculation; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR)","mg/Nm3",100,"220","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Solid biomass and/or peat","100-300 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Low-NOX burners (LNB); (iii) Air staging; (iv) Fuel staging, (v) Flue-gas recirculation; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR)","mg/Nm3",100,"220","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ",0]
["LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Solid biomass and/or peat","50-100 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Low-NOX burners (LNB); (iii) Air staging; (iv) Fuel staging, (v) Flue-gas recirculation; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR)","mg/Nm3",70,"225","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ","For plants burning fuels where the average potassium content is 2 000 mg/kg (dry) or higher, and/or the average sodium content is 300 mg/kg or higher, the higher end of the BAT-AEL range is 250 mg/Nm3.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Solid biomass and/or peat","50-100 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Low-NOX burners (LNB); (iii) Air staging; (iv) Fuel staging, (v) Flue-gas recirculation; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR)","mg/Nm3",70,"225","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ","For plants burning fuels where the average potassium content is 2 000 mg/kg (dry) or higher, and/or the average sodium content is 300 mg/kg or higher, the higher end of the BAT-AEL range is 250 mg/Nm3."]
["LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Solid biomass and/or peat","50-100 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Low-NOX burners (LNB); (iii) Air staging; (iv) Fuel staging, (v) Flue-gas recirculation; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR)","mg/Nm3",120,"275","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ","For plants put into operation no later than 7 January 2014 and burning fuels where the average potassium content is 2 000 mg/kg (dry) or higher, and/or the average sodium content is 300 mg/kg or higher, the higher end of the BAT-AEL range is 310 mg/Nm3.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Solid biomass and/or peat","50-100 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Low-NOX burners (LNB); (iii) Air staging; (iv) Fuel staging, (v) Flue-gas recirculation; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR)","mg/Nm3",120,"275","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ","For plants put into operation no later than 7 January 2014 and burning fuels where the average potassium content is 2 000 mg/kg (dry) or higher, and/or the average sodium content is 300 mg/kg or higher, the higher end of the BAT-AEL range is 310 mg/Nm3."]
["LCP","1. Energy industries","Unspecified","Unspecified","All","New","Coal and/or lignite ","< 100 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Combination of other primary techniques for NOX reduction (e.g. air staging, fuel staging, flue-gas recirculation, low- NOX burners (LNB)); (iii) Selective non- catalytic reduction (SNCR); (iv) Selective catalytic reduction (SCR); (v) Combined techniques for NOX and SOX reduction","mg/Nm3",100,150,"Green","Continuous ",0,0,0.06,"Yearly",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","New","Coal and/or lignite ","< 100 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Combination of other primary techniques for NOX reduction (e.g. air staging, fuel staging, flue-gas recirculation, low- NOX burners (LNB)); (iii) Selective non- catalytic reduction (SNCR); (iv) Selective catalytic reduction (SCR); (v) Combined techniques for NOX and SOX reduction","mg/Nm3",100,150,"Green","Continuous ",0,0,0.06,"Yearly",0]
["LCP","1. Energy industries","Unspecified","Unspecified","All","New","Coal and/or lignite ","< 100 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Combination of other primary techniques for NOX reduction (e.g. air staging, fuel staging, flue-gas recirculation, low- NOX burners (LNB)); (iii) Selective non- catalytic reduction (SNCR); (iv) Selective catalytic reduction (SCR); (v) Combined techniques for NOX and SOX reduction","mg/Nm3",155,200,"Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","New","Coal and/or lignite ","< 100 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Combination of other primary techniques for NOX reduction (e.g. air staging, fuel staging, flue-gas recirculation, low- NOX burners (LNB)); (iii) Selective non- catalytic reduction (SNCR); (iv) Selective catalytic reduction (SCR); (v) Combined techniques for NOX and SOX reduction","mg/Nm3",155,200,"Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ",0]
["LCP","1. Energy industries","Unspecified","Unspecified","All","New","Coal and/or lignite ","100-300 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Combination of other primary techniques for NOX reduction (e.g. air staging, fuel staging, flue-gas recirculation, low- NOX burners (LNB)); (iii) Selective non- catalytic reduction (SNCR); (iv) Selective catalytic reduction (SCR); (v) Combined techniques for NOX and SOX reduction","mg/Nm3",50,100,"Green","Continuous ",0,0,0.06,"Yearly",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","New","Coal and/or lignite ","100-300 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Combination of other primary techniques for NOX reduction (e.g. air staging, fuel staging, flue-gas recirculation, low- NOX burners (LNB)); (iii) Selective non- catalytic reduction (SNCR); (iv) Selective catalytic reduction (SCR); (v) Combined techniques for NOX and SOX reduction","mg/Nm3",50,100,"Green","Continuous ",0,0,0.06,"Yearly",0]
["LCP","1. Energy industries","Unspecified","Unspecified","All","New","Coal and/or lignite ","100-300 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Combination of other primary techniques for NOX reduction (e.g. air staging, fuel staging, flue-gas recirculation, low- NOX burners (LNB)); (iii) Selective non- catalytic reduction (SNCR); (iv) Selective catalytic reduction (SCR); (v) Combined techniques for NOX and SOX reduction","mg/Nm3",80,130,"Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","New","Coal and/or lignite ","100-300 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Combination of other primary techniques for NOX reduction (e.g. air staging, fuel staging, flue-gas recirculation, low- NOX burners (LNB)); (iii) Selective non- catalytic reduction (SNCR); (iv) Selective catalytic reduction (SCR); (v) Combined techniques for NOX and SOX reduction","mg/Nm3",80,130,"Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ",0]
["LCP","1. Energy industries","Unspecified","Unspecified","All","New","Solid biomass and/or peat","≥ 300 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Low-NOX burners (LNB); (iii) Air staging; (iv) Fuel staging, (v) Flue-gas recirculation; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR)","mg/Nm3",40,"140","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","New","Solid biomass and/or peat","≥ 300 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Low-NOX burners (LNB); (iii) Air staging; (iv) Fuel staging, (v) Flue-gas recirculation; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR)","mg/Nm3",40,"140","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ",0]
["LCP","1. Energy industries","Unspecified","Unspecified","All","New","Solid biomass and/or peat","≥ 300 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Low-NOX burners (LNB); (iii) Air staging; (iv) Fuel staging, (v) Flue-gas recirculation; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR)","mg/Nm3",65,"150","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","New","Solid biomass and/or peat","≥ 300 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Low-NOX burners (LNB); (iii) Air staging; (iv) Fuel staging, (v) Flue-gas recirculation; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR)","mg/Nm3",65,"150","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ",0]
["LCP","1. Energy industries","Unspecified","Unspecified","All","New","Solid biomass and/or peat","100-300 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Low-NOX burners (LNB); (iii) Air staging; (iv) Fuel staging, (v) Flue-gas recirculation; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR)","mg/Nm3",50,"140","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","New","Solid biomass and/or peat","100-300 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Low-NOX burners (LNB); (iii) Air staging; (iv) Fuel staging, (v) Flue-gas recirculation; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR)","mg/Nm3",50,"140","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ",0]
["LCP","1. Energy industries","Unspecified","Unspecified","All","New","Solid biomass and/or peat","100-300 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Low-NOX burners (LNB); (iii) Air staging; (iv) Fuel staging, (v) Flue-gas recirculation; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR)","mg/Nm3",100,"200","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","New","Solid biomass and/or peat","100-300 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Low-NOX burners (LNB); (iii) Air staging; (iv) Fuel staging, (v) Flue-gas recirculation; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR)","mg/Nm3",100,"200","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ",0]
["LCP","1. Energy industries","Unspecified","Unspecified","All","New","Solid biomass and/or peat","50-100 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Low-NOX burners (LNB); (iii) Air staging; (iv) Fuel staging, (v) Flue-gas recirculation; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR)","mg/Nm3",70,"150","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ","For plants burning fuels where the average potassium content is 2 000 mg/kg (dry) or higher, and/or the average sodium content is 300 mg/kg or higher, the higher end of the BAT-AEL range is 200 mg/Nm3.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","New","Solid biomass and/or peat","50-100 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Low-NOX burners (LNB); (iii) Air staging; (iv) Fuel staging, (v) Flue-gas recirculation; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR)","mg/Nm3",70,"150","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ","For plants burning fuels where the average potassium content is 2 000 mg/kg (dry) or higher, and/or the average sodium content is 300 mg/kg or higher, the higher end of the BAT-AEL range is 200 mg/Nm3."]
["LCP","1. Energy industries","Unspecified","Unspecified","All","New","Solid biomass and/or peat","50-100 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Low-NOX burners (LNB); (iii) Air staging; (iv) Fuel staging, (v) Flue-gas recirculation; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR)","mg/Nm3",120,"200","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ","For plants burning fuels where the average potassium content is 2 000 mg/kg (dry) or higher, and/or the average sodium content is 300 mg/kg or higher, the higher end of the BAT-AEL range is 260 mg/Nm3.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","New","Solid biomass and/or peat","50-100 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Low-NOX burners (LNB); (iii) Air staging; (iv) Fuel staging, (v) Flue-gas recirculation; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR)","mg/Nm3",120,"200","Green","Continuous ",0,0,0.06,"Yearly average or average of samples obtained during one year ","For plants burning fuels where the average potassium content is 2 000 mg/kg (dry) or higher, and/or the average sodium content is 300 mg/kg or higher, the higher end of the BAT-AEL range is 260 mg/Nm3."]
["LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Existing","100% iron and steel process gases ","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of iron and steel process gases in CCGTs, BAT is to use one or a combination of the techniques given below: (i) Process gas management system; (ii) Advanced control system; (iii) Water/steam addition; (iv) Dry low-NOX burners(DLN); (v) Low-NOX burners (LNB); (vi) Selective catalytic reduction (SCR)","mg/Nm3",20,"100","Green","Continuous ",0,0,0.03,"Yearly","Plants combusting a mixture of gases with an equivalent LHV of > 20 MJ/Nm3 are expected to emit at the higher end of the BAT-AEL ranges.\n\nThe lower end of the BAT-AEL range can be achieved when using SCR.\n\nFor plants operated < 1 500 h/yr, these BAT AELs do not apply.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Existing","100% iron and steel process gases ","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of iron and steel process gases in CCGTs, BAT is to use one or a combination of the techniques given below: (i) Process gas management system; (ii) Advanced control system; (iii) Water/steam addition; (iv) Dry low-NOX burners(DLN); (v) Low-NOX burners (LNB); (vi) Selective catalytic reduction (SCR)","mg/Nm3",20,"100","Green","Continuous ",0,0,0.03,"Yearly","Plants combusting a mixture of gases with an equivalent LHV of > 20 MJ/Nm3 are expected to emit at the higher end of the BAT-AEL ranges.\n\nThe lower end of the BAT-AEL range can be achieved when using SCR.\n\nFor plants operated < 1 500 h/yr, these BAT AELs do not apply."]
["LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Existing","100% iron and steel process gases ","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of iron and steel process gases in CCGTs, BAT is to use one or a combination of the techniques given below: (i) Process gas management system; (ii) Advanced control system; (iii) Water/steam addition; (iv) Dry low-NOX burners(DLN); (v) Low-NOX burners (LNB); (vi) Selective catalytic reduction (SCR)","mg/Nm3",22,"110","Green","Continuous ",0,0,0.03,"Daily average or average over sampling period ","Plants combusting a mixture of gases with an equivalent LHV of > 20 MJ/Nm3 are expected to emit at the higher end of the BAT-AEL ranges.\n\nThe lower end of the BAT-AEL range can be achieved when using SCR.\n\nIn the case of plants put into operation no later than 7 January 2014, the higher end of the BAT-AEL range is 160 mg/Nm3. Furthermore, the higher end of the BAT-AEL range may be exceeded when SCR cannot be used and when using a high share of COG (e.g. > 50 %) and/or when combusting COG with a relatively high level of H2. In this case, the higher end of the BAT-AEL range is 220 mg/Nm3.\n\nFor plants operated < 500 h/yr, these levels are indicative.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Existing","100% iron and steel process gases ","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of iron and steel process gases in CCGTs, BAT is to use one or a combination of the techniques given below: (i) Process gas management system; (ii) Advanced control system; (iii) Water/steam addition; (iv) Dry low-NOX burners(DLN); (v) Low-NOX burners (LNB); (vi) Selective catalytic reduction (SCR)","mg/Nm3",22,"110","Green","Continuous ",0,0,0.03,"Daily average or average over sampling period ","Plants combusting a mixture of gases with an equivalent LHV of > 20 MJ/Nm3 are expected to emit at the higher end of the BAT-AEL ranges.\n\nThe lower end of the BAT-AEL range can be achieved when using SCR.\n\nIn the case of plants put into operation no later than 7 January 2014, the higher end of the BAT-AEL range is 160 mg/Nm3. Furthermore, the higher end of the BAT-AEL range may be exceeded when SCR cannot be used and when using a high share of COG (e.g. > 50 %) and/or when combusting COG with a relatively high level of H2. In this case, the higher end of the BAT-AEL range is 220 mg/Nm3.\n\nFor plants operated < 500 h/yr, these levels are indicative."]
["LCP","1. Energy industries","Unspecified","Unspecified","Boilers","New","100% iron and steel process gases ","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of iron and steel process gases in CCGTs, BAT is to use one or a combination of the techniques given below: (i) Process gas management system; (ii) Advanced control system; (iii) Water/steam addition; (iv) Dry low-NOX burners(DLN); (v) Low-NOX burners (LNB); (vi) Selective catalytic reduction (SCR)","mg/Nm3",15,"65","Green","Continuous ",0,0,0.03,"Yearly","Plants combusting a mixture of gases with an equivalent LHV of > 20 MJ/Nm3 are expected to emit at the higher end of the BAT-AEL ranges.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","New","100% iron and steel process gases ","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of iron and steel process gases in CCGTs, BAT is to use one or a combination of the techniques given below: (i) Process gas management system; (ii) Advanced control system; (iii) Water/steam addition; (iv) Dry low-NOX burners(DLN); (v) Low-NOX burners (LNB); (vi) Selective catalytic reduction (SCR)","mg/Nm3",15,"65","Green","Continuous ",0,0,0.03,"Yearly","Plants combusting a mixture of gases with an equivalent LHV of > 20 MJ/Nm3 are expected to emit at the higher end of the BAT-AEL ranges."]
["LCP","1. Energy industries","Unspecified","Unspecified","Boilers","New","100% iron and steel process gases ","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of iron and steel process gases in CCGTs, BAT is to use one or a combination of the techniques given below: (i) Process gas management system; (ii) Advanced control system; (iii) Water/steam addition; (iv) Dry low-NOX burners(DLN); (v) Low-NOX burners (LNB); (vi) Selective catalytic reduction (SCR)","mg/Nm3",22,"100","Green","Continuous ",0,0,0.03,"Daily average or average over sampling period ","Plants combusting a mixture of gases with an equivalent LHV of > 20 MJ/Nm3 are expected to emit at the higher end of the BAT-AEL ranges.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","New","100% iron and steel process gases ","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of iron and steel process gases in CCGTs, BAT is to use one or a combination of the techniques given below: (i) Process gas management system; (ii) Advanced control system; (iii) Water/steam addition; (iv) Dry low-NOX burners(DLN); (v) Low-NOX burners (LNB); (vi) Selective catalytic reduction (SCR)","mg/Nm3",22,"100","Green","Continuous ",0,0,0.03,"Daily average or average over sampling period ","Plants combusting a mixture of gases with an equivalent LHV of > 20 MJ/Nm3 are expected to emit at the higher end of the BAT-AEL ranges."]
["LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Existing","Gases only ","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO emissions to air from the combustion of process fuels from the chemical industry, BAT is to use one or a combination of the techniques given below: (i) Low-NOX burners (LNB); (ii) Air staging; (iii) Fuel staging; (iv) Flue-gas recirculation; (v) Water/steam addition; (vi) Fuel choice; (vii) Advanced control system; (viii) Selective non-catalytic reduction (SNCR); (ix) Selective catalytic reduction (SCR)","mg/Nm3",70,"100","Green","Continuous ",0,0,0.03,"Yearly","For plants operated < 1 500 h/yr, these BAT AELs do not apply.  \n\nFor existing plants put into operation no later than 7 January 2014, the higher end of the BAT-AEL range is 180 mg/Nm3.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Existing","Gases only ","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO emissions to air from the combustion of process fuels from the chemical industry, BAT is to use one or a combination of the techniques given below: (i) Low-NOX burners (LNB); (ii) Air staging; (iii) Fuel staging; (iv) Flue-gas recirculation; (v) Water/steam addition; (vi) Fuel choice; (vii) Advanced control system; (viii) Selective non-catalytic reduction (SNCR); (ix) Selective catalytic reduction (SCR)","mg/Nm3",70,"100","Green","Continuous ",0,0,0.03,"Yearly","For plants operated < 1 500 h/yr, these BAT AELs do not apply.  \n\nFor existing plants put into operation no later than 7 January 2014, the higher end of the BAT-AEL range is 180 mg/Nm3."]
["LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Existing","Gases only ","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO emissions to air from the combustion of process fuels from the chemical industry, BAT is to use one or a combination of the techniques given below: (i) Low-NOX burners (LNB); (ii) Air staging; (iii) Fuel staging; (iv) Flue-gas recirculation; (v) Water/steam addition; (vi) Fuel choice; (vii) Advanced control system; (viii) Selective non-catalytic reduction (SNCR); (ix) Selective catalytic reduction (SCR)","mg/Nm3",85,"110","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ","For plants operated < 500 h/yr, these levels are indicative.\n\nFor existing plants put into operation no later than 7 January 2014, the higher end of the BAT-AEL range is 210 mg/Nm3.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Existing","Gases only ","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO emissions to air from the combustion of process fuels from the chemical industry, BAT is to use one or a combination of the techniques given below: (i) Low-NOX burners (LNB); (ii) Air staging; (iii) Fuel staging; (iv) Flue-gas recirculation; (v) Water/steam addition; (vi) Fuel choice; (vii) Advanced control system; (viii) Selective non-catalytic reduction (SNCR); (ix) Selective catalytic reduction (SCR)","mg/Nm3",85,"110","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ","For plants operated < 500 h/yr, these levels are indicative.\n\nFor existing plants put into operation no later than 7 January 2014, the higher end of the BAT-AEL range is 210 mg/Nm3."]
["LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Existing","HFO and/or gas oil in boilers","< 100 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Air staging; (ii) Fuel staging; (iii) Flue-gas recirculation; (iv) Low-NOX burners (LNB); (v) Water/steam addition; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR); (viii) Advanced control systeml (ix) Fuel choice","mg/Nm3",150,"270","Green","Continuous ",0,0,0.03,"Yearly","These BAT-AELs do not apply to plants operated < 1 500 h/yr.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Existing","HFO and/or gas oil in boilers","< 100 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Air staging; (ii) Fuel staging; (iii) Flue-gas recirculation; (iv) Low-NOX burners (LNB); (v) Water/steam addition; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR); (viii) Advanced control systeml (ix) Fuel choice","mg/Nm3",150,"270","Green","Continuous ",0,0,0.03,"Yearly","These BAT-AELs do not apply to plants operated < 1 500 h/yr."]
["LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Existing","HFO and/or gas oil in boilers","< 100 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Air staging; (ii) Fuel staging; (iii) Flue-gas recirculation; (iv) Low-NOX burners (LNB); (v) Water/steam addition; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR); (viii) Advanced control systeml (ix) Fuel choice","mg/Nm3",210,"330","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ","For plants operated < 500 h/yr, these levels are indicative.\n\nFor industrial boilers and district heating plants put into operation no later than 27 November 2003, which are operated < 1 500 h/yr and for which SCR and/or SNCR is not applicable, the higher end of the BAT-AEL range is 450 mg/Nm3.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Existing","HFO and/or gas oil in boilers","< 100 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Air staging; (ii) Fuel staging; (iii) Flue-gas recirculation; (iv) Low-NOX burners (LNB); (v) Water/steam addition; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR); (viii) Advanced control systeml (ix) Fuel choice","mg/Nm3",210,"330","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ","For plants operated < 500 h/yr, these levels are indicative.\n\nFor industrial boilers and district heating plants put into operation no later than 27 November 2003, which are operated < 1 500 h/yr and for which SCR and/or SNCR is not applicable, the higher end of the BAT-AEL range is 450 mg/Nm3."]
["LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Existing","HFO and/or gas oil in boilers","≥ 100 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Air staging; (ii) Fuel staging; (iii) Flue-gas recirculation; (iv) Low-NOX burners (LNB); (v) Water/steam addition; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR); (viii) Advanced control systeml (ix) Fuel choice","mg/Nm3",45,"100","Green","Continuous ",0,0,0.03,"Yearly","The higher end of the BAT-AEL range is 110 mg/Nm3 for plants of 100–300 MWth and plants of ≥ 300 MWth that were put into operation no later than 7 January 2014.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Existing","HFO and/or gas oil in boilers","≥ 100 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Air staging; (ii) Fuel staging; (iii) Flue-gas recirculation; (iv) Low-NOX burners (LNB); (v) Water/steam addition; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR); (viii) Advanced control systeml (ix) Fuel choice","mg/Nm3",45,"100","Green","Continuous ",0,0,0.03,"Yearly","The higher end of the BAT-AEL range is 110 mg/Nm3 for plants of 100–300 MWth and plants of ≥ 300 MWth that were put into operation no later than 7 January 2014."]
["LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Existing","HFO and/or gas oil in boilers","≥ 100 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Air staging; (ii) Fuel staging; (iii) Flue-gas recirculation; (iv) Low-NOX burners (LNB); (v) Water/steam addition; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR); (viii) Advanced control systeml (ix) Fuel choice","mg/Nm3",85,"110","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ","For industrial boilers and district heating plants of > 100 MWth put into operation no later than 27 November 2003, which are operated < 1 500 h/yr and for which SCR and/or SNCR is not applicable, the higher end of the BAT-AEL range is 365 mg/Nm3.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Existing","HFO and/or gas oil in boilers","≥ 100 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Air staging; (ii) Fuel staging; (iii) Flue-gas recirculation; (iv) Low-NOX burners (LNB); (v) Water/steam addition; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR); (viii) Advanced control systeml (ix) Fuel choice","mg/Nm3",85,"110","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ","For industrial boilers and district heating plants of > 100 MWth put into operation no later than 27 November 2003, which are operated < 1 500 h/yr and for which SCR and/or SNCR is not applicable, the higher end of the BAT-AEL range is 365 mg/Nm3."]
["LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Existing","Mixture of gases and liquids","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO emissions to air from the combustion of process fuels from the chemical industry, BAT is to use one or a combination of the techniques given below: (i) Low-NOX burners (LNB); (ii) Air staging; (iii) Fuel staging; (iv) Flue-gas recirculation; (v) Water/steam addition; (vi) Fuel choice; (vii) Advanced control system; (viii) Selective non-catalytic reduction (SNCR); (ix) Selective catalytic reduction (SCR)","mg/Nm3",80,"290","Green","Continuous ",0,0,0.03,"Yearly","For plants operated < 1 500 h/yr, these BAT AELs do not apply.\n\nFor existing plants of ≤ 500 MWth put into operation no later than 27 November 2003 using liquid fuels with a nitrogen content higher than 0,6 wt-%, the higher end of the BAT-AEL range is 380 mg/Nm3.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Existing","Mixture of gases and liquids","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO emissions to air from the combustion of process fuels from the chemical industry, BAT is to use one or a combination of the techniques given below: (i) Low-NOX burners (LNB); (ii) Air staging; (iii) Fuel staging; (iv) Flue-gas recirculation; (v) Water/steam addition; (vi) Fuel choice; (vii) Advanced control system; (viii) Selective non-catalytic reduction (SNCR); (ix) Selective catalytic reduction (SCR)","mg/Nm3",80,"290","Green","Continuous ",0,0,0.03,"Yearly","For plants operated < 1 500 h/yr, these BAT AELs do not apply.\n\nFor existing plants of ≤ 500 MWth put into operation no later than 27 November 2003 using liquid fuels with a nitrogen content higher than 0,6 wt-%, the higher end of the BAT-AEL range is 380 mg/Nm3."]
["LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Existing","Mixture of gases and liquids","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO emissions to air from the combustion of process fuels from the chemical industry, BAT is to use one or a combination of the techniques given below: (i) Low-NOX burners (LNB); (ii) Air staging; (iii) Fuel staging; (iv) Flue-gas recirculation; (v) Water/steam addition; (vi) Fuel choice; (vii) Advanced control system; (viii) Selective non-catalytic reduction (SNCR); (ix) Selective catalytic reduction (SCR)","mg/Nm3",100,"330","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ","For plants operated < 500 h/yr, these levels are indicative. \n\nFor existing plants of ≤ 500 MWth put into operation no later than 27 November 2003 using liquid fuels with a nitrogen content higher than 0,6 wt-%, the higher end of the BAT-AEL range is 380 mg/Nm3.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Existing","Mixture of gases and liquids","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO emissions to air from the combustion of process fuels from the chemical industry, BAT is to use one or a combination of the techniques given below: (i) Low-NOX burners (LNB); (ii) Air staging; (iii) Fuel staging; (iv) Flue-gas recirculation; (v) Water/steam addition; (vi) Fuel choice; (vii) Advanced control system; (viii) Selective non-catalytic reduction (SNCR); (ix) Selective catalytic reduction (SCR)","mg/Nm3",100,"330","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ","For plants operated < 500 h/yr, these levels are indicative. \n\nFor existing plants of ≤ 500 MWth put into operation no later than 27 November 2003 using liquid fuels with a nitrogen content higher than 0,6 wt-%, the higher end of the BAT-AEL range is 380 mg/Nm3."]
["LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Existing","Natural gas ","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",50,"100","Green","Continuous ",0,0,0.15,"Yearly","Optimising the functioning of an existing technique to reduce NOX emissions further may lead to levels of CO emissions at the higher end of the indicative range for CO emissions given after this table.\n\nThese BAT-AELs do not apply to plants operated < 1 500 h/yr.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Existing","Natural gas ","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",50,"100","Green","Continuous ",0,0,0.15,"Yearly","Optimising the functioning of an existing technique to reduce NOX emissions further may lead to levels of CO emissions at the higher end of the indicative range for CO emissions given after this table.\n\nThese BAT-AELs do not apply to plants operated < 1 500 h/yr."]
["LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Existing","Natural gas ","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",85,"110","Green","Continuous ",0,0,0.15,"Daily average or average over sampling period ","For plants operated < 500 h/yr, these levels are indicative.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Existing","Natural gas ","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",85,"110","Green","Continuous ",0,0,0.15,"Daily average or average over sampling period ","For plants operated < 500 h/yr, these levels are indicative."]
["LCP","1. Energy industries","Unspecified","Unspecified","Boilers","New","Gases only ","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO emissions to air from the combustion of process fuels from the chemical industry, BAT is to use one or a combination of the techniques given below: (i) Low-NOX burners (LNB); (ii) Air staging; (iii) Fuel staging; (iv) Flue-gas recirculation; (v) Water/steam addition; (vi) Fuel choice; (vii) Advanced control system; (viii) Selective non-catalytic reduction (SNCR); (ix) Selective catalytic reduction (SCR)","mg/Nm3",20,"80","Green","Continuous ",0,0,0.03,"Yearly",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","New","Gases only ","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO emissions to air from the combustion of process fuels from the chemical industry, BAT is to use one or a combination of the techniques given below: (i) Low-NOX burners (LNB); (ii) Air staging; (iii) Fuel staging; (iv) Flue-gas recirculation; (v) Water/steam addition; (vi) Fuel choice; (vii) Advanced control system; (viii) Selective non-catalytic reduction (SNCR); (ix) Selective catalytic reduction (SCR)","mg/Nm3",20,"80","Green","Continuous ",0,0,0.03,"Yearly",0]
["LCP","1. Energy industries","Unspecified","Unspecified","Boilers","New","Gases only ","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO emissions to air from the combustion of process fuels from the chemical industry, BAT is to use one or a combination of the techniques given below: (i) Low-NOX burners (LNB); (ii) Air staging; (iii) Fuel staging; (iv) Flue-gas recirculation; (v) Water/steam addition; (vi) Fuel choice; (vii) Advanced control system; (viii) Selective non-catalytic reduction (SNCR); (ix) Selective catalytic reduction (SCR)","mg/Nm3",30,"100","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","New","Gases only ","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO emissions to air from the combustion of process fuels from the chemical industry, BAT is to use one or a combination of the techniques given below: (i) Low-NOX burners (LNB); (ii) Air staging; (iii) Fuel staging; (iv) Flue-gas recirculation; (v) Water/steam addition; (vi) Fuel choice; (vii) Advanced control system; (viii) Selective non-catalytic reduction (SNCR); (ix) Selective catalytic reduction (SCR)","mg/Nm3",30,"100","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ",0]
["LCP","1. Energy industries","Unspecified","Unspecified","Boilers","New","HFO and/or gas oil in boilers","< 100 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Air staging; (ii) Fuel staging; (iii) Flue-gas recirculation; (iv) Low-NOX burners (LNB); (v) Water/steam addition; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR); (viii) Advanced control systeml (ix) Fuel choice","mg/Nm3",75,"200","Green","Continuous ",0,0,0.03,"Yearly",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","New","HFO and/or gas oil in boilers","< 100 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Air staging; (ii) Fuel staging; (iii) Flue-gas recirculation; (iv) Low-NOX burners (LNB); (v) Water/steam addition; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR); (viii) Advanced control systeml (ix) Fuel choice","mg/Nm3",75,"200","Green","Continuous ",0,0,0.03,"Yearly",0]
["LCP","1. Energy industries","Unspecified","Unspecified","Boilers","New","HFO and/or gas oil in boilers","≥ 100 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Air staging; (ii) Fuel staging; (iii) Flue-gas recirculation; (iv) Low-NOX burners (LNB); (v) Water/steam addition; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR); (viii) Advanced control systeml (ix) Fuel choice","mg/Nm3",45,"75","Green","Continuous ",0,0,0.03,"Yearly",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","New","HFO and/or gas oil in boilers","≥ 100 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Air staging; (ii) Fuel staging; (iii) Flue-gas recirculation; (iv) Low-NOX burners (LNB); (v) Water/steam addition; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR); (viii) Advanced control systeml (ix) Fuel choice","mg/Nm3",45,"75","Green","Continuous ",0,0,0.03,"Yearly",0]
["LCP","1. Energy industries","Unspecified","Unspecified","Boilers","New","Mixture of gases and liquids","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO emissions to air from the combustion of process fuels from the chemical industry, BAT is to use one or a combination of the techniques given below: (i) Low-NOX burners (LNB); (ii) Air staging; (iii) Fuel staging; (iv) Flue-gas recirculation; (v) Water/steam addition; (vi) Fuel choice; (vii) Advanced control system; (viii) Selective non-catalytic reduction (SNCR); (ix) Selective catalytic reduction (SCR)","mg/Nm3",30,"85","Green","Continuous ",0,0,0.03,"Yearly",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","New","Mixture of gases and liquids","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO emissions to air from the combustion of process fuels from the chemical industry, BAT is to use one or a combination of the techniques given below: (i) Low-NOX burners (LNB); (ii) Air staging; (iii) Fuel staging; (iv) Flue-gas recirculation; (v) Water/steam addition; (vi) Fuel choice; (vii) Advanced control system; (viii) Selective non-catalytic reduction (SNCR); (ix) Selective catalytic reduction (SCR)","mg/Nm3",30,"85","Green","Continuous ",0,0,0.03,"Yearly",0]
["LCP","1. Energy industries","Unspecified","Unspecified","Boilers","New","Mixture of gases and liquids","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO emissions to air from the combustion of process fuels from the chemical industry, BAT is to use one or a combination of the techniques given below: (i) Low-NOX burners (LNB); (ii) Air staging; (iii) Fuel staging; (iv) Flue-gas recirculation; (v) Water/steam addition; (vi) Fuel choice; (vii) Advanced control system; (viii) Selective non-catalytic reduction (SNCR); (ix) Selective catalytic reduction (SCR)","mg/Nm3",50,"110","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","New","Mixture of gases and liquids","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO emissions to air from the combustion of process fuels from the chemical industry, BAT is to use one or a combination of the techniques given below: (i) Low-NOX burners (LNB); (ii) Air staging; (iii) Fuel staging; (iv) Flue-gas recirculation; (v) Water/steam addition; (vi) Fuel choice; (vii) Advanced control system; (viii) Selective non-catalytic reduction (SNCR); (ix) Selective catalytic reduction (SCR)","mg/Nm3",50,"110","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ",0]
["LCP","1. Energy industries","Unspecified","Unspecified","Boilers","New","Natural gas ","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",10,"60","Green","Continuous ",0,0,0.15,"Yearly","Optimising the functioning of an existing technique to reduce NOX emissions further may lead to levels of CO emissions at the higher end of the indicative range for CO emissions given after this table.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","New","Natural gas ","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",10,"60","Green","Continuous ",0,0,0.15,"Yearly","Optimising the functioning of an existing technique to reduce NOX emissions further may lead to levels of CO emissions at the higher end of the indicative range for CO emissions given after this table."]
["LCP","1. Energy industries","Unspecified","Unspecified","Boilers","New","Natural gas ","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",30,"85","Green","Continuous ",0,0,0.15,"Daily average or average over sampling period ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","New","Natural gas ","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",30,"85","Green","Continuous ",0,0,0.15,"Daily average or average over sampling period ",0]
["LCP","1. Energy industries","Unspecified","Unspecified","Boilers","New","HFO and/or gas oil in boilers","< 100 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Air staging; (ii) Fuel staging; (iii) Flue-gas recirculation; (iv) Low-NOX burners (LNB); (v) Water/steam addition; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR); (viii) Advanced control systeml (ix) Fuel choice","mg/Nm3",100,"215","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","New","HFO and/or gas oil in boilers","< 100 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Air staging; (ii) Fuel staging; (iii) Flue-gas recirculation; (iv) Low-NOX burners (LNB); (v) Water/steam addition; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR); (viii) Advanced control systeml (ix) Fuel choice","mg/Nm3",100,"215","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ",0]
["LCP","1. Energy industries","Unspecified","Unspecified","Boilers","New","HFO and/or gas oil in boilers","≥ 100 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Air staging; (ii) Fuel staging; (iii) Flue-gas recirculation; (iv) Low-NOX burners (LNB); (v) Water/steam addition; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR); (viii) Advanced control systeml (ix) Fuel choice","mg/Nm3",85,"100","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ","The higher end of the BAT-AEL range is 145 mg/Nm3 for plants of 100–300 MWth and plants of ≥ 300 MWth that were put into operation no later than 7 January 2014.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","New","HFO and/or gas oil in boilers","≥ 100 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Air staging; (ii) Fuel staging; (iii) Flue-gas recirculation; (iv) Low-NOX burners (LNB); (v) Water/steam addition; (vi) Selective non- catalytic reduction (SNCR); (vii) Selective catalytic reduction (SCR); (viii) Advanced control systeml (ix) Fuel choice","mg/Nm3",85,"100","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ","The higher end of the BAT-AEL range is 145 mg/Nm3 for plants of 100–300 MWth and plants of ≥ 300 MWth that were put into operation no later than 7 January 2014."]
["LCP","1. Energy industries","Unspecified","Unspecified","CCGT","Existing","100% iron and steel process gases ","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of iron and steel process gases in CCGTs, BAT is to use one or a combination of the techniques given below: (i) Process gas management system; (ii) Advanced control system; (iii) Water/steam addition; (iv) Dry low-NOX burners(DLN); (v) Low-NOX burners (LNB); (vi) Selective catalytic reduction (SCR)","mg/Nm3",20,"50","Green","Continuous ",0,0,0.15,"Yearly","Plants combusting a mixture of gases with an equivalent LHV of > 20 MJ/Nm3 are expected to emit at the higher end of the BAT-AEL ranges.\n\nThe lower end of the BAT-AEL range can be achieved when using SCR.\n\nFor plants operated < 1 500 h/yr, these BAT AELs do not apply.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","CCGT","Existing","100% iron and steel process gases ","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of iron and steel process gases in CCGTs, BAT is to use one or a combination of the techniques given below: (i) Process gas management system; (ii) Advanced control system; (iii) Water/steam addition; (iv) Dry low-NOX burners(DLN); (v) Low-NOX burners (LNB); (vi) Selective catalytic reduction (SCR)","mg/Nm3",20,"50","Green","Continuous ",0,0,0.15,"Yearly","Plants combusting a mixture of gases with an equivalent LHV of > 20 MJ/Nm3 are expected to emit at the higher end of the BAT-AEL ranges.\n\nThe lower end of the BAT-AEL range can be achieved when using SCR.\n\nFor plants operated < 1 500 h/yr, these BAT AELs do not apply."]
["LCP","1. Energy industries","Unspecified","Unspecified","CCGT","Existing","100% iron and steel process gases ","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of iron and steel process gases in CCGTs, BAT is to use one or a combination of the techniques given below: (i) Process gas management system; (ii) Advanced control system; (iii) Water/steam addition; (iv) Dry low-NOX burners(DLN); (v) Low-NOX burners (LNB); (vi) Selective catalytic reduction (SCR)","mg/Nm3",30,"55","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period ","Plants combusting a mixture of gases with an equivalent LHV of > 20 MJ/Nm3 are expected to emit at the higher end of the BAT-AEL ranges.\n\nFor plants operated < 500 h/yr, these levels are indicative.\n\nIn the case of plants put into operation no later than 7 January 2014, the higher end of the BAT-AEL range is 70 mg/Nm3.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","CCGT","Existing","100% iron and steel process gases ","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of iron and steel process gases in CCGTs, BAT is to use one or a combination of the techniques given below: (i) Process gas management system; (ii) Advanced control system; (iii) Water/steam addition; (iv) Dry low-NOX burners(DLN); (v) Low-NOX burners (LNB); (vi) Selective catalytic reduction (SCR)","mg/Nm3",30,"55","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period ","Plants combusting a mixture of gases with an equivalent LHV of > 20 MJ/Nm3 are expected to emit at the higher end of the BAT-AEL ranges.\n\nFor plants operated < 500 h/yr, these levels are indicative.\n\nIn the case of plants put into operation no later than 7 January 2014, the higher end of the BAT-AEL range is 70 mg/Nm3."]
["LCP","1. Energy industries","Unspecified","Unspecified","CCGT","New","100% iron and steel process gases ","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of iron and steel process gases in CCGTs, BAT is to use one or a combination of the techniques given below: (i) Process gas management system; (ii) Advanced control system; (iii) Water/steam addition; (iv) Dry low-NOX burners(DLN); (v) Low-NOX burners (LNB); (vi) Selective catalytic reduction (SCR)","mg/Nm3",20,"35","Green","Continuous ",0,0,0.15,"Yearly","Plants combusting a mixture of gases with an equivalent LHV of > 20 MJ/Nm3 are expected to emit at the higher end of the BAT-AEL ranges.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","CCGT","New","100% iron and steel process gases ","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of iron and steel process gases in CCGTs, BAT is to use one or a combination of the techniques given below: (i) Process gas management system; (ii) Advanced control system; (iii) Water/steam addition; (iv) Dry low-NOX burners(DLN); (v) Low-NOX burners (LNB); (vi) Selective catalytic reduction (SCR)","mg/Nm3",20,"35","Green","Continuous ",0,0,0.15,"Yearly","Plants combusting a mixture of gases with an equivalent LHV of > 20 MJ/Nm3 are expected to emit at the higher end of the BAT-AEL ranges."]
["LCP","1. Energy industries","Unspecified","Unspecified","CCGT","New","100% iron and steel process gases ","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of iron and steel process gases in CCGTs, BAT is to use one or a combination of the techniques given below: (i) Process gas management system; (ii) Advanced control system; (iii) Water/steam addition; (iv) Dry low-NOX burners(DLN); (v) Low-NOX burners (LNB); (vi) Selective catalytic reduction (SCR)","mg/Nm3",30,"50","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period ","Plants combusting a mixture of gases with an equivalent LHV of > 20 MJ/Nm3 are expected to emit at the higher end of the BAT-AEL ranges.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","CCGT","New","100% iron and steel process gases ","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of iron and steel process gases in CCGTs, BAT is to use one or a combination of the techniques given below: (i) Process gas management system; (ii) Advanced control system; (iii) Water/steam addition; (iv) Dry low-NOX burners(DLN); (v) Low-NOX burners (LNB); (vi) Selective catalytic reduction (SCR)","mg/Nm3",30,"50","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period ","Plants combusting a mixture of gases with an equivalent LHV of > 20 MJ/Nm3 are expected to emit at the higher end of the BAT-AEL ranges."]
["LCP","1. Energy industries","Unspecified","Unspecified","CCGT","New","Natural gas ","≥ 50 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",10,"30","Green","Continuous ",0,0,0.15,"Yearly","These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines\n\nIn the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective.\n\nThese BAT-AELs do not apply to existing plants operated < 1 500 h/yr.\n\nOptimising the functioning of an existing technique to reduce NOX emissions further may lead to levels of CO emissions at the higher end of the indicative range for CO emissions given after this table.\n\nThese BAT-AELs do not apply to existing turbines for mechanical drive applications or to plants operated < 500 h/yr.\n\nFor plants with a net electrical efficiency (EE) greater than 55 %, a correction factor may be applied to the higher end of the BAT-AEL range, corresponding to [higher end] × EE/55, where EE is the net electrical efficiency of the plant determined at ISO baseload conditions.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","CCGT","New","Natural gas ","≥ 50 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",10,"30","Green","Continuous ",0,0,0.15,"Yearly","These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines\n\nIn the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective.\n\nThese BAT-AELs do not apply to existing plants operated < 1 500 h/yr.\n\nOptimising the functioning of an existing technique to reduce NOX emissions further may lead to levels of CO emissions at the higher end of the indicative range for CO emissions given after this table.\n\nThese BAT-AELs do not apply to existing turbines for mechanical drive applications or to plants operated < 500 h/yr.\n\nFor plants with a net electrical efficiency (EE) greater than 55 %, a correction factor may be applied to the higher end of the BAT-AEL range, corresponding to [higher end] × EE/55, where EE is the net electrical efficiency of the plant determined at ISO baseload conditions."]
["LCP","1. Energy industries","Unspecified","Unspecified","CCGT","New","Natural gas ","≥ 50 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",15,"40","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period ","These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines\n\nIn the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","CCGT","New","Natural gas ","≥ 50 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",15,"40","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period ","These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines\n\nIn the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective."]
["LCP","1. Energy industries","Unspecified","Unspecified","CCGT with a net total fuel utilisation of < 75 %","Existing","Natural gas ","≥ 600 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",10,"40","Green","Continuous ",0,0,0.15,"Yearly","These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines\n\nIn the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective.\n\nThese BAT-AELs do not apply to existing plants operated < 1 500 h/yr.\n\nOptimising the functioning of an existing technique to reduce NOX emissions further may lead to levels of CO emissions at the higher end of the indicative range for CO emissions given after this table.\n\nThese BAT-AELs do not apply to existing turbines for mechanical drive applications or to plants operated < 500 h/yr.\n\nFor plants with a net electrical efficiency (EE) greater than 55 %, a correction factor may be applied to the higher end of the BAT-AEL range, corresponding to [higher end] × EE/55, where EE is the net electrical efficiency of the plant determined at ISO baseload conditions.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","CCGT with a net total fuel utilisation of < 75 %","Existing","Natural gas ","≥ 600 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",10,"40","Green","Continuous ",0,0,0.15,"Yearly","These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines\n\nIn the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective.\n\nThese BAT-AELs do not apply to existing plants operated < 1 500 h/yr.\n\nOptimising the functioning of an existing technique to reduce NOX emissions further may lead to levels of CO emissions at the higher end of the indicative range for CO emissions given after this table.\n\nThese BAT-AELs do not apply to existing turbines for mechanical drive applications or to plants operated < 500 h/yr.\n\nFor plants with a net electrical efficiency (EE) greater than 55 %, a correction factor may be applied to the higher end of the BAT-AEL range, corresponding to [higher end] × EE/55, where EE is the net electrical efficiency of the plant determined at ISO baseload conditions."]
["LCP","1. Energy industries","Unspecified","Unspecified","CCGT with a net total fuel utilisation of < 75 %","Existing","Natural gas ","≥ 600 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",18,"50","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period ","These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines\n\nIn the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective.\n\nThese BAT-AELs do not apply to existing turbines for mechanical drive applications or to plants operated < 500 h/yr.\n\nFor plants with a net electrical efficiency (EE) greater than 55 %, a correction factor may be applied to the higher end of the BAT-AEL range, corresponding to [higher end] × EE/55, where EE is the net electrical efficiency of the plant determined at ISO baseload conditions.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","CCGT with a net total fuel utilisation of < 75 %","Existing","Natural gas ","≥ 600 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",18,"50","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period ","These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines\n\nIn the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective.\n\nThese BAT-AELs do not apply to existing turbines for mechanical drive applications or to plants operated < 500 h/yr.\n\nFor plants with a net electrical efficiency (EE) greater than 55 %, a correction factor may be applied to the higher end of the BAT-AEL range, corresponding to [higher end] × EE/55, where EE is the net electrical efficiency of the plant determined at ISO baseload conditions."]
["LCP","1. Energy industries","Unspecified","Unspecified","CCGT with a net total fuel utilisation of ≥ 75 %","Existing","Natural gas ","≥ 600 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",10,"50","Green","Continuous ",0,0,0.15,"Yearly","These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines\n\nIn the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective.\n\nThese BAT-AELs do not apply to existing plants operated < 1 500 h/yr.\n\nOptimising the functioning of an existing technique to reduce NOX emissions further may lead to levels of CO emissions at the higher end of the indicative range for CO emissions given after this table.\n\nThese BAT-AELs do not apply to existing turbines for mechanical drive applications or to plants operated < 500 h/yr.\n\nFor plants with a net electrical efficiency (EE) greater than 55 %, a correction factor may be applied to the higher end of the BAT-AEL range, corresponding to [higher end] × EE/55, where EE is the net electrical efficiency of the plant determined at ISO baseload conditions.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","CCGT with a net total fuel utilisation of ≥ 75 %","Existing","Natural gas ","≥ 600 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",10,"50","Green","Continuous ",0,0,0.15,"Yearly","These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines\n\nIn the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective.\n\nThese BAT-AELs do not apply to existing plants operated < 1 500 h/yr.\n\nOptimising the functioning of an existing technique to reduce NOX emissions further may lead to levels of CO emissions at the higher end of the indicative range for CO emissions given after this table.\n\nThese BAT-AELs do not apply to existing turbines for mechanical drive applications or to plants operated < 500 h/yr.\n\nFor plants with a net electrical efficiency (EE) greater than 55 %, a correction factor may be applied to the higher end of the BAT-AEL range, corresponding to [higher end] × EE/55, where EE is the net electrical efficiency of the plant determined at ISO baseload conditions."]
["LCP","1. Energy industries","Unspecified","Unspecified","CCGT with a net total fuel utilisation of ≥ 75 %","Existing","Natural gas ","≥ 600 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",18,"55","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period ","These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines\n\nIn the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective.\n\nThese BAT-AELs do not apply to existing turbines for mechanical drive applications or to plants operated < 500 h/yr.\n\nFor plants with a net electrical efficiency (EE) greater than 55 %, a correction factor may be applied to the higher end of the BAT-AEL range, corresponding to [higher end] × EE/55, where EE is the net electrical efficiency of the plant determined at ISO baseload conditions.\n\nFor existing plants put into operation no later than 7 January 2014, the higher end of the BAT-AEL range is 65 mg/Nm3.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","CCGT with a net total fuel utilisation of ≥ 75 %","Existing","Natural gas ","≥ 600 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",18,"55","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period ","These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines\n\nIn the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective.\n\nThese BAT-AELs do not apply to existing turbines for mechanical drive applications or to plants operated < 500 h/yr.\n\nFor plants with a net electrical efficiency (EE) greater than 55 %, a correction factor may be applied to the higher end of the BAT-AEL range, corresponding to [higher end] × EE/55, where EE is the net electrical efficiency of the plant determined at ISO baseload conditions.\n\nFor existing plants put into operation no later than 7 January 2014, the higher end of the BAT-AEL range is 65 mg/Nm3."]
["LCP","1. Energy industries","Unspecified","Unspecified","Coal-fired PC boiler","Existing","Coal and/or lignite ","≥ 300 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Combination of other primary techniques for NOX reduction (e.g. air staging, fuel staging, flue-gas recirculation, low- NOX burners (LNB)); (iii) Selective non- catalytic reduction (SNCR); (iv) Selective catalytic reduction (SCR); (v) Combined techniques for NOX and SOX reduction","mg/Nm3",85,"165","Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ","In the case of plants put into operation no later than 7 January 2014, the higher end of the range is 200 mg/Nm3 for plants operated ≥ 1 500 h/yr, and 220 mg/Nm3 for plants operated < 1 500 h/yr.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Coal-fired PC boiler","Existing","Coal and/or lignite ","≥ 300 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Combination of other primary techniques for NOX reduction (e.g. air staging, fuel staging, flue-gas recirculation, low- NOX burners (LNB)); (iii) Selective non- catalytic reduction (SNCR); (iv) Selective catalytic reduction (SCR); (v) Combined techniques for NOX and SOX reduction","mg/Nm3",85,"165","Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ","In the case of plants put into operation no later than 7 January 2014, the higher end of the range is 200 mg/Nm3 for plants operated ≥ 1 500 h/yr, and 220 mg/Nm3 for plants operated < 1 500 h/yr."]
["LCP","1. Energy industries","Unspecified","Unspecified","Coal-fired PC boiler","Existing","Coal and/or lignite ","≥ 300 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Combination of other primary techniques for NOX reduction (e.g. air staging, fuel staging, flue-gas recirculation, low- NOX burners (LNB)); (iii) Selective non- catalytic reduction (SNCR); (iv) Selective catalytic reduction (SCR); (v) Combined techniques for NOX and SOX reduction","mg/Nm3",65,150,"Green","Continuous ",0,0,0.06,"Yearly",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Coal-fired PC boiler","Existing","Coal and/or lignite ","≥ 300 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Combination of other primary techniques for NOX reduction (e.g. air staging, fuel staging, flue-gas recirculation, low- NOX burners (LNB)); (iii) Selective non- catalytic reduction (SNCR); (iv) Selective catalytic reduction (SCR); (v) Combined techniques for NOX and SOX reduction","mg/Nm3",65,150,"Green","Continuous ",0,0,0.06,"Yearly",0]
["LCP","1. Energy industries","Unspecified","Unspecified","Coal-fired PC boiler","New","Coal and/or lignite ","≥ 300 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Combination of other primary techniques for NOX reduction (e.g. air staging, fuel staging, flue-gas recirculation, low- NOX burners (LNB)); (iii) Selective non- catalytic reduction (SNCR); (iv) Selective catalytic reduction (SCR); (v) Combined techniques for NOX and SOX reduction","mg/Nm3",65,85,"Green","Continuous ",0,0,0.06,"Yearly",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Coal-fired PC boiler","New","Coal and/or lignite ","≥ 300 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Combination of other primary techniques for NOX reduction (e.g. air staging, fuel staging, flue-gas recirculation, low- NOX burners (LNB)); (iii) Selective non- catalytic reduction (SNCR); (iv) Selective catalytic reduction (SCR); (v) Combined techniques for NOX and SOX reduction","mg/Nm3",65,85,"Green","Continuous ",0,0,0.06,"Yearly",0]
["LCP","1. Energy industries","Unspecified","Unspecified","Coal-fired PC boiler","New","Coal and/or lignite ","≥ 300 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Combination of other primary techniques for NOX reduction (e.g. air staging, fuel staging, flue-gas recirculation, low- NOX burners (LNB)); (iii) Selective non- catalytic reduction (SNCR); (iv) Selective catalytic reduction (SCR); (v) Combined techniques for NOX and SOX reduction","mg/Nm3",80,125,"Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Coal-fired PC boiler","New","Coal and/or lignite ","≥ 300 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Combination of other primary techniques for NOX reduction (e.g. air staging, fuel staging, flue-gas recirculation, low- NOX burners (LNB)); (iii) Selective non- catalytic reduction (SNCR); (iv) Selective catalytic reduction (SCR); (v) Combined techniques for NOX and SOX reduction","mg/Nm3",80,125,"Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ",0]
["LCP","1. Energy industries","Unspecified","Unspecified","Dual fuel gas turbines ","Unspecified","Gas oil ","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of gas oil in gas turbines, BAT is to use one or a combination of the techniques given below: (i) Water/steam addition; (ii) Low-NOX burners (LNB); (iii) Selective catalytic reduction (SCR)","mg/Nm3",145,"250","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period.","The emission level for NOX emissions to air from the combustion of gas oil in dual fuel gas turbines for emergency use operated < 500 h/yr",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Dual fuel gas turbines ","Unspecified","Gas oil ","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of gas oil in gas turbines, BAT is to use one or a combination of the techniques given below: (i) Water/steam addition; (ii) Low-NOX burners (LNB); (iii) Selective catalytic reduction (SCR)","mg/Nm3",145,"250","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period.","The emission level for NOX emissions to air from the combustion of gas oil in dual fuel gas turbines for emergency use operated < 500 h/yr"]
["LCP","1. Energy industries","Unspecified","Unspecified","Engine","Existing","Natural gas ","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",20,"100","Green","Continuous ",0,0,0.15,"Yearly","Optimising the functioning of an existing technique to reduce NOX emissions further may lead to levels of CO emissions at the higher end of the indicative range for CO emissions given after this table.\n\nThese BAT-AELs do not apply to plants operated < 1 500 h/yr.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Engine","Existing","Natural gas ","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",20,"100","Green","Continuous ",0,0,0.15,"Yearly","Optimising the functioning of an existing technique to reduce NOX emissions further may lead to levels of CO emissions at the higher end of the indicative range for CO emissions given after this table.\n\nThese BAT-AELs do not apply to plants operated < 1 500 h/yr."]
["LCP","1. Energy industries","Unspecified","Unspecified","Engine","Existing","Natural gas ","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",55,"110","Green","Continuous ",0,0,0.15,"Daily average or average over sampling period ","For plants operated < 500 h/yr, these levels are indicative.\n\nIn the case of engines for emergency use operated < 500 h/yr that could not apply the lean-burn concept or use SCR, the higher end of the indicative range is 175 mg/Nm3.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Engine","Existing","Natural gas ","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",55,"110","Green","Continuous ",0,0,0.15,"Daily average or average over sampling period ","For plants operated < 500 h/yr, these levels are indicative.\n\nIn the case of engines for emergency use operated < 500 h/yr that could not apply the lean-burn concept or use SCR, the higher end of the indicative range is 175 mg/Nm3."]
["LCP","1. Energy industries","Unspecified","Unspecified","Engine","New","Natural gas ","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",20,"75","Green","Continuous ",0,0,0.15,"Yearly","Optimising the functioning of an existing technique to reduce NOX emissions further may lead to levels of CO emissions at the higher end of the indicative range for CO emissions given after this table.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Engine","New","Natural gas ","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",20,"75","Green","Continuous ",0,0,0.15,"Yearly","Optimising the functioning of an existing technique to reduce NOX emissions further may lead to levels of CO emissions at the higher end of the indicative range for CO emissions given after this table."]
["LCP","1. Energy industries","Unspecified","Unspecified","Engine","New","Natural gas ","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",55,"85","Green","Continuous ",0,0,0.15,"Daily average or average over sampling period ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Engine","New","Natural gas ","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",55,"85","Green","Continuous ",0,0,0.15,"Daily average or average over sampling period ",0]
["LCP","1. Energy industries","Unspecified","Unspecified","FBC boiler combusting coal and/or lignite and lignite-fired PC boiler","Existing","Coal and/or lignite ","≥ 300 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Combination of other primary techniques for NOX reduction (e.g. air staging, fuel staging, flue-gas recirculation, low- NOX burners (LNB)); (iii) Selective non- catalytic reduction (SNCR); (iv) Selective catalytic reduction (SCR); (v) Combined techniques for NOX and SOX reduction","mg/Nm3",140,165,"Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ","The higher end of the range is 220 mg/Nm3 for FBC boilers put into operation no later than 7 January 2014 and for lignite-fired PC boilers.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","FBC boiler combusting coal and/or lignite and lignite-fired PC boiler","Existing","Coal and/or lignite ","≥ 300 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Combination of other primary techniques for NOX reduction (e.g. air staging, fuel staging, flue-gas recirculation, low- NOX burners (LNB)); (iii) Selective non- catalytic reduction (SNCR); (iv) Selective catalytic reduction (SCR); (v) Combined techniques for NOX and SOX reduction","mg/Nm3",140,165,"Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ","The higher end of the range is 220 mg/Nm3 for FBC boilers put into operation no later than 7 January 2014 and for lignite-fired PC boilers."]
["LCP","1. Energy industries","Unspecified","Unspecified","FBC boiler combusting coal and/or lignite and lignite-fired PC boiler","Existing","Coal and/or lignite ","≥ 300 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Combination of other primary techniques for NOX reduction (e.g. air staging, fuel staging, flue-gas recirculation, low- NOX burners (LNB)); (iii) Selective non- catalytic reduction (SNCR); (iv) Selective catalytic reduction (SCR); (v) Combined techniques for NOX and SOX reduction","mg/Nm3",85,"150","Green","Continuous ",0,0,0.06,"Yearly","The lower end of the range is considered achievable when using SCR.\n\nThe higher end of the range is 175 mg/Nm3 for FBC boilers put into operation no later than 7 January 2014 and for lignite-fired PC boilers.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","FBC boiler combusting coal and/or lignite and lignite-fired PC boiler","Existing","Coal and/or lignite ","≥ 300 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Combination of other primary techniques for NOX reduction (e.g. air staging, fuel staging, flue-gas recirculation, low- NOX burners (LNB)); (iii) Selective non- catalytic reduction (SNCR); (iv) Selective catalytic reduction (SCR); (v) Combined techniques for NOX and SOX reduction","mg/Nm3",85,"150","Green","Continuous ",0,0,0.06,"Yearly","The lower end of the range is considered achievable when using SCR.\n\nThe higher end of the range is 175 mg/Nm3 for FBC boilers put into operation no later than 7 January 2014 and for lignite-fired PC boilers."]
["LCP","1. Energy industries","Unspecified","Unspecified","FBC boiler combusting coal and/or lignite and lignite-fired PC boiler","New","Coal and/or lignite ","≥ 300 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Combination of other primary techniques for NOX reduction (e.g. air staging, fuel staging, flue-gas recirculation, low- NOX burners (LNB)); (iii) Selective non- catalytic reduction (SNCR); (iv) Selective catalytic reduction (SCR); (v) Combined techniques for NOX and SOX reduction","mg/Nm3",50,85,"Green","Continuous ",0,0,0.06,"Yearly",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","FBC boiler combusting coal and/or lignite and lignite-fired PC boiler","New","Coal and/or lignite ","≥ 300 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Combination of other primary techniques for NOX reduction (e.g. air staging, fuel staging, flue-gas recirculation, low- NOX burners (LNB)); (iii) Selective non- catalytic reduction (SNCR); (iv) Selective catalytic reduction (SCR); (v) Combined techniques for NOX and SOX reduction","mg/Nm3",50,85,"Green","Continuous ",0,0,0.06,"Yearly",0]
["LCP","1. Energy industries","Unspecified","Unspecified","FBC boiler combusting coal and/or lignite and lignite-fired PC boiler","New","Coal and/or lignite ","≥ 300 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Combination of other primary techniques for NOX reduction (e.g. air staging, fuel staging, flue-gas recirculation, low- NOX burners (LNB)); (iii) Selective non- catalytic reduction (SNCR); (iv) Selective catalytic reduction (SCR); (v) Combined techniques for NOX and SOX reduction","mg/Nm3",80,125,"Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","FBC boiler combusting coal and/or lignite and lignite-fired PC boiler","New","Coal and/or lignite ","≥ 300 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Combination of other primary techniques for NOX reduction (e.g. air staging, fuel staging, flue-gas recirculation, low- NOX burners (LNB)); (iii) Selective non- catalytic reduction (SNCR); (iv) Selective catalytic reduction (SCR); (v) Combined techniques for NOX and SOX reduction","mg/Nm3",80,125,"Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ",0]
["LCP","1. Energy industries","Unspecified","Unspecified","Fired engines ","Existing","HFO and/or gas oil in reciprocating engines","≥ 50 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of HFO and/or gas oil in reciprocating engines, BAT is to use one or a combination of the techniques given below: (i) Low-NOX combustion concept in diesel engines; (ii) Exhaust-gas recirculation (EGR); (iii) Water/steam addition; (iv) Selective catalytic reduction (SCR)","mg/Nm3",152,"625","Green","Continuous ",0,0,0.15,"Yearly","These BAT-AELs do not apply to plants operated < 1 500 h/yr or to plants that cannot be fitted with secondary abatement techniques.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Fired engines ","Existing","HFO and/or gas oil in reciprocating engines","≥ 50 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of HFO and/or gas oil in reciprocating engines, BAT is to use one or a combination of the techniques given below: (i) Low-NOX combustion concept in diesel engines; (ii) Exhaust-gas recirculation (EGR); (iii) Water/steam addition; (iv) Selective catalytic reduction (SCR)","mg/Nm3",152,"625","Green","Continuous ",0,0,0.15,"Yearly","These BAT-AELs do not apply to plants operated < 1 500 h/yr or to plants that cannot be fitted with secondary abatement techniques."]
["LCP","1. Energy industries","Unspecified","Unspecified","Fired engines ","Existing","HFO and/or gas oil in reciprocating engines","≥ 50 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of HFO and/or gas oil in reciprocating engines, BAT is to use one or a combination of the techniques given below: (i) Low-NOX combustion concept in diesel engines; (ii) Exhaust-gas recirculation (EGR); (iii) Water/steam addition; (iv) Selective catalytic reduction (SCR)","mg/Nm3",150,"750","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period ","The BAT-AEL range is 1 150–1 900 mg/Nm3 for plants operated < 1 500 h/yr and for plants that cannot be fitted with secondary abatement techniques.\n\nFor plants operated < 500 h/yr, these levels are indicative.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Fired engines ","Existing","HFO and/or gas oil in reciprocating engines","≥ 50 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of HFO and/or gas oil in reciprocating engines, BAT is to use one or a combination of the techniques given below: (i) Low-NOX combustion concept in diesel engines; (ii) Exhaust-gas recirculation (EGR); (iii) Water/steam addition; (iv) Selective catalytic reduction (SCR)","mg/Nm3",150,"750","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period ","The BAT-AEL range is 1 150–1 900 mg/Nm3 for plants operated < 1 500 h/yr and for plants that cannot be fitted with secondary abatement techniques.\n\nFor plants operated < 500 h/yr, these levels are indicative."]
["LCP","1. Energy industries","Unspecified","Unspecified","Fired engines ","New","HFO and/or gas oil in reciprocating engines","≥ 50 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of HFO and/or gas oil in reciprocating engines, BAT is to use one or a combination of the techniques given below: (i) Low-NOX combustion concept in diesel engines; (ii) Exhaust-gas recirculation (EGR); (iii) Water/steam addition; (iv) Selective catalytic reduction (SCR)","mg/Nm3",115,"190","Green","Continuous ",0,0,0.15,"Yearly","For plants including units of < 20 MWth combusting HFO, the higher end of the BAT-AEL range applying to those units is 225 mg/Nm3.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Fired engines ","New","HFO and/or gas oil in reciprocating engines","≥ 50 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of HFO and/or gas oil in reciprocating engines, BAT is to use one or a combination of the techniques given below: (i) Low-NOX combustion concept in diesel engines; (ii) Exhaust-gas recirculation (EGR); (iii) Water/steam addition; (iv) Selective catalytic reduction (SCR)","mg/Nm3",115,"190","Green","Continuous ",0,0,0.15,"Yearly","For plants including units of < 20 MWth combusting HFO, the higher end of the BAT-AEL range applying to those units is 225 mg/Nm3."]
["LCP","1. Energy industries","Unspecified","Unspecified","Fired engines ","New","HFO and/or gas oil in reciprocating engines","≥ 50 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of HFO and/or gas oil in reciprocating engines, BAT is to use one or a combination of the techniques given below: (i) Low-NOX combustion concept in diesel engines; (ii) Exhaust-gas recirculation (EGR); (iii) Water/steam addition; (iv) Selective catalytic reduction (SCR)","mg/Nm3",145,"300","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Fired engines ","New","HFO and/or gas oil in reciprocating engines","≥ 50 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of HFO and/or gas oil in reciprocating engines, BAT is to use one or a combination of the techniques given below: (i) Low-NOX combustion concept in diesel engines; (ii) Exhaust-gas recirculation (EGR); (iii) Water/steam addition; (iv) Selective catalytic reduction (SCR)","mg/Nm3",145,"300","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period ",0]
["LCP","1. Energy industries","Unspecified","Unspecified","Gas turbine for mechanical drive applications — All but plants operated < 500 h/yr","Existing","Natural gas ","≥ 50 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",25,"55","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period ","These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines\n\nIn the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective.\n\nFor existing plants put into operation no later than 7 January 2014, the higher end of the BAT-AEL range is 65 mg/Nm3.\n\nFor existing plants put into operation no later than 7 January 2014, the higher end of the BAT-AEL range is 65 mg/Nm3.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Gas turbine for mechanical drive applications — All but plants operated < 500 h/yr","Existing","Natural gas ","≥ 50 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",25,"55","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period ","These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines\n\nIn the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective.\n\nFor existing plants put into operation no later than 7 January 2014, the higher end of the BAT-AEL range is 65 mg/Nm3.\n\nFor existing plants put into operation no later than 7 January 2014, the higher end of the BAT-AEL range is 65 mg/Nm3."]
["LCP","1. Energy industries","Unspecified","Unspecified","Gas turbine for mechanical drive applications — All but plants operated < 500 h/yr","Existing","Natural gas ","≥ 50 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",15,"50","Green","Continuous ",0,0,0.15,"Yearly","These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines\n\nIn the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective.\n\nThese BAT-AELs do not apply to existing plants operated < 1 500 h/yr.\n\nOptimising the functioning of an existing technique to reduce NOX emissions further may lead to levels of CO emissions at the higher end of the indicative range for CO emissions given after this table.\n\nFor existing plants put into operation no later than 7 January 2014, the higher end of the BAT-AEL range is 60 mg/Nm3.\n",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Gas turbine for mechanical drive applications — All but plants operated < 500 h/yr","Existing","Natural gas ","≥ 50 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",15,"50","Green","Continuous ",0,0,0.15,"Yearly","These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines\n\nIn the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective.\n\nThese BAT-AELs do not apply to existing plants operated < 1 500 h/yr.\n\nOptimising the functioning of an existing technique to reduce NOX emissions further may lead to levels of CO emissions at the higher end of the indicative range for CO emissions given after this table.\n\nFor existing plants put into operation no later than 7 January 2014, the higher end of the BAT-AEL range is 60 mg/Nm3.\n"]
["LCP","1. Energy industries","Unspecified","Unspecified","Gas turbine put into operation no later than 27 November 2003, or existing gas turbine for emergency use and operated < 500 h/yr","Existing","Natural gas ","≥ 50 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3","N/A","N/A","Green","Continuous ",0,0,0.15,"Yearly","These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines\n\nIn the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective.\n\nThese BAT-AELs do not apply to existing plants operated < 1 500 h/yr.\n\nOptimising the functioning of an existing technique to reduce NOX emissions further may lead to levels of CO emissions at the higher end of the indicative range for CO emissions given after this table.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Gas turbine put into operation no later than 27 November 2003, or existing gas turbine for emergency use and operated < 500 h/yr","Existing","Natural gas ","≥ 50 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3","N/A","N/A","Green","Continuous ",0,0,0.15,"Yearly","These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines\n\nIn the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective.\n\nThese BAT-AELs do not apply to existing plants operated < 1 500 h/yr.\n\nOptimising the functioning of an existing technique to reduce NOX emissions further may lead to levels of CO emissions at the higher end of the indicative range for CO emissions given after this table."]
["LCP","1. Energy industries","Unspecified","Unspecified","Gas turbine put into operation no later than 27 November 2003, or existing gas turbine for emergency use and operated < 500 h/yr","Existing","Natural gas ","≥ 50 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",60,"140","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period ","These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines\n\nIn the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective.\n\nThe lower end of the BAT-AEL range for NOX can be achieved with DLN burners.\n\nThese levels are indicative.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Gas turbine put into operation no later than 27 November 2003, or existing gas turbine for emergency use and operated < 500 h/yr","Existing","Natural gas ","≥ 50 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",60,"140","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period ","These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines\n\nIn the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective.\n\nThe lower end of the BAT-AEL range for NOX can be achieved with DLN burners.\n\nThese levels are indicative."]
["LCP","1. Energy industries","Unspecified","Unspecified","IGCC","Existing","Unspecified","≥ 100 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent and/or reduce NOX emissions to air while limiting CO emissions to air from IGCC plants, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Water/steam addition; (iii) Dry low-NOX burners (DLN); (iv) Syngas dilution with waste nitrogen from the air supply unit (ASU); (v) Selective catalytic reduction (SCR)","mg/Nm3",12,"45","Green","Continuous",0,0,0.15,"Yearly","As an indication, the yearly average CO emission levels for existing plants operated ≥ 1 500 h/yr and for new plants will generally be < 5–30 mg/Nm3.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","IGCC","Existing","Unspecified","≥ 100 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent and/or reduce NOX emissions to air while limiting CO emissions to air from IGCC plants, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Water/steam addition; (iii) Dry low-NOX burners (DLN); (iv) Syngas dilution with waste nitrogen from the air supply unit (ASU); (v) Selective catalytic reduction (SCR)","mg/Nm3",12,"45","Green","Continuous",0,0,0.15,"Yearly","As an indication, the yearly average CO emission levels for existing plants operated ≥ 1 500 h/yr and for new plants will generally be < 5–30 mg/Nm3."]
["LCP","1. Energy industries","Unspecified","Unspecified","IGCC","Existing","Unspecified","≥ 100 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent and/or reduce NOX emissions to air while limiting CO emissions to air from IGCC plants, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Water/steam addition; (iii) Dry low-NOX burners (DLN); (iv) Syngas dilution with waste nitrogen from the air supply unit (ASU); (v) Selective catalytic reduction (SCR)","mg/Nm3",1,"60","Green","Continuous",0,0,0.15,"Daily average or average over the sampling period ","As an indication, the yearly average CO emission levels for existing plants operated ≥ 1 500 h/yr and for new plants will generally be < 5–30 mg/Nm3.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","IGCC","Existing","Unspecified","≥ 100 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent and/or reduce NOX emissions to air while limiting CO emissions to air from IGCC plants, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Water/steam addition; (iii) Dry low-NOX burners (DLN); (iv) Syngas dilution with waste nitrogen from the air supply unit (ASU); (v) Selective catalytic reduction (SCR)","mg/Nm3",1,"60","Green","Continuous",0,0,0.15,"Daily average or average over the sampling period ","As an indication, the yearly average CO emission levels for existing plants operated ≥ 1 500 h/yr and for new plants will generally be < 5–30 mg/Nm3."]
["LCP","1. Energy industries","Unspecified","Unspecified","IGCC","New","Unspecified","≥ 100 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent and/or reduce NOX emissions to air while limiting CO emissions to air from IGCC plants, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Water/steam addition; (iii) Dry low-NOX burners (DLN); (iv) Syngas dilution with waste nitrogen from the air supply unit (ASU); (v) Selective catalytic reduction (SCR)","mg/Nm3",10,"25","Green","Continuous",0,0,0.15,"Yearly","As an indication, the yearly average CO emission levels for existing plants operated ≥ 1 500 h/yr and for new plants will generally be < 5–30 mg/Nm3.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","IGCC","New","Unspecified","≥ 100 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent and/or reduce NOX emissions to air while limiting CO emissions to air from IGCC plants, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Water/steam addition; (iii) Dry low-NOX burners (DLN); (iv) Syngas dilution with waste nitrogen from the air supply unit (ASU); (v) Selective catalytic reduction (SCR)","mg/Nm3",10,"25","Green","Continuous",0,0,0.15,"Yearly","As an indication, the yearly average CO emission levels for existing plants operated ≥ 1 500 h/yr and for new plants will generally be < 5–30 mg/Nm3."]
["LCP","1. Energy industries","Unspecified","Unspecified","IGCC","New","Unspecified","≥ 100 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent and/or reduce NOX emissions to air while limiting CO emissions to air from IGCC plants, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Water/steam addition; (iii) Dry low-NOX burners (DLN); (iv) Syngas dilution with waste nitrogen from the air supply unit (ASU); (v) Selective catalytic reduction (SCR)","mg/Nm3",1,"35","Green","Continuous",0,0,0.15,"Daily average or average over the sampling period ","As an indication, the yearly average CO emission levels for existing plants operated ≥ 1 500 h/yr and for new plants will generally be < 5–30 mg/Nm3.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","IGCC","New","Unspecified","≥ 100 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent and/or reduce NOX emissions to air while limiting CO emissions to air from IGCC plants, BAT is to use one or a combination of the techniques given below: (i) Combustion optimisation; (ii) Water/steam addition; (iii) Dry low-NOX burners (DLN); (iv) Syngas dilution with waste nitrogen from the air supply unit (ASU); (v) Selective catalytic reduction (SCR)","mg/Nm3",1,"35","Green","Continuous",0,0,0.15,"Daily average or average over the sampling period ","As an indication, the yearly average CO emission levels for existing plants operated ≥ 1 500 h/yr and for new plants will generally be < 5–30 mg/Nm3."]
["LCP","1. Energy industries","Unspecified","Unspecified","OCGT","New","Natural gas ","≥ 50 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",15,"35","Green","Continuous ",0,0,0.15,"Yearly","These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines\n\nIn the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective.\n\nThese BAT-AELs do not apply to existing plants operated < 1 500 h/yr.\n\nOptimising the functioning of an existing technique to reduce NOX emissions further may lead to levels of CO emissions at the higher end of the indicative range for CO emissions given after this table.\n\nThese BAT-AELs do not apply to existing turbines for mechanical drive applications or to plants operated < 500 h/yr.\n\nFor plants with a net electrical efficiency (EE) greater than 39 %, a correction factor may be applied to the higher end of the range, corresponding to [higher end] × EE/39, where EE is the net electrical energy efficiency or net mechanical energy efficiency of the plant determined at ISO baseload conditions.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","OCGT","New","Natural gas ","≥ 50 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",15,"35","Green","Continuous ",0,0,0.15,"Yearly","These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines\n\nIn the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective.\n\nThese BAT-AELs do not apply to existing plants operated < 1 500 h/yr.\n\nOptimising the functioning of an existing technique to reduce NOX emissions further may lead to levels of CO emissions at the higher end of the indicative range for CO emissions given after this table.\n\nThese BAT-AELs do not apply to existing turbines for mechanical drive applications or to plants operated < 500 h/yr.\n\nFor plants with a net electrical efficiency (EE) greater than 39 %, a correction factor may be applied to the higher end of the range, corresponding to [higher end] × EE/39, where EE is the net electrical energy efficiency or net mechanical energy efficiency of the plant determined at ISO baseload conditions."]
["LCP","1. Energy industries","Unspecified","Unspecified","OCGT","New","Natural gas ","≥ 50 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",25,"50","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period ","These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines\n\nIn the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective.\n\nThese BAT-AELs do not apply to existing turbines for mechanical drive applications or to plants operated < 500 h/yr.\n\nFor plants with a net electrical efficiency (EE) greater than 39 %, a correction factor may be applied to the higher end of the range, corresponding to [higher end] × EE/39, where EE is the net electrical energy efficiency or net mechanical energy efficiency of the plant determined at ISO baseload conditions.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","OCGT","New","Natural gas ","≥ 50 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",25,"50","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period ","These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines\n\nIn the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective.\n\nThese BAT-AELs do not apply to existing turbines for mechanical drive applications or to plants operated < 500 h/yr.\n\nFor plants with a net electrical efficiency (EE) greater than 39 %, a correction factor may be applied to the higher end of the range, corresponding to [higher end] × EE/39, where EE is the net electrical energy efficiency or net mechanical energy efficiency of the plant determined at ISO baseload conditions."]
["LCP","1. Energy industries","Unspecified","Unspecified","OCGT (excluding turbines for mechanical drive applications) — All but plants operated < 500 h/yr","Existing","Natural gas ","≥ 50 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",15,"50","Green","Continuous ",0,0,0.15,"Yearly","These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines\n\nIn the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective.\n\nThese BAT-AELs do not apply to existing plants operated < 1 500 h/yr.\n\nOptimising the functioning of an existing technique to reduce NOX emissions further may lead to levels of CO emissions at the higher end of the indicative range for CO emissions given after this table.\n\nThese BAT-AELs do not apply to existing turbines for mechanical drive applications or to plants operated < 500 h/yr.\n\nFor plants with a net electrical efficiency (EE) greater than 39 %, a correction factor may be applied to the higher end of the range, corresponding to [higher end] × EE/39, where EE is the net electrical energy efficiency or net mechanical energy efficiency of the plant determined at ISO baseload conditions.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","OCGT (excluding turbines for mechanical drive applications) — All but plants operated < 500 h/yr","Existing","Natural gas ","≥ 50 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",15,"50","Green","Continuous ",0,0,0.15,"Yearly","These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines\n\nIn the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective.\n\nThese BAT-AELs do not apply to existing plants operated < 1 500 h/yr.\n\nOptimising the functioning of an existing technique to reduce NOX emissions further may lead to levels of CO emissions at the higher end of the indicative range for CO emissions given after this table.\n\nThese BAT-AELs do not apply to existing turbines for mechanical drive applications or to plants operated < 500 h/yr.\n\nFor plants with a net electrical efficiency (EE) greater than 39 %, a correction factor may be applied to the higher end of the range, corresponding to [higher end] × EE/39, where EE is the net electrical energy efficiency or net mechanical energy efficiency of the plant determined at ISO baseload conditions."]
["LCP","1. Energy industries","Unspecified","Unspecified","OCGT (excluding turbines for mechanical drive applications) — All but plants operated < 500 h/yr","Existing","Natural gas ","≥ 50 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",25,"55","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period ","These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines\n\nIn the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective.\n\nThe higher end of the range is 80 mg/Nm3 in the case of plants which were put into operation no later than 27 November 2003 and are operated between 500 h/yr and 1 500 h/yr.\n\n\nThese BAT-AELs do not apply to existing turbines for mechanical drive applications or to plants operated < 500 h/yr.\n\nFor plants with a net electrical efficiency (EE) greater than 39 %, a correction factor may be applied to the higher end of the range, corresponding to [higher end] × EE/39, where EE is the net electrical energy efficiency or net mechanical e",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","OCGT (excluding turbines for mechanical drive applications) — All but plants operated < 500 h/yr","Existing","Natural gas ","≥ 50 MWth","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of natural gas in engines, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Lean-burn concept; (iii) Advanced lean-burn concept; (iv) Selective catalytic reduction (SCR)","mg/Nm3",25,"55","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period ","These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines\n\nIn the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective.\n\nThe higher end of the range is 80 mg/Nm3 in the case of plants which were put into operation no later than 27 November 2003 and are operated between 500 h/yr and 1 500 h/yr.\n\n\nThese BAT-AELs do not apply to existing turbines for mechanical drive applications or to plants operated < 500 h/yr.\n\nFor plants with a net electrical efficiency (EE) greater than 39 %, a correction factor may be applied to the higher end of the range, corresponding to [higher end] × EE/39, where EE is the net electrical energy efficiency or net mechanical e"]
["LCP","1. Energy industries","Unspecified","Unspecified","Open-cycle gas turbines on offshore platforms","Existing","Gaseous fuels ","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of gaseous and/or liquid fuels on offshore platforms, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Dry low-NOX burners (DLN); (iii) Lean-burn concept; (iv) Low-NOX burners (LNB)","mg/Nm3",50,"350","Green","Continuous ",0,0,0.03,"Average over the sampling period","These BAT-AELs are based on > 70 % of baseload power available on the day.\n\nThis includes single fuel and dual fuel gas turbines.\n\nThe lower end of the BAT-AEL range can be achieved with DLN burners.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Open-cycle gas turbines on offshore platforms","Existing","Gaseous fuels ","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of gaseous and/or liquid fuels on offshore platforms, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Dry low-NOX burners (DLN); (iii) Lean-burn concept; (iv) Low-NOX burners (LNB)","mg/Nm3",50,"350","Green","Continuous ",0,0,0.03,"Average over the sampling period","These BAT-AELs are based on > 70 % of baseload power available on the day.\n\nThis includes single fuel and dual fuel gas turbines.\n\nThe lower end of the BAT-AEL range can be achieved with DLN burners."]
["LCP","1. Energy industries","Unspecified","Unspecified","Open-cycle gas turbines on offshore platforms","New","Gaseous fuels ","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of gaseous and/or liquid fuels on offshore platforms, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Dry low-NOX burners (DLN); (iii) Lean-burn concept; (iv) Low-NOX burners (LNB)","mg/Nm3",15,"50","Green","Continuous ",0,0,0.03,"Average over the sampling period","These BAT-AELs are based on > 70 % of baseload power available on the day. \n\nThis includes single fuel and dual fuel gas turbines.\n\nThe higher end of the BAT-AEL range is 250 mg/Nm3 if DLN burners are not applicable.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Open-cycle gas turbines on offshore platforms","New","Gaseous fuels ","Unspecified ","Unspecified","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion of gaseous and/or liquid fuels on offshore platforms, BAT is to use one or a combination of the techniques given below: (i) Advanced control system; (ii) Dry low-NOX burners (DLN); (iii) Lean-burn concept; (iv) Low-NOX burners (LNB)","mg/Nm3",15,"50","Green","Continuous ",0,0,0.03,"Average over the sampling period","These BAT-AELs are based on > 70 % of baseload power available on the day. \n\nThis includes single fuel and dual fuel gas turbines.\n\nThe higher end of the BAT-AEL range is 250 mg/Nm3 if DLN burners are not applicable."]
["LCP","1. Energy industries","Unspecified","Unspecified","Biomass-, peat-, coal- and/or lignite-fired combustion plant","Unspecified","Co-incineration of waste with biomass, peat, coal and/or lignite","Unspecified ","Unspecified","Air","PCDD/F","In order to reduce emissions of volatile organic compounds and polychlorinated dibenzo-dioxins and -furans to air from the co-incineration of waste with biomass, peat, coal and/or lignite, BAT is to use a combination of the techniques given in BAT 6, BAT 26 and below: (i) Activated carbon injection; (ii) Rapid quenching using wet scrubbing/flue-gas condenser; (iii) Selective catalytic reduction (SCR)","ng I-TEQ/Nm3",0.01,"0.03","Green","Once every 6 months ",0,0,0.06,"Average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Biomass-, peat-, coal- and/or lignite-fired combustion plant","Unspecified","Co-incineration of waste with biomass, peat, coal and/or lignite","Unspecified ","Unspecified","Air","PCDD/F","In order to reduce emissions of volatile organic compounds and polychlorinated dibenzo-dioxins and -furans to air from the co-incineration of waste with biomass, peat, coal and/or lignite, BAT is to use a combination of the techniques given in BAT 6, BAT 26 and below: (i) Activated carbon injection; (ii) Rapid quenching using wet scrubbing/flue-gas condenser; (iii) Selective catalytic reduction (SCR)","ng I-TEQ/Nm3",0.01,"0.03","Green","Once every 6 months ",0,0,0.06,"Average over the sampling period",0]
["LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Unspecified","100 % process fuels from the chemical industry","Unspecified ","Unspecified","Air","PCDD/F","In order to reduce emissions to air of volatile organic compounds and polychlorinated dibenzo- dioxins and -furans from the combustion of process fuels from the chemical industry in boilers, BAT is to use one or a combination of the techniques given in BAT 6 and below: (i) Activated carbon injection; (ii) Rapid quenching using wet scrubbing/flue-gas condenser; (iii) Selective catalytic reduction (SCR)","ng I-TEQ/Nm3",1.2E-2,"0.036","Green","Once every 6 months",0,0,0.03,"Average over the sampling period","These BAT-AELs only apply to plants using fuels derived from chemical processes involving chlorinated substances.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Unspecified","100 % process fuels from the chemical industry","Unspecified ","Unspecified","Air","PCDD/F","In order to reduce emissions to air of volatile organic compounds and polychlorinated dibenzo- dioxins and -furans from the combustion of process fuels from the chemical industry in boilers, BAT is to use one or a combination of the techniques given in BAT 6 and below: (i) Activated carbon injection; (ii) Rapid quenching using wet scrubbing/flue-gas condenser; (iii) Selective catalytic reduction (SCR)","ng I-TEQ/Nm3",1.2E-2,"0.036","Green","Once every 6 months",0,0,0.03,"Average over the sampling period","These BAT-AELs only apply to plants using fuels derived from chemical processes involving chlorinated substances."]
["LCP","1. Energy industries","Unspecified","Unspecified","Unspecified","Unspecified","Co-incineration of waste with biomass and/or peat","Unspecified ","Unspecified","Air","Sb + As + Pb + Cr + Co + Cu + Mn + Ni + V","In order to reduce dust and particulate-bound metal emissions to air from the co-incineration of waste with biomass and/or peat, BAT is to use one or a combination of the techniques given in BAT 26.","mg/Nm3",7.4999999999999997E-2,"0.3","Amber",0,0,0,0.06,"Average of samples obtained during one year",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Unspecified","Unspecified","Co-incineration of waste with biomass and/or peat","Unspecified ","Unspecified","Air","Sb + As + Pb + Cr + Co + Cu + Mn + Ni + V","In order to reduce dust and particulate-bound metal emissions to air from the co-incineration of waste with biomass and/or peat, BAT is to use one or a combination of the techniques given in BAT 26.","mg/Nm3",7.4999999999999997E-2,"0.3","Amber",0,0,0,0.06,"Average of samples obtained during one year",0]
["LCP","1. Energy industries","Unspecified","Unspecified","Unspecified","Unspecified","Co-incineration of waste with coal and/or lignite","< 300 MWth ","Unspecified","Air","Sb + As + Pb + Cr + Co + Cu + Mn + Ni + V","In order to reduce dust and particulate-bound metal emissions to air from the co-incineration of waste with coal and/or lignite, BAT is to use one or a combination of the techniques given in BAT 22.","mg/Nm3",5.0000000000000001E-3,"0.5","Green","Once every 6 months",0,0,0.06,"Average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Unspecified","Unspecified","Co-incineration of waste with coal and/or lignite","< 300 MWth ","Unspecified","Air","Sb + As + Pb + Cr + Co + Cu + Mn + Ni + V","In order to reduce dust and particulate-bound metal emissions to air from the co-incineration of waste with coal and/or lignite, BAT is to use one or a combination of the techniques given in BAT 22.","mg/Nm3",5.0000000000000001E-3,"0.5","Green","Once every 6 months",0,0,0.06,"Average over the sampling period",0]
["LCP","1. Energy industries","Unspecified","Unspecified","Unspecified","Unspecified","Co-incineration of waste with coal and/or lignite","≥ 300 MWth","Unspecified","Air","Sb + As + Pb + Cr + Co + Cu + Mn + Ni + V","In order to reduce dust and particulate-bound metal emissions to air from the co-incineration of waste with coal and/or lignite, BAT is to use one or a combination of the techniques given in BAT 22.","mg/Nm3",5.0000000000000001E-3,"0.2","Green","Once every 3 months ",0,0,0.06,"Average of samples obtained during one year",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Unspecified","Unspecified","Co-incineration of waste with coal and/or lignite","≥ 300 MWth","Unspecified","Air","Sb + As + Pb + Cr + Co + Cu + Mn + Ni + V","In order to reduce dust and particulate-bound metal emissions to air from the co-incineration of waste with coal and/or lignite, BAT is to use one or a combination of the techniques given in BAT 22.","mg/Nm3",5.0000000000000001E-3,"0.2","Green","Once every 3 months ",0,0,0.06,"Average of samples obtained during one year",0]
["LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Coal and/or lignite ","< 100 MWth","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD; (viii) Combined techniques for NOX and SOX reduction; (ix) Replacement or removal of the gas- gas heater located downstream of the wet FGD; (x) Fuel choice","mg/Nm3",150,360,"Green","Continuous ",0,0,0.06,"Yearly",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Coal and/or lignite ","< 100 MWth","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD; (viii) Combined techniques for NOX and SOX reduction; (ix) Replacement or removal of the gas- gas heater located downstream of the wet FGD; (x) Fuel choice","mg/Nm3",150,360,"Green","Continuous ",0,0,0.06,"Yearly",0]
["LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Coal and/or lignite ","100-300 MWth","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD; (viii) Combined techniques for NOX and SOX reduction; (ix) Replacement or removal of the gas- gas heater located downstream of the wet FGD; (x) Fuel choice","mg/Nm3",95,200,"Green","Continuous ",0,0,0.06,"Yearly",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Coal and/or lignite ","100-300 MWth","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD; (viii) Combined techniques for NOX and SOX reduction; (ix) Replacement or removal of the gas- gas heater located downstream of the wet FGD; (x) Fuel choice","mg/Nm3",95,200,"Green","Continuous ",0,0,0.06,"Yearly",0]
["LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Solid biomass and/or peat","< 100 MWth","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3",15,"100","Green","Continuous ",0,0,0.06,"Yearly ","These BAT-AELs do not apply to plants operated < 1 500 h/yr.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Solid biomass and/or peat","< 100 MWth","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3",15,"100","Green","Continuous ",0,0,0.06,"Yearly ","These BAT-AELs do not apply to plants operated < 1 500 h/yr."]
["LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Solid biomass and/or peat","< 100 MWth","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3",30,"215","Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ","For plants operated < 500 h/yr, these levels are indicative.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Solid biomass and/or peat","< 100 MWth","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3",30,"215","Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ","For plants operated < 500 h/yr, these levels are indicative."]
["LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Solid biomass and/or peat","≥ 300 MWth","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3",10,"50","Green","Continuous ",0,0,0.06,"Yearly ","For existing plants burning fuels where the average sulphur content is 0,1 wt-% (dry) or higher, the higher end of the BAT-AEL range is 100 mg/Nm3.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Solid biomass and/or peat","≥ 300 MWth","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3",10,"50","Green","Continuous ",0,0,0.06,"Yearly ","For existing plants burning fuels where the average sulphur content is 0,1 wt-% (dry) or higher, the higher end of the BAT-AEL range is 100 mg/Nm3."]
["LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Solid biomass and/or peat","≥ 300 MWth","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3",20,"85","Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ","For existing plants burning fuels where the average sulphur content is 0,1 wt-% (dry) or higher, the higher end of the BAT-AEL range is 165 mg/Nm3, or 215 mg/Nm3 if those plants have been put into operation no later than 7 January 2014 and/or are FBC boilers combusting peat.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Solid biomass and/or peat","≥ 300 MWth","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3",20,"85","Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ","For existing plants burning fuels where the average sulphur content is 0,1 wt-% (dry) or higher, the higher end of the BAT-AEL range is 165 mg/Nm3, or 215 mg/Nm3 if those plants have been put into operation no later than 7 January 2014 and/or are FBC boilers combusting peat."]
["LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Solid biomass and/or peat","100-300 MWth","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3",10,"70","Green","Continuous ",0,0,0.06,"Yearly ","For existing plants burning fuels where the average sulphur content is 0,1 wt-% (dry) or higher, the higher end of the BAT-AEL range is 100 mg/Nm3.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Solid biomass and/or peat","100-300 MWth","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3",10,"70","Green","Continuous ",0,0,0.06,"Yearly ","For existing plants burning fuels where the average sulphur content is 0,1 wt-% (dry) or higher, the higher end of the BAT-AEL range is 100 mg/Nm3."]
["LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Solid biomass and/or peat","100-300 MWth","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3",20,"175","Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ","For existing plants burning fuels where the average sulphur content is 0,1 wt-% (dry) or higher, the higher end of the BAT-AEL range is 215 mg/Nm3.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Solid biomass and/or peat","100-300 MWth","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3",20,"175","Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ","For existing plants burning fuels where the average sulphur content is 0,1 wt-% (dry) or higher, the higher end of the BAT-AEL range is 215 mg/Nm3."]
["LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Coal and/or lignite ","< 100 MWth","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD; (viii) Combined techniques for NOX and SOX reduction; (ix) Replacement or removal of the gas- gas heater located downstream of the wet FGD; (x) Fuel choice","mg/Nm3",170,400,"Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ","For plants operated < 500 h/yr, these levels are indicative.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Coal and/or lignite ","< 100 MWth","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD; (viii) Combined techniques for NOX and SOX reduction; (ix) Replacement or removal of the gas- gas heater located downstream of the wet FGD; (x) Fuel choice","mg/Nm3",170,400,"Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ","For plants operated < 500 h/yr, these levels are indicative."]
["LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Coal and/or lignite ","100-300 MWth","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD; (viii) Combined techniques for NOX and SOX reduction; (ix) Replacement or removal of the gas- gas heater located downstream of the wet FGD; (x) Fuel choice","mg/Nm3",135,220,"Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ","In the case of plants put into operation no later than 7 January 2014, the upper end of the BAT-AEL range is 250 mg/Nm3.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","Existing","Coal and/or lignite ","100-300 MWth","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD; (viii) Combined techniques for NOX and SOX reduction; (ix) Replacement or removal of the gas- gas heater located downstream of the wet FGD; (x) Fuel choice","mg/Nm3",135,220,"Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ","In the case of plants put into operation no later than 7 January 2014, the upper end of the BAT-AEL range is 250 mg/Nm3."]
["LCP","1. Energy industries","Unspecified","Unspecified","All","New","Coal and/or lignite ","< 100 MWth","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD; (viii) Combined techniques for NOX and SOX reduction; (ix) Replacement or removal of the gas- gas heater located downstream of the wet FGD; (x) Fuel choice","mg/Nm3",150,200,"Green","Continuous ",0,0,0.06,"Yearly",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","New","Coal and/or lignite ","< 100 MWth","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD; (viii) Combined techniques for NOX and SOX reduction; (ix) Replacement or removal of the gas- gas heater located downstream of the wet FGD; (x) Fuel choice","mg/Nm3",150,200,"Green","Continuous ",0,0,0.06,"Yearly",0]
["LCP","1. Energy industries","Unspecified","Unspecified","All","New","Coal and/or lignite ","< 100 MWth","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD; (viii) Combined techniques for NOX and SOX reduction; (ix) Replacement or removal of the gas- gas heater located downstream of the wet FGD; (x) Fuel choice","mg/Nm3",170,220,"Green","Continuous ",0,0,0.06,"Daily",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","New","Coal and/or lignite ","< 100 MWth","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD; (viii) Combined techniques for NOX and SOX reduction; (ix) Replacement or removal of the gas- gas heater located downstream of the wet FGD; (x) Fuel choice","mg/Nm3",170,220,"Green","Continuous ",0,0,0.06,"Daily",0]
["LCP","1. Energy industries","Unspecified","Unspecified","All","New","Coal and/or lignite ","100-300 MWth","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD; (viii) Combined techniques for NOX and SOX reduction; (ix) Replacement or removal of the gas- gas heater located downstream of the wet FGD; (x) Fuel choice","mg/Nm3",80,150,"Green","Continuous ",0,0,0.06,"Yearly",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","New","Coal and/or lignite ","100-300 MWth","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD; (viii) Combined techniques for NOX and SOX reduction; (ix) Replacement or removal of the gas- gas heater located downstream of the wet FGD; (x) Fuel choice","mg/Nm3",80,150,"Green","Continuous ",0,0,0.06,"Yearly",0]
["LCP","1. Energy industries","Unspecified","Unspecified","All","New","Coal and/or lignite ","100-300 MWth","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD; (viii) Combined techniques for NOX and SOX reduction; (ix) Replacement or removal of the gas- gas heater located downstream of the wet FGD; (x) Fuel choice","mg/Nm3",135,200,"Green","Continuous ",0,0,0.06,"Daily",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","New","Coal and/or lignite ","100-300 MWth","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD; (viii) Combined techniques for NOX and SOX reduction; (ix) Replacement or removal of the gas- gas heater located downstream of the wet FGD; (x) Fuel choice","mg/Nm3",135,200,"Green","Continuous ",0,0,0.06,"Daily",0]
["LCP","1. Energy industries","Unspecified","Unspecified","All","New","Solid biomass and/or peat","< 100 MWth","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3",15,"70","Green","Continuous ",0,0,0.06,"Yearly ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","New","Solid biomass and/or peat","< 100 MWth","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3",15,"70","Green","Continuous ",0,0,0.06,"Yearly ",0]
["LCP","1. Energy industries","Unspecified","Unspecified","All","New","Solid biomass and/or peat","< 100 MWth","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3",30,"175","Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","New","Solid biomass and/or peat","< 100 MWth","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3",30,"175","Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ",0]
["LCP","1. Energy industries","Unspecified","Unspecified","All","New","Solid biomass and/or peat","≥ 300 MWth","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3",10,"35","Green","Continuous ",0,0,0.06,"Yearly ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","New","Solid biomass and/or peat","≥ 300 MWth","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3",10,"35","Green","Continuous ",0,0,0.06,"Yearly ",0]
["LCP","1. Energy industries","Unspecified","Unspecified","All","New","Solid biomass and/or peat","≥ 300 MWth","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3",20,"70","Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","New","Solid biomass and/or peat","≥ 300 MWth","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3",20,"70","Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ",0]
["LCP","1. Energy industries","Unspecified","Unspecified","All","New","Solid biomass and/or peat","100-300 MWth","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3",10,"50","Green","Continuous ",0,0,0.06,"Yearly ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","New","Solid biomass and/or peat","100-300 MWth","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3",10,"50","Green","Continuous ",0,0,0.06,"Yearly ",0]
["LCP","1. Energy industries","Unspecified","Unspecified","All","New","Solid biomass and/or peat","100-300 MWth","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3",20,"85","Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","All","New","Solid biomass and/or peat","100-300 MWth","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi)Flue-gas condenser; (vii) Wet flue-gas desulphurisation (wet FGD); (viii) Fuel choice ","mg/Nm3",20,"85","Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ",0]
["LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Unspecified","100% iron and steel process gases ","Unspecified ","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX emissions to air from the combustion of iron and steel process gases, BAT is to use a combination of the techniques given below: (i) Process gas management system and auxiliary fuel choice; (ii) Coke oven gas pretreatment at the iron- and steel-works","mg/Nm3",25,"150","Green","Continuous ",0,0,0.03,"Yearly","For existing plants operated < 1 500 h/yr, these BAT AELs do not apply.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Unspecified","100% iron and steel process gases ","Unspecified ","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX emissions to air from the combustion of iron and steel process gases, BAT is to use a combination of the techniques given below: (i) Process gas management system and auxiliary fuel choice; (ii) Coke oven gas pretreatment at the iron- and steel-works","mg/Nm3",25,"150","Green","Continuous ",0,0,0.03,"Yearly","For existing plants operated < 1 500 h/yr, these BAT AELs do not apply."]
["LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Unspecified","100% iron and steel process gases ","Unspecified ","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX emissions to air from the combustion of iron and steel process gases, BAT is to use a combination of the techniques given below: (i) Process gas management system and auxiliary fuel choice; (ii) Coke oven gas pretreatment at the iron- and steel-works","mg/Nm3",50,"200","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ","For existing plants operated < 500 h/yr, these levels are indicative.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Unspecified","100% iron and steel process gases ","Unspecified ","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX emissions to air from the combustion of iron and steel process gases, BAT is to use a combination of the techniques given below: (i) Process gas management system and auxiliary fuel choice; (ii) Coke oven gas pretreatment at the iron- and steel-works","mg/Nm3",50,"200","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ","For existing plants operated < 500 h/yr, these levels are indicative."]
["LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Existing","100 % process fuels from the chemical industry","Unspecified ","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to reduce SOX, HCl and HF emissions to air from the combustion of process fuels from the chemical industry in boilers, BAT is to use one or a combination of the techniques given below: (i) Fuel choice; (ii) Boiler sorbent injection (in-furnace or in-bed); (iii) Duct sorbent injection (DSI); (iv) Spray dry absorber (SDA); (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD","mg/Nm3",90,"200","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ","For existing plants operated < 500 h/yr, these levels are indicative.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Existing","100 % process fuels from the chemical industry","Unspecified ","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to reduce SOX, HCl and HF emissions to air from the combustion of process fuels from the chemical industry in boilers, BAT is to use one or a combination of the techniques given below: (i) Fuel choice; (ii) Boiler sorbent injection (in-furnace or in-bed); (iii) Duct sorbent injection (DSI); (iv) Spray dry absorber (SDA); (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD","mg/Nm3",90,"200","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ","For existing plants operated < 500 h/yr, these levels are indicative."]
["LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Existing","HFO and/or gas oil in boilers","< 300 MWth ","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Duct sorbent injection (DSI); (ii) Spray dry absorber (SDA); (iii) Flue-gas condenser; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Seawater FGD; (vi) Fuel choice","mg/Nm3",50,"175","Green","Continuous ",0,0,0.03,"Yearly","These BAT-AELs do not apply to plants operated < 1 500 h/yr.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Existing","HFO and/or gas oil in boilers","< 300 MWth ","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Duct sorbent injection (DSI); (ii) Spray dry absorber (SDA); (iii) Flue-gas condenser; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Seawater FGD; (vi) Fuel choice","mg/Nm3",50,"175","Green","Continuous ",0,0,0.03,"Yearly","These BAT-AELs do not apply to plants operated < 1 500 h/yr."]
["LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Existing","HFO and/or gas oil in boilers","< 300 MWth ","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Duct sorbent injection (DSI); (ii) Spray dry absorber (SDA); (iii) Flue-gas condenser; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Seawater FGD; (vi) Fuel choice","mg/Nm3",150,"200","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ","For plants operated < 500 h/yr, these levels are indicative.\n\nFor industrial boilers and district heating plants put into operation no later than 27 November 2003 and operated < 1 500 h/yr, the higher end of the BAT-AEL range is 400 mg/Nm3.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Existing","HFO and/or gas oil in boilers","< 300 MWth ","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Duct sorbent injection (DSI); (ii) Spray dry absorber (SDA); (iii) Flue-gas condenser; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Seawater FGD; (vi) Fuel choice","mg/Nm3",150,"200","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ","For plants operated < 500 h/yr, these levels are indicative.\n\nFor industrial boilers and district heating plants put into operation no later than 27 November 2003 and operated < 1 500 h/yr, the higher end of the BAT-AEL range is 400 mg/Nm3."]
["LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Existing","HFO and/or gas oil in boilers","≥ 300 MWth","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Duct sorbent injection (DSI); (ii) Spray dry absorber (SDA); (iii) Flue-gas condenser; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Seawater FGD; (vi) Fuel choice","mg/Nm3",50,"110","Green","Continuous ",0,0,0.03,"Yearly","These BAT-AELs do not apply to plants operated < 1 500 h/yr.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Existing","HFO and/or gas oil in boilers","≥ 300 MWth","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Duct sorbent injection (DSI); (ii) Spray dry absorber (SDA); (iii) Flue-gas condenser; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Seawater FGD; (vi) Fuel choice","mg/Nm3",50,"110","Green","Continuous ",0,0,0.03,"Yearly","These BAT-AELs do not apply to plants operated < 1 500 h/yr."]
["LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Existing","HFO and/or gas oil in boilers","≥ 300 MWth","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Duct sorbent injection (DSI); (ii) Spray dry absorber (SDA); (iii) Flue-gas condenser; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Seawater FGD; (vi) Fuel choice","mg/Nm3",150,"165","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ","For plants operated < 500 h/yr, these levels are indicative.\n\nFor industrial boilers and district heating plants put into operation no later than 27 November 2003 and operated < 1 500 h/yr, the higher end of the BAT-AEL range is 400 mg/Nm3.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Existing","HFO and/or gas oil in boilers","≥ 300 MWth","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Duct sorbent injection (DSI); (ii) Spray dry absorber (SDA); (iii) Flue-gas condenser; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Seawater FGD; (vi) Fuel choice","mg/Nm3",150,"165","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ","For plants operated < 500 h/yr, these levels are indicative.\n\nFor industrial boilers and district heating plants put into operation no later than 27 November 2003 and operated < 1 500 h/yr, the higher end of the BAT-AEL range is 400 mg/Nm3."]
["LCP","1. Energy industries","Unspecified","Unspecified","Boilers","New","100 % process fuels from the chemical industry","Unspecified ","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to reduce SOX, HCl and HF emissions to air from the combustion of process fuels from the chemical industry in boilers, BAT is to use one or a combination of the techniques given below: (i) Fuel choice; (ii) Boiler sorbent injection (in-furnace or in-bed); (iii) Duct sorbent injection (DSI); (iv) Spray dry absorber (SDA); (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD","mg/Nm3",10,"110","Green","Continuous ",0,0,0.03,"Yearly","For existing plants operated < 1 500 h/yr, these BAT-AELs do not apply.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","New","100 % process fuels from the chemical industry","Unspecified ","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to reduce SOX, HCl and HF emissions to air from the combustion of process fuels from the chemical industry in boilers, BAT is to use one or a combination of the techniques given below: (i) Fuel choice; (ii) Boiler sorbent injection (in-furnace or in-bed); (iii) Duct sorbent injection (DSI); (iv) Spray dry absorber (SDA); (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD","mg/Nm3",10,"110","Green","Continuous ",0,0,0.03,"Yearly","For existing plants operated < 1 500 h/yr, these BAT-AELs do not apply."]
["LCP","1. Energy industries","Unspecified","Unspecified","Boilers","New","HFO and/or gas oil in boilers","< 300 MWth ","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Duct sorbent injection (DSI); (ii) Spray dry absorber (SDA); (iii) Flue-gas condenser; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Seawater FGD; (vi) Fuel choice","mg/Nm3",50,"175","Green","Continuous ",0,0,0.03,"Yearly",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","New","HFO and/or gas oil in boilers","< 300 MWth ","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Duct sorbent injection (DSI); (ii) Spray dry absorber (SDA); (iii) Flue-gas condenser; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Seawater FGD; (vi) Fuel choice","mg/Nm3",50,"175","Green","Continuous ",0,0,0.03,"Yearly",0]
["LCP","1. Energy industries","Unspecified","Unspecified","Boilers","New","HFO and/or gas oil in boilers","< 300 MWth ","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Duct sorbent injection (DSI); (ii) Spray dry absorber (SDA); (iii) Flue-gas condenser; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Seawater FGD; (vi) Fuel choice","mg/Nm3",150,"200","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","New","HFO and/or gas oil in boilers","< 300 MWth ","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Duct sorbent injection (DSI); (ii) Spray dry absorber (SDA); (iii) Flue-gas condenser; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Seawater FGD; (vi) Fuel choice","mg/Nm3",150,"200","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ",0]
["LCP","1. Energy industries","Unspecified","Unspecified","Boilers","New","HFO and/or gas oil in boilers","≥ 300 MWth","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Duct sorbent injection (DSI); (ii) Spray dry absorber (SDA); (iii) Flue-gas condenser; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Seawater FGD; (vi) Fuel choice","mg/Nm3",35,"50","Green","Continuous ",0,0,0.03,"Yearly",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","New","HFO and/or gas oil in boilers","≥ 300 MWth","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Duct sorbent injection (DSI); (ii) Spray dry absorber (SDA); (iii) Flue-gas condenser; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Seawater FGD; (vi) Fuel choice","mg/Nm3",35,"50","Green","Continuous ",0,0,0.03,"Yearly",0]
["LCP","1. Energy industries","Unspecified","Unspecified","Boilers","New","HFO and/or gas oil in boilers","≥ 300 MWth","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Duct sorbent injection (DSI); (ii) Spray dry absorber (SDA); (iii) Flue-gas condenser; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Seawater FGD; (vi) Fuel choice","mg/Nm3",50,"120","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","New","HFO and/or gas oil in boilers","≥ 300 MWth","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of HFO and/or gas oil in boilers, BAT is to use one or a combination of the techniques given below: (i) Duct sorbent injection (DSI); (ii) Spray dry absorber (SDA); (iii) Flue-gas condenser; (iv) Wet flue-gas desulphurisation (wet FGD); (v) Seawater FGD; (vi) Fuel choice","mg/Nm3",50,"120","Green","Continuous ",0,0,0.03,"Daily average or average over the sampling period ",0]
["LCP","1. Energy industries","Unspecified","Unspecified","CCGT","Unspecified","100% iron and steel process gases ","Unspecified ","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX emissions to air from the combustion of iron and steel process gases, BAT is to use a combination of the techniques given below: (i) Process gas management system and auxiliary fuel choice; (ii) Coke oven gas pretreatment at the iron- and steel-works","mg/Nm3",10,"45","Green","Continuous ",0,0,0.15,"Yearly","For existing plants operated < 1 500 h/yr, these BAT AELs do not apply.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","CCGT","Unspecified","100% iron and steel process gases ","Unspecified ","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX emissions to air from the combustion of iron and steel process gases, BAT is to use a combination of the techniques given below: (i) Process gas management system and auxiliary fuel choice; (ii) Coke oven gas pretreatment at the iron- and steel-works","mg/Nm3",10,"45","Green","Continuous ",0,0,0.15,"Yearly","For existing plants operated < 1 500 h/yr, these BAT AELs do not apply."]
["LCP","1. Energy industries","Unspecified","Unspecified","CCGT","Unspecified","100% iron and steel process gases ","Unspecified ","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX emissions to air from the combustion of iron and steel process gases, BAT is to use a combination of the techniques given below: (i) Process gas management system and auxiliary fuel choice; (ii) Coke oven gas pretreatment at the iron- and steel-works","mg/Nm3",20,"70","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period ","For existing plants operated < 500 h/yr, these levels are indicative.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","CCGT","Unspecified","100% iron and steel process gases ","Unspecified ","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX emissions to air from the combustion of iron and steel process gases, BAT is to use a combination of the techniques given below: (i) Process gas management system and auxiliary fuel choice; (ii) Coke oven gas pretreatment at the iron- and steel-works","mg/Nm3",20,"70","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period ","For existing plants operated < 500 h/yr, these levels are indicative."]
["LCP","1. Energy industries","Unspecified","Unspecified","Fired engines ","Existing","HFO and/or gas oil in reciprocating engines","All sizes","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of HFO and/or gas oil in reciprocating engines, BAT is to use one or a combination of the techniques given below: (i) Fuel choice; (ii) Duct sorbent injection (DSI); (iii) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",100,"200","Green","Continuous ",0,0,0.15,"Yearly","These BAT-AELs do not apply to plants operated < 1 500 h/yr.\n\nThe higher end of the BAT-AEL range is 280 mg/Nm3 if no secondary abatement technique can be applied. This corresponds to a sulphur content of the fuel of 0,5 wt-% (dry).",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Fired engines ","Existing","HFO and/or gas oil in reciprocating engines","All sizes","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of HFO and/or gas oil in reciprocating engines, BAT is to use one or a combination of the techniques given below: (i) Fuel choice; (ii) Duct sorbent injection (DSI); (iii) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",100,"200","Green","Continuous ",0,0,0.15,"Yearly","These BAT-AELs do not apply to plants operated < 1 500 h/yr.\n\nThe higher end of the BAT-AEL range is 280 mg/Nm3 if no secondary abatement technique can be applied. This corresponds to a sulphur content of the fuel of 0,5 wt-% (dry)."]
["LCP","1. Energy industries","Unspecified","Unspecified","Fired engines ","Existing","HFO and/or gas oil in reciprocating engines","All sizes","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of HFO and/or gas oil in reciprocating engines, BAT is to use one or a combination of the techniques given below: (i) Fuel choice; (ii) Duct sorbent injection (DSI); (iii) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",105,"235","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period ","For plants operated < 500 h/yr, these levels are indicative.\n\nThe higher end of the BAT-AEL range is 280 mg/Nm3 if no secondary abatement technique can be applied. This corresponds to a sulphur content of the fuel of 0,5 wt-% (dry).",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Fired engines ","Existing","HFO and/or gas oil in reciprocating engines","All sizes","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of HFO and/or gas oil in reciprocating engines, BAT is to use one or a combination of the techniques given below: (i) Fuel choice; (ii) Duct sorbent injection (DSI); (iii) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",105,"235","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period ","For plants operated < 500 h/yr, these levels are indicative.\n\nThe higher end of the BAT-AEL range is 280 mg/Nm3 if no secondary abatement technique can be applied. This corresponds to a sulphur content of the fuel of 0,5 wt-% (dry)."]
["LCP","1. Energy industries","Unspecified","Unspecified","Fired engines ","New","HFO and/or gas oil in reciprocating engines","All sizes","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of HFO and/or gas oil in reciprocating engines, BAT is to use one or a combination of the techniques given below: (i) Fuel choice; (ii) Duct sorbent injection (DSI); (iii) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",45,"100","Green","Continuous ",0,0,0.15,"Yearly",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Fired engines ","New","HFO and/or gas oil in reciprocating engines","All sizes","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of HFO and/or gas oil in reciprocating engines, BAT is to use one or a combination of the techniques given below: (i) Fuel choice; (ii) Duct sorbent injection (DSI); (iii) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",45,"100","Green","Continuous ",0,0,0.15,"Yearly",0]
["LCP","1. Energy industries","Unspecified","Unspecified","Fired engines ","New","HFO and/or gas oil in reciprocating engines","All sizes","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of HFO and/or gas oil in reciprocating engines, BAT is to use one or a combination of the techniques given below: (i) Fuel choice; (ii) Duct sorbent injection (DSI); (iii) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",60,"110","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Fired engines ","New","HFO and/or gas oil in reciprocating engines","All sizes","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of HFO and/or gas oil in reciprocating engines, BAT is to use one or a combination of the techniques given below: (i) Fuel choice; (ii) Duct sorbent injection (DSI); (iii) Wet flue-gas desulphurisation (wet FGD)","mg/Nm3",60,"110","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period ",0]
["LCP","1. Energy industries","Unspecified","Unspecified","Fluidised bed boiler","Existing","Coal and/or lignite ","≥ 300 MWth","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD; (viii) Combined techniques for NOX and SOX reduction; (ix) Replacement or removal of the gas- gas heater located downstream of the wet FGD; (x) Fuel choice","mg/Nm3",20,180,"Green","Continuous ",0,0,0.06,"Yearly","For circulating fluidised bed boilers, the lower end of the range can be achieved by using high-efficiency wet FGD. The higher end of the range can be achieved by using boiler in-bed sorbent injection.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Fluidised bed boiler","Existing","Coal and/or lignite ","≥ 300 MWth","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD; (viii) Combined techniques for NOX and SOX reduction; (ix) Replacement or removal of the gas- gas heater located downstream of the wet FGD; (x) Fuel choice","mg/Nm3",20,180,"Green","Continuous ",0,0,0.06,"Yearly","For circulating fluidised bed boilers, the lower end of the range can be achieved by using high-efficiency wet FGD. The higher end of the range can be achieved by using boiler in-bed sorbent injection."]
["LCP","1. Energy industries","Unspecified","Unspecified","Fluidised bed boiler","Existing","Coal and/or lignite ","≥ 300 MWth","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD; (viii) Combined techniques for NOX and SOX reduction; (ix) Replacement or removal of the gas- gas heater located downstream of the wet FGD; (x) Fuel choice","mg/Nm3",50,220,"Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ","For circulating fluidised bed boilers, the lower end of the range can be achieved by using high-efficiency wet FGD. The higher end of the range can be achieved by using boiler in-bed sorbent injection.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Fluidised bed boiler","Existing","Coal and/or lignite ","≥ 300 MWth","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD; (viii) Combined techniques for NOX and SOX reduction; (ix) Replacement or removal of the gas- gas heater located downstream of the wet FGD; (x) Fuel choice","mg/Nm3",50,220,"Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ","For circulating fluidised bed boilers, the lower end of the range can be achieved by using high-efficiency wet FGD. The higher end of the range can be achieved by using boiler in-bed sorbent injection."]
["LCP","1. Energy industries","Unspecified","Unspecified","Fluidised bed boiler","New","Coal and/or lignite ","≥ 300 MWth","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD; (viii) Combined techniques for NOX and SOX reduction; (ix) Replacement or removal of the gas- gas heater located downstream of the wet FGD; (x) Fuel choice","mg/Nm3",20,75,"Green","Continuous ",0,0,0.06,"Yearly","For circulating fluidised bed boilers, the lower end of the range can be achieved by using high-efficiency wet FGD. The higher end of the range can be achieved by using boiler in-bed sorbent injection.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Fluidised bed boiler","New","Coal and/or lignite ","≥ 300 MWth","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD; (viii) Combined techniques for NOX and SOX reduction; (ix) Replacement or removal of the gas- gas heater located downstream of the wet FGD; (x) Fuel choice","mg/Nm3",20,75,"Green","Continuous ",0,0,0.06,"Yearly","For circulating fluidised bed boilers, the lower end of the range can be achieved by using high-efficiency wet FGD. The higher end of the range can be achieved by using boiler in-bed sorbent injection."]
["LCP","1. Energy industries","Unspecified","Unspecified","Fluidised bed boiler","New","Coal and/or lignite ","≥ 300 MWth","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD; (viii) Combined techniques for NOX and SOX reduction; (ix) Replacement or removal of the gas- gas heater located downstream of the wet FGD; (x) Fuel choice","mg/Nm3",25,110,"Green","Continuous ",0,0,0.06,"Daily","For circulating fluidised bed boilers, the lower end of the range can be achieved by using high-efficiency wet FGD. The higher end of the range can be achieved by using boiler in-bed sorbent injection.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Fluidised bed boiler","New","Coal and/or lignite ","≥ 300 MWth","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD; (viii) Combined techniques for NOX and SOX reduction; (ix) Replacement or removal of the gas- gas heater located downstream of the wet FGD; (x) Fuel choice","mg/Nm3",25,110,"Green","Continuous ",0,0,0.06,"Daily","For circulating fluidised bed boilers, the lower end of the range can be achieved by using high-efficiency wet FGD. The higher end of the range can be achieved by using boiler in-bed sorbent injection."]
["LCP","1. Energy industries","Unspecified","Unspecified","Gas turbines (including dual fuel turbines) ","Newand Existing","Gas oil ","Unspecified ","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX and dust emissions to air from the combustion of gas oil in gas turbines, BAT is to use the technique given below: Fuel choice","mg/Nm3",35,"60","Green","Continuous ",0,0,0.15,"Yearly","These BAT-AELs do not apply to existing plants operated < 1 500 h/yr.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Gas turbines (including dual fuel turbines) ","Newand Existing","Gas oil ","Unspecified ","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX and dust emissions to air from the combustion of gas oil in gas turbines, BAT is to use the technique given below: Fuel choice","mg/Nm3",35,"60","Green","Continuous ",0,0,0.15,"Yearly","These BAT-AELs do not apply to existing plants operated < 1 500 h/yr."]
["LCP","1. Energy industries","Unspecified","Unspecified","Gas turbines (including dual fuel turbines) ","Newand Existing","Gas oil ","Unspecified ","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX and dust emissions to air from the combustion of gas oil in gas turbines, BAT is to use the technique given below: Fuel choice","mg/Nm3",50,"66","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period ","For existing plants operated < 500 h/yr, these levels are indicative.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Gas turbines (including dual fuel turbines) ","Newand Existing","Gas oil ","Unspecified ","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX and dust emissions to air from the combustion of gas oil in gas turbines, BAT is to use the technique given below: Fuel choice","mg/Nm3",50,"66","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period ","For existing plants operated < 500 h/yr, these levels are indicative."]
["LCP","1. Energy industries","Unspecified","Unspecified","Gas turbines (including dual fuel turbines) ","Newand Existing","Gas oil ","Unspecified ","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX and dust emissions to air from the combustion of gas oil in gas turbines, BAT is to use the technique given below: Fuel choice","mg/Nm3",2,"5","Green","Continuous ",0,0,0.15,"Yearly","These BAT-AELs do not apply to existing plants operated < 1 500 h/yr.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Gas turbines (including dual fuel turbines) ","Newand Existing","Gas oil ","Unspecified ","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX and dust emissions to air from the combustion of gas oil in gas turbines, BAT is to use the technique given below: Fuel choice","mg/Nm3",2,"5","Green","Continuous ",0,0,0.15,"Yearly","These BAT-AELs do not apply to existing plants operated < 1 500 h/yr."]
["LCP","1. Energy industries","Unspecified","Unspecified","Gas turbines (including dual fuel turbines) ","Newand Existing","Gas oil ","Unspecified ","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX and dust emissions to air from the combustion of gas oil in gas turbines, BAT is to use the technique given below: Fuel choice","mg/Nm3",2,"10","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period ","For existing plants operated < 500 h/yr, these levels are indicative.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Gas turbines (including dual fuel turbines) ","Newand Existing","Gas oil ","Unspecified ","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX and dust emissions to air from the combustion of gas oil in gas turbines, BAT is to use the technique given below: Fuel choice","mg/Nm3",2,"10","Green","Continuous ",0,0,0.15,"Daily average or average over the sampling period ","For existing plants operated < 500 h/yr, these levels are indicative."]
["LCP","1. Energy industries","Unspecified","Unspecified","IGCC","Unspecified","Unspecified","≥ 100 MWth","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to reduce SOX emissions to air from IGCC plants, BAT is to use the technique given below: Acid gas removal","mg/Nm3",3,"16","Green","Continuous",0,0,0.15,"Yearly",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","IGCC","Unspecified","Unspecified","≥ 100 MWth","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to reduce SOX emissions to air from IGCC plants, BAT is to use the technique given below: Acid gas removal","mg/Nm3",3,"16","Green","Continuous",0,0,0.15,"Yearly",0]
["LCP","1. Energy industries","Unspecified","Unspecified","PC boiler ","Existing","Coal and/or lignite ","≥ 300 MWth","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD; (viii) Combined techniques for NOX and SOX reduction; (ix) Replacement or removal of the gas- gas heater located downstream of the wet FGD; (x) Fuel choice","mg/Nm3",10,130,"Green","Continuous ",0,0,0.06,"Yearly","The lower end of the range can be achieved with the use of low-sulphur fuels in combination with the most advanced wet abatement system designs.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","PC boiler ","Existing","Coal and/or lignite ","≥ 300 MWth","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD; (viii) Combined techniques for NOX and SOX reduction; (ix) Replacement or removal of the gas- gas heater located downstream of the wet FGD; (x) Fuel choice","mg/Nm3",10,130,"Green","Continuous ",0,0,0.06,"Yearly","The lower end of the range can be achieved with the use of low-sulphur fuels in combination with the most advanced wet abatement system designs."]
["LCP","1. Energy industries","Unspecified","Unspecified","PC boiler ","Existing","Coal and/or lignite ","≥ 300 MWth","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD; (viii) Combined techniques for NOX and SOX reduction; (ix) Replacement or removal of the gas- gas heater located downstream of the wet FGD; (x) Fuel choice","mg/Nm3",25,165,"Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ","The higher end of the BAT-AEL range is 220 mg/Nm3 in the case of plants put into operation no later than 7 January 2014 and operated < 1 500 h/yr. For other existing plants put into operation no later than 7 January 2014, the higher end of the BAT-AEL range is 205 mg/Nm3.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","PC boiler ","Existing","Coal and/or lignite ","≥ 300 MWth","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD; (viii) Combined techniques for NOX and SOX reduction; (ix) Replacement or removal of the gas- gas heater located downstream of the wet FGD; (x) Fuel choice","mg/Nm3",25,165,"Green","Continuous ",0,0,0.06,"Daily average or average over the sampling period ","The higher end of the BAT-AEL range is 220 mg/Nm3 in the case of plants put into operation no later than 7 January 2014 and operated < 1 500 h/yr. For other existing plants put into operation no later than 7 January 2014, the higher end of the BAT-AEL range is 205 mg/Nm3."]
["LCP","1. Energy industries","Unspecified","Unspecified","PC boiler ","New","Coal and/or lignite ","≥ 300 MWth","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD; (viii) Combined techniques for NOX and SOX reduction; (ix) Replacement or removal of the gas- gas heater located downstream of the wet FGD; (x) Fuel choice","mg/Nm3",10,75,"Green","Continuous ",0,0,0.06,"Yearly",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","PC boiler ","New","Coal and/or lignite ","≥ 300 MWth","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD; (viii) Combined techniques for NOX and SOX reduction; (ix) Replacement or removal of the gas- gas heater located downstream of the wet FGD; (x) Fuel choice","mg/Nm3",10,75,"Green","Continuous ",0,0,0.06,"Yearly",0]
["LCP","1. Energy industries","Unspecified","Unspecified","PC boiler ","New","Coal and/or lignite ","≥ 300 MWth","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD; (viii) Combined techniques for NOX and SOX reduction; (ix) Replacement or removal of the gas- gas heater located downstream of the wet FGD; (x) Fuel choice","mg/Nm3",25,110,"Green","Continuous ",0,0,0.06,"Daily",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","PC boiler ","New","Coal and/or lignite ","≥ 300 MWth","Unspecified","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below: (i) Boiler sorbent injection (in-furnace or in-bed); (ii) Duct sorbent injection (DSI); (iii) Spray dry absorber (SDA); (iv) Circulating fluidised bed (CFB) dry scrubber; (v) Wet scrubbing; (vi) Wet flue-gas desulphurisation (wet FGD); (vii) Seawater FGD; (viii) Combined techniques for NOX and SOX reduction; (ix) Replacement or removal of the gas- gas heater located downstream of the wet FGD; (x) Fuel choice","mg/Nm3",25,110,"Green","Continuous ",0,0,0.06,"Daily",0]
["LCP","1. Energy industries","Unspecified","Unspecified","Biomass-, peat-, coal- and/or lignite-fired combustion plant","Unspecified","Co-incineration of waste with biomass, peat, coal and/or lignite","Unspecified ","Unspecified","Air","VOC","In order to reduce emissions of volatile organic compounds and polychlorinated dibenzo-dioxins and -furans to air from the co-incineration of waste with biomass, peat, coal and/or lignite, BAT is to use a combination of the techniques given in BAT 6, BAT 26 and below: (i) Activated carbon injection; (ii) Rapid quenching using wet scrubbing/flue-gas condenser; (iii) Selective catalytic reduction (SCR)","mg/Nm3",0.1,"5","Green","Continuous",0,0,0.06,"Yearly",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Biomass-, peat-, coal- and/or lignite-fired combustion plant","Unspecified","Co-incineration of waste with biomass, peat, coal and/or lignite","Unspecified ","Unspecified","Air","VOC","In order to reduce emissions of volatile organic compounds and polychlorinated dibenzo-dioxins and -furans to air from the co-incineration of waste with biomass, peat, coal and/or lignite, BAT is to use a combination of the techniques given in BAT 6, BAT 26 and below: (i) Activated carbon injection; (ii) Rapid quenching using wet scrubbing/flue-gas condenser; (iii) Selective catalytic reduction (SCR)","mg/Nm3",0.1,"5","Green","Continuous",0,0,0.06,"Yearly",0]
["LCP","1. Energy industries","Unspecified","Unspecified","Biomass-, peat-, coal- and/or lignite-fired combustion plant","Unspecified","Co-incineration of waste with biomass, peat, coal and/or lignite","Unspecified ","Unspecified","Air","VOC","In order to reduce emissions of volatile organic compounds and polychlorinated dibenzo-dioxins and -furans to air from the co-incineration of waste with biomass, peat, coal and/or lignite, BAT is to use a combination of the techniques given in BAT 6, BAT 26 and below: (i) Activated carbon injection; (ii) Rapid quenching using wet scrubbing/flue-gas condenser; (iii) Selective catalytic reduction (SCR)","mg/Nm3",0.5,"10","Green","Continuous",0,0,0.06,"Daily",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Biomass-, peat-, coal- and/or lignite-fired combustion plant","Unspecified","Co-incineration of waste with biomass, peat, coal and/or lignite","Unspecified ","Unspecified","Air","VOC","In order to reduce emissions of volatile organic compounds and polychlorinated dibenzo-dioxins and -furans to air from the co-incineration of waste with biomass, peat, coal and/or lignite, BAT is to use a combination of the techniques given in BAT 6, BAT 26 and below: (i) Activated carbon injection; (ii) Rapid quenching using wet scrubbing/flue-gas condenser; (iii) Selective catalytic reduction (SCR)","mg/Nm3",0.5,"10","Green","Continuous",0,0,0.06,"Daily",0]
["LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Unspecified","100 % process fuels from the chemical industry","Unspecified ","Unspecified","Air","VOC","In order to reduce emissions to air of volatile organic compounds and polychlorinated dibenzo- dioxins and -furans from the combustion of process fuels from the chemical industry in boilers, BAT is to use one or a combination of the techniques given in BAT 6 and below: (i) Activated carbon injection; (ii) Rapid quenching using wet scrubbing/flue-gas condenser; (iii) Selective catalytic reduction (SCR)","mg/Nm3",0.6,"12","Green","Once every 6 months",0,0,0.03,"Average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Boilers","Unspecified","100 % process fuels from the chemical industry","Unspecified ","Unspecified","Air","VOC","In order to reduce emissions to air of volatile organic compounds and polychlorinated dibenzo- dioxins and -furans from the combustion of process fuels from the chemical industry in boilers, BAT is to use one or a combination of the techniques given in BAT 6 and below: (i) Activated carbon injection; (ii) Rapid quenching using wet scrubbing/flue-gas condenser; (iii) Selective catalytic reduction (SCR)","mg/Nm3",0.6,"12","Green","Once every 6 months",0,0,0.03,"Average over the sampling period",0]
["LCP","1. Energy industries","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water from flue-gas treatment, BAT is to use an appropriate combination of the techniques given below, and to use secondary techniques as close as possible to the source in order to avoid dilution: (i) Optimised combustion (see BAT 6) and flue-gas treatment systems (e.g. SCR/SNCR, see BAT 7); (ii) Adsorption on activated carbon; (iii) Aerobic biological treatment; (iv) Anoxic/anaerobic biological treatment; (v) Coagulation and flocculation; (vi) Crystallisation; (vii) Filtration (e.g. sand filtration, microfiltration, ultrafiltration); (viii) Flotation; (ix) Ion exchange; (x) Neutralisation; (xi) Oxidation; (xii) Precipitation; (xiii) Sedimentation; (xiv) Stripping","ug/l",10,50,"Green","Once every month",0,0,"Unspecified ","Daily ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water from flue-gas treatment, BAT is to use an appropriate combination of the techniques given below, and to use secondary techniques as close as possible to the source in order to avoid dilution: (i) Optimised combustion (see BAT 6) and flue-gas treatment systems (e.g. SCR/SNCR, see BAT 7); (ii) Adsorption on activated carbon; (iii) Aerobic biological treatment; (iv) Anoxic/anaerobic biological treatment; (v) Coagulation and flocculation; (vi) Crystallisation; (vii) Filtration (e.g. sand filtration, microfiltration, ultrafiltration); (viii) Flotation; (ix) Ion exchange; (x) Neutralisation; (xi) Oxidation; (xii) Precipitation; (xiii) Sedimentation; (xiv) Stripping","ug/l",10,50,"Green","Once every month",0,0,"Unspecified ","Daily ",0]
["LCP","1. Energy industries","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water from flue-gas treatment, BAT is to use an appropriate combination of the techniques given below, and to use secondary techniques as close as possible to the source in order to avoid dilution: (i) Optimised combustion (see BAT 6) and flue-gas treatment systems (e.g. SCR/SNCR, see BAT 7); (ii) Adsorption on activated carbon; (iii) Aerobic biological treatment; (iv) Anoxic/anaerobic biological treatment; (v) Coagulation and flocculation; (vi) Crystallisation; (vii) Filtration (e.g. sand filtration, microfiltration, ultrafiltration); (viii) Flotation; (ix) Ion exchange; (x) Neutralisation; (xi) Oxidation; (xii) Precipitation; (xiii) Sedimentation; (xiv) Stripping","ug/l",2,5,"Green","Once every month",0,0,"Unspecified ","Daily ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water from flue-gas treatment, BAT is to use an appropriate combination of the techniques given below, and to use secondary techniques as close as possible to the source in order to avoid dilution: (i) Optimised combustion (see BAT 6) and flue-gas treatment systems (e.g. SCR/SNCR, see BAT 7); (ii) Adsorption on activated carbon; (iii) Aerobic biological treatment; (iv) Anoxic/anaerobic biological treatment; (v) Coagulation and flocculation; (vi) Crystallisation; (vii) Filtration (e.g. sand filtration, microfiltration, ultrafiltration); (viii) Flotation; (ix) Ion exchange; (x) Neutralisation; (xi) Oxidation; (xii) Precipitation; (xiii) Sedimentation; (xiv) Stripping","ug/l",2,5,"Green","Once every month",0,0,"Unspecified ","Daily ",0]
["LCP","1. Energy industries","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water from flue-gas treatment, BAT is to use an appropriate combination of the techniques given below, and to use secondary techniques as close as possible to the source in order to avoid dilution: (i) Optimised combustion (see BAT 6) and flue-gas treatment systems (e.g. SCR/SNCR, see BAT 7); (ii) Adsorption on activated carbon; (iii) Aerobic biological treatment; (iv) Anoxic/anaerobic biological treatment; (v) Coagulation and flocculation; (vi) Crystallisation; (vii) Filtration (e.g. sand filtration, microfiltration, ultrafiltration); (viii) Flotation; (ix) Ion exchange; (x) Neutralisation; (xi) Oxidation; (xii) Precipitation; (xiii) Sedimentation; (xiv) Stripping","mg/l",60,150,"Green","Once every month",0,0,"Unspecified ","Daily ","Either the BAT-AEL for TOC or the BAT-AEL for COD applies. TOC is the preferred option because its monitoring does not rely on the use of very toxic compounds.\n\nThis BAT-AEL applies after subtraction of the intake load.\n\nThis BAT-AEL only applies to waste water from the use of wet FGD.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water from flue-gas treatment, BAT is to use an appropriate combination of the techniques given below, and to use secondary techniques as close as possible to the source in order to avoid dilution: (i) Optimised combustion (see BAT 6) and flue-gas treatment systems (e.g. SCR/SNCR, see BAT 7); (ii) Adsorption on activated carbon; (iii) Aerobic biological treatment; (iv) Anoxic/anaerobic biological treatment; (v) Coagulation and flocculation; (vi) Crystallisation; (vii) Filtration (e.g. sand filtration, microfiltration, ultrafiltration); (viii) Flotation; (ix) Ion exchange; (x) Neutralisation; (xi) Oxidation; (xii) Precipitation; (xiii) Sedimentation; (xiv) Stripping","mg/l",60,150,"Green","Once every month",0,0,"Unspecified ","Daily ","Either the BAT-AEL for TOC or the BAT-AEL for COD applies. TOC is the preferred option because its monitoring does not rely on the use of very toxic compounds.\n\nThis BAT-AEL applies after subtraction of the intake load.\n\nThis BAT-AEL only applies to waste water from the use of wet FGD."]
["LCP","1. Energy industries","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water from flue-gas treatment, BAT is to use an appropriate combination of the techniques given below, and to use secondary techniques as close as possible to the source in order to avoid dilution: (i) Optimised combustion (see BAT 6) and flue-gas treatment systems (e.g. SCR/SNCR, see BAT 7); (ii) Adsorption on activated carbon; (iii) Aerobic biological treatment; (iv) Anoxic/anaerobic biological treatment; (v) Coagulation and flocculation; (vi) Crystallisation; (vii) Filtration (e.g. sand filtration, microfiltration, ultrafiltration); (viii) Flotation; (ix) Ion exchange; (x) Neutralisation; (xi) Oxidation; (xii) Precipitation; (xiii) Sedimentation; (xiv) Stripping","ug/l",10,50,"Green","Once every month",0,0,"Unspecified ","Daily ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water from flue-gas treatment, BAT is to use an appropriate combination of the techniques given below, and to use secondary techniques as close as possible to the source in order to avoid dilution: (i) Optimised combustion (see BAT 6) and flue-gas treatment systems (e.g. SCR/SNCR, see BAT 7); (ii) Adsorption on activated carbon; (iii) Aerobic biological treatment; (iv) Anoxic/anaerobic biological treatment; (v) Coagulation and flocculation; (vi) Crystallisation; (vii) Filtration (e.g. sand filtration, microfiltration, ultrafiltration); (viii) Flotation; (ix) Ion exchange; (x) Neutralisation; (xi) Oxidation; (xii) Precipitation; (xiii) Sedimentation; (xiv) Stripping","ug/l",10,50,"Green","Once every month",0,0,"Unspecified ","Daily ",0]
["LCP","1. Energy industries","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water from flue-gas treatment, BAT is to use an appropriate combination of the techniques given below, and to use secondary techniques as close as possible to the source in order to avoid dilution: (i) Optimised combustion (see BAT 6) and flue-gas treatment systems (e.g. SCR/SNCR, see BAT 7); (ii) Adsorption on activated carbon; (iii) Aerobic biological treatment; (iv) Anoxic/anaerobic biological treatment; (v) Coagulation and flocculation; (vi) Crystallisation; (vii) Filtration (e.g. sand filtration, microfiltration, ultrafiltration); (viii) Flotation; (ix) Ion exchange; (x) Neutralisation; (xi) Oxidation; (xii) Precipitation; (xiii) Sedimentation; (xiv) Stripping","ug/l",10,50,"Green","Once every month",0,0,"Unspecified ","Daily ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water from flue-gas treatment, BAT is to use an appropriate combination of the techniques given below, and to use secondary techniques as close as possible to the source in order to avoid dilution: (i) Optimised combustion (see BAT 6) and flue-gas treatment systems (e.g. SCR/SNCR, see BAT 7); (ii) Adsorption on activated carbon; (iii) Aerobic biological treatment; (iv) Anoxic/anaerobic biological treatment; (v) Coagulation and flocculation; (vi) Crystallisation; (vii) Filtration (e.g. sand filtration, microfiltration, ultrafiltration); (viii) Flotation; (ix) Ion exchange; (x) Neutralisation; (xi) Oxidation; (xii) Precipitation; (xiii) Sedimentation; (xiv) Stripping","ug/l",10,50,"Green","Once every month",0,0,"Unspecified ","Daily ",0]
["LCP","1. Energy industries","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water from flue-gas treatment, BAT is to use an appropriate combination of the techniques given below, and to use secondary techniques as close as possible to the source in order to avoid dilution: (i) Optimised combustion (see BAT 6) and flue-gas treatment systems (e.g. SCR/SNCR, see BAT 7); (ii) Adsorption on activated carbon; (iii) Aerobic biological treatment; (iv) Anoxic/anaerobic biological treatment; (v) Coagulation and flocculation; (vi) Crystallisation; (vii) Filtration (e.g. sand filtration, microfiltration, ultrafiltration); (viii) Flotation; (ix) Ion exchange; (x) Neutralisation; (xi) Oxidation; (xii) Precipitation; (xiii) Sedimentation; (xiv) Stripping","mg/l",10,25,"Green","Once every month",0,0,"Unspecified ","Daily ","This BAT-AEL only applies to waste water from the use of wet FGD.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water from flue-gas treatment, BAT is to use an appropriate combination of the techniques given below, and to use secondary techniques as close as possible to the source in order to avoid dilution: (i) Optimised combustion (see BAT 6) and flue-gas treatment systems (e.g. SCR/SNCR, see BAT 7); (ii) Adsorption on activated carbon; (iii) Aerobic biological treatment; (iv) Anoxic/anaerobic biological treatment; (v) Coagulation and flocculation; (vi) Crystallisation; (vii) Filtration (e.g. sand filtration, microfiltration, ultrafiltration); (viii) Flotation; (ix) Ion exchange; (x) Neutralisation; (xi) Oxidation; (xii) Precipitation; (xiii) Sedimentation; (xiv) Stripping","mg/l",10,25,"Green","Once every month",0,0,"Unspecified ","Daily ","This BAT-AEL only applies to waste water from the use of wet FGD."]
["LCP","1. Energy industries","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water from flue-gas treatment, BAT is to use an appropriate combination of the techniques given below, and to use secondary techniques as close as possible to the source in order to avoid dilution: (i) Optimised combustion (see BAT 6) and flue-gas treatment systems (e.g. SCR/SNCR, see BAT 7); (ii) Adsorption on activated carbon; (iii) Aerobic biological treatment; (iv) Anoxic/anaerobic biological treatment; (v) Coagulation and flocculation; (vi) Crystallisation; (vii) Filtration (e.g. sand filtration, microfiltration, ultrafiltration); (viii) Flotation; (ix) Ion exchange; (x) Neutralisation; (xi) Oxidation; (xii) Precipitation; (xiii) Sedimentation; (xiv) Stripping","ug/l",0.2,3,"Green","Once every month",0,0,"Unspecified ","Daily ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water from flue-gas treatment, BAT is to use an appropriate combination of the techniques given below, and to use secondary techniques as close as possible to the source in order to avoid dilution: (i) Optimised combustion (see BAT 6) and flue-gas treatment systems (e.g. SCR/SNCR, see BAT 7); (ii) Adsorption on activated carbon; (iii) Aerobic biological treatment; (iv) Anoxic/anaerobic biological treatment; (v) Coagulation and flocculation; (vi) Crystallisation; (vii) Filtration (e.g. sand filtration, microfiltration, ultrafiltration); (viii) Flotation; (ix) Ion exchange; (x) Neutralisation; (xi) Oxidation; (xii) Precipitation; (xiii) Sedimentation; (xiv) Stripping","ug/l",0.2,3,"Green","Once every month",0,0,"Unspecified ","Daily ",0]
["LCP","1. Energy industries","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water from flue-gas treatment, BAT is to use an appropriate combination of the techniques given below, and to use secondary techniques as close as possible to the source in order to avoid dilution: (i) Optimised combustion (see BAT 6) and flue-gas treatment systems (e.g. SCR/SNCR, see BAT 7); (ii) Adsorption on activated carbon; (iii) Aerobic biological treatment; (iv) Anoxic/anaerobic biological treatment; (v) Coagulation and flocculation; (vi) Crystallisation; (vii) Filtration (e.g. sand filtration, microfiltration, ultrafiltration); (viii) Flotation; (ix) Ion exchange; (x) Neutralisation; (xi) Oxidation; (xii) Precipitation; (xiii) Sedimentation; (xiv) Stripping","ug/l",10,50,"Green","Once every month",0,0,"Unspecified ","Daily ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water from flue-gas treatment, BAT is to use an appropriate combination of the techniques given below, and to use secondary techniques as close as possible to the source in order to avoid dilution: (i) Optimised combustion (see BAT 6) and flue-gas treatment systems (e.g. SCR/SNCR, see BAT 7); (ii) Adsorption on activated carbon; (iii) Aerobic biological treatment; (iv) Anoxic/anaerobic biological treatment; (v) Coagulation and flocculation; (vi) Crystallisation; (vii) Filtration (e.g. sand filtration, microfiltration, ultrafiltration); (viii) Flotation; (ix) Ion exchange; (x) Neutralisation; (xi) Oxidation; (xii) Precipitation; (xiii) Sedimentation; (xiv) Stripping","ug/l",10,50,"Green","Once every month",0,0,"Unspecified ","Daily ",0]
["LCP","1. Energy industries","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water from flue-gas treatment, BAT is to use an appropriate combination of the techniques given below, and to use secondary techniques as close as possible to the source in order to avoid dilution: (i) Optimised combustion (see BAT 6) and flue-gas treatment systems (e.g. SCR/SNCR, see BAT 7); (ii) Adsorption on activated carbon; (iii) Aerobic biological treatment; (iv) Anoxic/anaerobic biological treatment; (v) Coagulation and flocculation; (vi) Crystallisation; (vii) Filtration (e.g. sand filtration, microfiltration, ultrafiltration); (viii) Flotation; (ix) Ion exchange; (x) Neutralisation; (xi) Oxidation; (xii) Precipitation; (xiii) Sedimentation; (xiv) Stripping","ug/l",10,20,"Green","Once every month",0,0,"Unspecified ","Daily ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water from flue-gas treatment, BAT is to use an appropriate combination of the techniques given below, and to use secondary techniques as close as possible to the source in order to avoid dilution: (i) Optimised combustion (see BAT 6) and flue-gas treatment systems (e.g. SCR/SNCR, see BAT 7); (ii) Adsorption on activated carbon; (iii) Aerobic biological treatment; (iv) Anoxic/anaerobic biological treatment; (v) Coagulation and flocculation; (vi) Crystallisation; (vii) Filtration (e.g. sand filtration, microfiltration, ultrafiltration); (viii) Flotation; (ix) Ion exchange; (x) Neutralisation; (xi) Oxidation; (xii) Precipitation; (xiii) Sedimentation; (xiv) Stripping","ug/l",10,20,"Green","Once every month",0,0,"Unspecified ","Daily ",0]
["LCP","1. Energy industries","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water from flue-gas treatment, BAT is to use an appropriate combination of the techniques given below, and to use secondary techniques as close as possible to the source in order to avoid dilution: (i) Optimised combustion (see BAT 6) and flue-gas treatment systems (e.g. SCR/SNCR, see BAT 7); (ii) Adsorption on activated carbon; (iii) Aerobic biological treatment; (iv) Anoxic/anaerobic biological treatment; (v) Coagulation and flocculation; (vi) Crystallisation; (vii) Filtration (e.g. sand filtration, microfiltration, ultrafiltration); (viii) Flotation; (ix) Ion exchange; (x) Neutralisation; (xi) Oxidation; (xii) Precipitation; (xiii) Sedimentation; (xiv) Stripping","mg/l",1.3,2,"Green","Once every month",0,0,"Unspecified ","Daily ","This BAT-AEL only applies to waste water from the use of wet FGD.\n\nThis BAT-AEL only applies to combustion plants using calcium compounds in flue-gas treatment. \n\nThe higher end of the BAT-AEL range may not apply in the case of highly saline waste water (e.g. chloride concentrations ≥ 5 g/l) due to the increased solubility of calcium sulphate.\n\nThis BAT-AEL does not apply to discharges to the sea or to brackish water bodies.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water from flue-gas treatment, BAT is to use an appropriate combination of the techniques given below, and to use secondary techniques as close as possible to the source in order to avoid dilution: (i) Optimised combustion (see BAT 6) and flue-gas treatment systems (e.g. SCR/SNCR, see BAT 7); (ii) Adsorption on activated carbon; (iii) Aerobic biological treatment; (iv) Anoxic/anaerobic biological treatment; (v) Coagulation and flocculation; (vi) Crystallisation; (vii) Filtration (e.g. sand filtration, microfiltration, ultrafiltration); (viii) Flotation; (ix) Ion exchange; (x) Neutralisation; (xi) Oxidation; (xii) Precipitation; (xiii) Sedimentation; (xiv) Stripping","mg/l",1.3,2,"Green","Once every month",0,0,"Unspecified ","Daily ","This BAT-AEL only applies to waste water from the use of wet FGD.\n\nThis BAT-AEL only applies to combustion plants using calcium compounds in flue-gas treatment. \n\nThe higher end of the BAT-AEL range may not apply in the case of highly saline waste water (e.g. chloride concentrations ≥ 5 g/l) due to the increased solubility of calcium sulphate.\n\nThis BAT-AEL does not apply to discharges to the sea or to brackish water bodies."]
["LCP","1. Energy industries","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water from flue-gas treatment, BAT is to use an appropriate combination of the techniques given below, and to use secondary techniques as close as possible to the source in order to avoid dilution: (i) Optimised combustion (see BAT 6) and flue-gas treatment systems (e.g. SCR/SNCR, see BAT 7); (ii) Adsorption on activated carbon; (iii) Aerobic biological treatment; (iv) Anoxic/anaerobic biological treatment; (v) Coagulation and flocculation; (vi) Crystallisation; (vii) Filtration (e.g. sand filtration, microfiltration, ultrafiltration); (viii) Flotation; (ix) Ion exchange; (x) Neutralisation; (xi) Oxidation; (xii) Precipitation; (xiii) Sedimentation; (xiv) Stripping","mg/l",0.1,0.2,"Green","Once every month",0,0,"Unspecified ","Daily ","This BAT-AEL only applies to waste water from the use of wet FGD.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water from flue-gas treatment, BAT is to use an appropriate combination of the techniques given below, and to use secondary techniques as close as possible to the source in order to avoid dilution: (i) Optimised combustion (see BAT 6) and flue-gas treatment systems (e.g. SCR/SNCR, see BAT 7); (ii) Adsorption on activated carbon; (iii) Aerobic biological treatment; (iv) Anoxic/anaerobic biological treatment; (v) Coagulation and flocculation; (vi) Crystallisation; (vii) Filtration (e.g. sand filtration, microfiltration, ultrafiltration); (viii) Flotation; (ix) Ion exchange; (x) Neutralisation; (xi) Oxidation; (xii) Precipitation; (xiii) Sedimentation; (xiv) Stripping","mg/l",0.1,0.2,"Green","Once every month",0,0,"Unspecified ","Daily ","This BAT-AEL only applies to waste water from the use of wet FGD."]
["LCP","1. Energy industries","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water from flue-gas treatment, BAT is to use an appropriate combination of the techniques given below, and to use secondary techniques as close as possible to the source in order to avoid dilution: (i) Optimised combustion (see BAT 6) and flue-gas treatment systems (e.g. SCR/SNCR, see BAT 7); (ii) Adsorption on activated carbon; (iii) Aerobic biological treatment; (iv) Anoxic/anaerobic biological treatment; (v) Coagulation and flocculation; (vi) Crystallisation; (vii) Filtration (e.g. sand filtration, microfiltration, ultrafiltration); (viii) Flotation; (ix) Ion exchange; (x) Neutralisation; (xi) Oxidation; (xii) Precipitation; (xiii) Sedimentation; (xiv) Stripping","mg/l",1,20,"Green","Once every month",0,0,"Unspecified ","Daily ","This BAT-AEL only applies to waste water from the use of wet FGD.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water from flue-gas treatment, BAT is to use an appropriate combination of the techniques given below, and to use secondary techniques as close as possible to the source in order to avoid dilution: (i) Optimised combustion (see BAT 6) and flue-gas treatment systems (e.g. SCR/SNCR, see BAT 7); (ii) Adsorption on activated carbon; (iii) Aerobic biological treatment; (iv) Anoxic/anaerobic biological treatment; (v) Coagulation and flocculation; (vi) Crystallisation; (vii) Filtration (e.g. sand filtration, microfiltration, ultrafiltration); (viii) Flotation; (ix) Ion exchange; (x) Neutralisation; (xi) Oxidation; (xii) Precipitation; (xiii) Sedimentation; (xiv) Stripping","mg/l",1,20,"Green","Once every month",0,0,"Unspecified ","Daily ","This BAT-AEL only applies to waste water from the use of wet FGD."]
["LCP","1. Energy industries","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water from flue-gas treatment, BAT is to use an appropriate combination of the techniques given below, and to use secondary techniques as close as possible to the source in order to avoid dilution: (i) Optimised combustion (see BAT 6) and flue-gas treatment systems (e.g. SCR/SNCR, see BAT 7); (ii) Adsorption on activated carbon; (iii) Aerobic biological treatment; (iv) Anoxic/anaerobic biological treatment; (v) Coagulation and flocculation; (vi) Crystallisation; (vii) Filtration (e.g. sand filtration, microfiltration, ultrafiltration); (viii) Flotation; (ix) Ion exchange; (x) Neutralisation; (xi) Oxidation; (xii) Precipitation; (xiii) Sedimentation; (xiv) Stripping","mg/l",20,50,"Green","Once every month",0,0,"Unspecified ","Daily ","Either the BAT-AEL for TOC or the BAT-AEL for COD applies. TOC is the preferred option because its monitoring does not rely on the use of very toxic compounds.\n\nThis BAT-AEL applies after subtraction of the intake load.\n\nThis BAT-AEL only applies to waste water from the use of wet FGD.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water from flue-gas treatment, BAT is to use an appropriate combination of the techniques given below, and to use secondary techniques as close as possible to the source in order to avoid dilution: (i) Optimised combustion (see BAT 6) and flue-gas treatment systems (e.g. SCR/SNCR, see BAT 7); (ii) Adsorption on activated carbon; (iii) Aerobic biological treatment; (iv) Anoxic/anaerobic biological treatment; (v) Coagulation and flocculation; (vi) Crystallisation; (vii) Filtration (e.g. sand filtration, microfiltration, ultrafiltration); (viii) Flotation; (ix) Ion exchange; (x) Neutralisation; (xi) Oxidation; (xii) Precipitation; (xiii) Sedimentation; (xiv) Stripping","mg/l",20,50,"Green","Once every month",0,0,"Unspecified ","Daily ","Either the BAT-AEL for TOC or the BAT-AEL for COD applies. TOC is the preferred option because its monitoring does not rely on the use of very toxic compounds.\n\nThis BAT-AEL applies after subtraction of the intake load.\n\nThis BAT-AEL only applies to waste water from the use of wet FGD."]
["LCP","1. Energy industries","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water from flue-gas treatment, BAT is to use an appropriate combination of the techniques given below, and to use secondary techniques as close as possible to the source in order to avoid dilution: (i) Optimised combustion (see BAT 6) and flue-gas treatment systems (e.g. SCR/SNCR, see BAT 7); (ii) Adsorption on activated carbon; (iii) Aerobic biological treatment; (iv) Anoxic/anaerobic biological treatment; (v) Coagulation and flocculation; (vi) Crystallisation; (vii) Filtration (e.g. sand filtration, microfiltration, ultrafiltration); (viii) Flotation; (ix) Ion exchange; (x) Neutralisation; (xi) Oxidation; (xii) Precipitation; (xiii) Sedimentation; (xiv) Stripping","mg/l",10,30,"Green","Once every month",0,0,"Unspecified ","Daily ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water from flue-gas treatment, BAT is to use an appropriate combination of the techniques given below, and to use secondary techniques as close as possible to the source in order to avoid dilution: (i) Optimised combustion (see BAT 6) and flue-gas treatment systems (e.g. SCR/SNCR, see BAT 7); (ii) Adsorption on activated carbon; (iii) Aerobic biological treatment; (iv) Anoxic/anaerobic biological treatment; (v) Coagulation and flocculation; (vi) Crystallisation; (vii) Filtration (e.g. sand filtration, microfiltration, ultrafiltration); (viii) Flotation; (ix) Ion exchange; (x) Neutralisation; (xi) Oxidation; (xii) Precipitation; (xiii) Sedimentation; (xiv) Stripping","mg/l",10,30,"Green","Once every month",0,0,"Unspecified ","Daily ",0]
["LCP","1. Energy industries","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water from flue-gas treatment, BAT is to use an appropriate combination of the techniques given below, and to use secondary techniques as close as possible to the source in order to avoid dilution: (i) Optimised combustion (see BAT 6) and flue-gas treatment systems (e.g. SCR/SNCR, see BAT 7); (ii) Adsorption on activated carbon; (iii) Aerobic biological treatment; (iv) Anoxic/anaerobic biological treatment; (v) Coagulation and flocculation; (vi) Crystallisation; (vii) Filtration (e.g. sand filtration, microfiltration, ultrafiltration); (viii) Flotation; (ix) Ion exchange; (x) Neutralisation; (xi) Oxidation; (xii) Precipitation; (xiii) Sedimentation; (xiv) Stripping","ug/l",50,200,"Green","Once every month",0,0,"Unspecified ","Daily ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water from flue-gas treatment, BAT is to use an appropriate combination of the techniques given below, and to use secondary techniques as close as possible to the source in order to avoid dilution: (i) Optimised combustion (see BAT 6) and flue-gas treatment systems (e.g. SCR/SNCR, see BAT 7); (ii) Adsorption on activated carbon; (iii) Aerobic biological treatment; (iv) Anoxic/anaerobic biological treatment; (v) Coagulation and flocculation; (vi) Crystallisation; (vii) Filtration (e.g. sand filtration, microfiltration, ultrafiltration); (viii) Flotation; (ix) Ion exchange; (x) Neutralisation; (xi) Oxidation; (xii) Precipitation; (xiii) Sedimentation; (xiv) Stripping","ug/l",50,200,"Green","Once every month",0,0,"Unspecified ","Daily ",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Alumina and Anode production","Anode production","Unspecified ","Unspecified","Unspecified","Unspecified","Baking plant in a stand-alone anode production plant","Air","Benzo-a-pyrene","In order to reduce dust, PAH and fluoride emissions to air from a baking plant in a stand-alone anode production plant, BAT is to use a pre-filtration unit and a regenerative thermal oxidiser followed by a dry scrubber (e.g. lime bed)","mg/Nm3",1E-3,0.01,"Green","Once per year ",0,0,0,"Average over sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Alumina and Anode production","Anode production","Unspecified ","Unspecified","Unspecified","Unspecified","Baking plant in a stand-alone anode production plant","Air","Benzo-a-pyrene","In order to reduce dust, PAH and fluoride emissions to air from a baking plant in a stand-alone anode production plant, BAT is to use a pre-filtration unit and a regenerative thermal oxidiser followed by a dry scrubber (e.g. lime bed)","mg/Nm3",1E-3,0.01,"Green","Once per year ",0,0,0,"Average over sampling period",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Alumina and Anode production","Anode production","Unspecified ","Unspecified","Unspecified","Unspecified","Baking plant with a primary aluminium smelter ","Air","Benzo-a-pyrene","In order to reduce dust, sulphur dioxide, PAH and fluoride emissions to air from a baking plant in an anode production plant integrated with a primary aluminium smelter, BAT is to use one or a combination of the techniques given below: (i) Use of raw materials and fuels containing a\nlow amount of sulphur; (ii) Dry scrubber using alumina as the adsorbent\nagent followed by a bag filter; (iii) Wet scrubber; (iv) Regenerative thermal oxidiser in combination\nwith a dust abatement system","mg/Nm3",1E-3,0.01,"Green","Once per year ",0,0,0,"Average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Alumina and Anode production","Anode production","Unspecified ","Unspecified","Unspecified","Unspecified","Baking plant with a primary aluminium smelter ","Air","Benzo-a-pyrene","In order to reduce dust, sulphur dioxide, PAH and fluoride emissions to air from a baking plant in an anode production plant integrated with a primary aluminium smelter, BAT is to use one or a combination of the techniques given below: (i) Use of raw materials and fuels containing a\nlow amount of sulphur; (ii) Dry scrubber using alumina as the adsorbent\nagent followed by a bag filter; (iii) Wet scrubber; (iv) Regenerative thermal oxidiser in combination\nwith a dust abatement system","mg/Nm3",1E-3,0.01,"Green","Once per year ",0,0,0,"Average over the sampling period",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Alumina and Anode production","Anode production","Unspecified ","Unspecified","Unspecified","Unspecified","Paste plant (hot pitch storage, paste\nmixing, cooling and forming)","Air","Benzo-a-pyrene","In order to reduce dust and PAH emissions to air from a paste plant (hot pitch storage, paste mixing, cooling and forming), BAT is to use one or a combination of the techniques given below: (i) Dry scrubber using coke as the adsorbent agent, with or without precooling, followed by a bag filter; (ii) Regenerative thermal oxidiser; (iii) Catalytic thermal oxidiser","mg/Nm3",1E-3,0.01,"Green","Once per year ",0,0,0,"Average over the sampling period ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Alumina and Anode production","Anode production","Unspecified ","Unspecified","Unspecified","Unspecified","Paste plant (hot pitch storage, paste\nmixing, cooling and forming)","Air","Benzo-a-pyrene","In order to reduce dust and PAH emissions to air from a paste plant (hot pitch storage, paste mixing, cooling and forming), BAT is to use one or a combination of the techniques given below: (i) Dry scrubber using coke as the adsorbent agent, with or without precooling, followed by a bag filter; (ii) Regenerative thermal oxidiser; (iii) Catalytic thermal oxidiser","mg/Nm3",1E-3,0.01,"Green","Once per year ",0,0,0,"Average over the sampling period ",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Carbon and Graphite Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Baking","Air","Benzo-a-pyrene","In order to reduce dust and PAH emissions to air from baking, BAT is to use one or a combination of the techniques given below: (i) ESP, in combination with a thermal oxidation step (e.g.\nregenerative thermal oxidiser) when highly volatile\ncompounds are expected; (ii) Regenerative thermal oxidiser, in combination with a\npretreatment (e.g. ESP) in cases of a high dust content\nin the exhaust gas; (iii) Thermal oxidiser","mg/Nm3",5.0000000000000001E-3,1.4999999999999999E-2,"Green","Once per year",0,0,0,"Average over the sampling period","The lower end of the range is associated with the use of a thermal oxidiser. The upper end of the range is associated with the use of a combination of an ESP and a regenerative thermal oxidiser.\n\nFor cathode production, the upper end of the range is 0,05 mg/Nm3.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Carbon and Graphite Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Baking","Air","Benzo-a-pyrene","In order to reduce dust and PAH emissions to air from baking, BAT is to use one or a combination of the techniques given below: (i) ESP, in combination with a thermal oxidation step (e.g.\nregenerative thermal oxidiser) when highly volatile\ncompounds are expected; (ii) Regenerative thermal oxidiser, in combination with a\npretreatment (e.g. ESP) in cases of a high dust content\nin the exhaust gas; (iii) Thermal oxidiser","mg/Nm3",5.0000000000000001E-3,1.4999999999999999E-2,"Green","Once per year",0,0,0,"Average over the sampling period","The lower end of the range is associated with the use of a thermal oxidiser. The upper end of the range is associated with the use of a combination of an ESP and a regenerative thermal oxidiser.\n\nFor cathode production, the upper end of the range is 0,05 mg/Nm3."]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Carbon and Graphite Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Impregnation","Air","Benzo-a-pyrene","In order to reduce dust and PAH emissions to air from impregnation, BAT is to use one or a combination of the techniques given below: (i) Dry scrubber followed by a bag filter; (ii) Coke filter; (iii) Thermal oxidiser","mg/Nm3",1E-3,0.01,"Green","Once per year",0,0,0,"Average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Carbon and Graphite Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Impregnation","Air","Benzo-a-pyrene","In order to reduce dust and PAH emissions to air from impregnation, BAT is to use one or a combination of the techniques given below: (i) Dry scrubber followed by a bag filter; (ii) Coke filter; (iii) Thermal oxidiser","mg/Nm3",1E-3,0.01,"Green","Once per year",0,0,0,"Average over the sampling period",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Carbon and Graphite Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Production of green paste and green shapes","Air","Benzo-a-pyrene","In order to reduce dust and PAH emissions to air from the production of green paste and green shapes, BAT is to use one or a combination of the techniques given below: (i) Dry scrubber using coke as the adsorbent agent and with or without precooling, followed by a bag\nfilter; (ii) Coke filter; (iii) Regenerative thermal oxidiser; (iv) Thermal oxidiser","mg/Nm3",1E-3,0.01,"Green","Once per year",0,0,0,"Average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Carbon and Graphite Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Production of green paste and green shapes","Air","Benzo-a-pyrene","In order to reduce dust and PAH emissions to air from the production of green paste and green shapes, BAT is to use one or a combination of the techniques given below: (i) Dry scrubber using coke as the adsorbent agent and with or without precooling, followed by a bag\nfilter; (ii) Coke filter; (iii) Regenerative thermal oxidiser; (iv) Thermal oxidiser","mg/Nm3",1E-3,0.01,"Green","Once per year",0,0,0,"Average over the sampling period",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Carbon and Graphite Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Storage, handling and transportation of coke and pitch, and mechanical processes (such as grinding) and graphitising and machining","Air","Benzo-a-pyrene","In order to reduce dust emissions to air from the storage, handling and transportation of coke and pitch, and mechanical processes (such as grinding) and graphitising and machining, BAT is to use a bag filter.","mg/Nm3","N/A",0.01,"Green","Once per year",0,0,0,"Average over the sampling period","BaP particles are only expected if processing solid pitch",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Carbon and Graphite Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Storage, handling and transportation of coke and pitch, and mechanical processes (such as grinding) and graphitising and machining","Air","Benzo-a-pyrene","In order to reduce dust emissions to air from the storage, handling and transportation of coke and pitch, and mechanical processes (such as grinding) and graphitising and machining, BAT is to use a bag filter.","mg/Nm3","N/A",0.01,"Green","Once per year",0,0,0,"Average over the sampling period","BaP particles are only expected if processing solid pitch"]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Zinc and Cadmium Production","Cadmium Production","Unspecified","Unspecified","Unspecified","Unspecified","Pyrometallurgical cadmium production and the melting, alloying and casting of cadmium ingots","Air","Cadmium and its compounds (as Cd)","In order to reduce dust and metal emissions to air from pyrometallurgical cadmium production and the melting, alloying and casting of cadmium ingots, BAT is to use one or a combination of the techniques given below: (i) Bag filter; (ii) ESP; (iii) Wet scrubber ","mg/Nm3","N/A",0.1,"Green","Once per year",0,0,0,"Average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Zinc and Cadmium Production","Cadmium Production","Unspecified","Unspecified","Unspecified","Unspecified","Pyrometallurgical cadmium production and the melting, alloying and casting of cadmium ingots","Air","Cadmium and its compounds (as Cd)","In order to reduce dust and metal emissions to air from pyrometallurgical cadmium production and the melting, alloying and casting of cadmium ingots, BAT is to use one or a combination of the techniques given below: (i) Bag filter; (ii) ESP; (iii) Wet scrubber ","mg/Nm3","N/A",0.1,"Green","Once per year",0,0,0,"Average over the sampling period",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Alumina and Anode production","Secondary aluminium production ","Unspecified","Unspecified","Unspecified","Unspecified","Thermal treatment of contaminated secondary raw materials (e.g. swarf), the melting furnace, and remelting and molten metal treatment","Air","Chlorine","In order to reduce emissions to air of HCl, Cl2 and HF from the thermal treatment of contaminated secondary raw materials (e.g. swarf), the melting furnace, and remelting and molten metal treatment, BAT is to use one or a combination of the techniques given below: (i) Select and feed the raw materials according to the furnace and the abatement techniques used; (ii) Ca(OH)2 or sodium bicarbonate injection in combination with a bag filter; (iii) Control of the refining process, adapting the quantity of refining gas used to remove the contaminants\npresent into the molten metals; (iv) Use of dilute chlorine with inert gas in the refining process","mg/Nm3","N/A",1,"Green","Once per year",0,0,0,"Average over the sampling period","Only applicable to emissions from refining processes carried out with chemicals containing chlorine.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Alumina and Anode production","Secondary aluminium production ","Unspecified","Unspecified","Unspecified","Unspecified","Thermal treatment of contaminated secondary raw materials (e.g. swarf), the melting furnace, and remelting and molten metal treatment","Air","Chlorine","In order to reduce emissions to air of HCl, Cl2 and HF from the thermal treatment of contaminated secondary raw materials (e.g. swarf), the melting furnace, and remelting and molten metal treatment, BAT is to use one or a combination of the techniques given below: (i) Select and feed the raw materials according to the furnace and the abatement techniques used; (ii) Ca(OH)2 or sodium bicarbonate injection in combination with a bag filter; (iii) Control of the refining process, adapting the quantity of refining gas used to remove the contaminants\npresent into the molten metals; (iv) Use of dilute chlorine with inert gas in the refining process","mg/Nm3","N/A",1,"Green","Once per year",0,0,0,"Average over the sampling period","Only applicable to emissions from refining processes carried out with chemicals containing chlorine."]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Metals Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Hydrometallurgical operation, including the associated incineration, calcining and drying operations","Air","Chlorine","In order to reduce HCl and Cl2 emissions to air from a hydrometallurgical operation, including the associated incineration, calcining and drying operations, BAT is to use an alkaline scrubber.","mg/Nm3",0.5,2,"Green","Once per year",0,0,0,"Average over the sampling period ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Metals Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Hydrometallurgical operation, including the associated incineration, calcining and drying operations","Air","Chlorine","In order to reduce HCl and Cl2 emissions to air from a hydrometallurgical operation, including the associated incineration, calcining and drying operations, BAT is to use an alkaline scrubber.","mg/Nm3",0.5,2,"Green","Once per year",0,0,0,"Average over the sampling period ",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Nickel and Cobalt Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Atmospheric or pressure leaching processes","Air","Chlorine","In order to reduce nickel and chlorine emissions to air from the atmospheric or pressure leaching processes, BAT is to use a wet scrubber.","mg/Nm3","N/A",1,"Green","Once per year",0,0,0,"Average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Nickel and Cobalt Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Atmospheric or pressure leaching processes","Air","Chlorine","In order to reduce nickel and chlorine emissions to air from the atmospheric or pressure leaching processes, BAT is to use a wet scrubber.","mg/Nm3","N/A",1,"Green","Once per year",0,0,0,"Average over the sampling period",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Alumina and Anode production","Anode production","Unspecified ","Unspecified","Unspecified","Unspecified","Baking plant in a stand-alone anode production plant","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust, PAH and fluoride emissions to air from a baking plant in a stand-alone anode production plant, BAT is to use a pre-filtration unit and a regenerative thermal oxidiser followed by a dry scrubber (e.g. lime bed)","mg/Nm3",2,5,"Green","Continuous",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Alumina and Anode production","Anode production","Unspecified ","Unspecified","Unspecified","Unspecified","Baking plant in a stand-alone anode production plant","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust, PAH and fluoride emissions to air from a baking plant in a stand-alone anode production plant, BAT is to use a pre-filtration unit and a regenerative thermal oxidiser followed by a dry scrubber (e.g. lime bed)","mg/Nm3",2,5,"Green","Continuous",0,0,0,"Daily average",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Alumina and Anode production","Anode production","Unspecified ","Unspecified","Unspecified","Unspecified","Baking plant with a primary aluminium smelter ","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust, sulphur dioxide, PAH and fluoride emissions to air from a baking plant in an anode production plant integrated with a primary aluminium smelter, BAT is to use one or a combination of the techniques given below: (i) Use of raw materials and fuels containing a\nlow amount of sulphur; (ii) Dry scrubber using alumina as the adsorbent\nagent followed by a bag filter; (iii) Wet scrubber; (iv) Regenerative thermal oxidiser in combination\nwith a dust abatement system","mg/Nm3",2,5,"Green","Continuous",0,0,0,"Daily average or as an average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Alumina and Anode production","Anode production","Unspecified ","Unspecified","Unspecified","Unspecified","Baking plant with a primary aluminium smelter ","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust, sulphur dioxide, PAH and fluoride emissions to air from a baking plant in an anode production plant integrated with a primary aluminium smelter, BAT is to use one or a combination of the techniques given below: (i) Use of raw materials and fuels containing a\nlow amount of sulphur; (ii) Dry scrubber using alumina as the adsorbent\nagent followed by a bag filter; (iii) Wet scrubber; (iv) Regenerative thermal oxidiser in combination\nwith a dust abatement system","mg/Nm3",2,5,"Green","Continuous",0,0,0,"Daily average or as an average over the sampling period",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Alumina and Anode production","Anode production","Unspecified ","Unspecified","Unspecified","Unspecified","Paste plant (hot pitch storage, paste\nmixing, cooling and forming)","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and PAH emissions to air from a paste plant (hot pitch storage, paste mixing, cooling and forming), BAT is to use one or a combination of the techniques given below: (i) Dry scrubber using coke as the adsorbent agent, with or without precooling, followed by a bag filter; (ii) Regenerative thermal oxidiser; (iii) Catalytic thermal oxidiser","mg/Nm3",2,5,"Green","Continuous or\nonce per year",0,0,0,"Daily average or as an average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Alumina and Anode production","Anode production","Unspecified ","Unspecified","Unspecified","Unspecified","Paste plant (hot pitch storage, paste\nmixing, cooling and forming)","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and PAH emissions to air from a paste plant (hot pitch storage, paste mixing, cooling and forming), BAT is to use one or a combination of the techniques given below: (i) Dry scrubber using coke as the adsorbent agent, with or without precooling, followed by a bag filter; (ii) Regenerative thermal oxidiser; (iii) Catalytic thermal oxidiser","mg/Nm3",2,5,"Green","Continuous or\nonce per year",0,0,0,"Daily average or as an average over the sampling period",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Alumina and Anode production","Primary aluminium production","Unspecified ","Existing","Unspecified","Unspecified","Electrolysis house (collected from the electrolytic cells and roof vents) ","Air","Particulates (PM10) (Annual Mean)","In order to prevent or collect diffuse emissions from electrolytic cells in primary aluminium production using the Søderberg technology, BAT is to use a combination of the techniques given below: (i) Use of paste with a pitch content between 25 % and 28 % (dry paste); (ii) Upgrade the manifold design to allow closed point feeding operations and improved off-gas collection\nefficiency; (iii) Alumina point feeding\n\nIn order to prevent or collect diffuse emissions from electrolytic cells in primary aluminium\nproduction using prebaked anodes, BAT is to use a combination of the techniques given below: (i) Automatic multiple point feeding of alumina; (ii) Complete hood coverage of the cell and adequate off-gas extraction rates (to lead the off-gas to the\ntreatment in BAT 67) taking into account fluoride generation from bath and carbon anode\nconsumption; (iii) Boosted suction system connected to the abatement techniques listed in BAT 67; (iv) Minimisation of the time for changing anodes and other activities that require cell hoods to be\nremoved; (v) Efficient process control system avoiding process deviations that might otherwise lead to increased cell\nevolution and emissions; (vi) Use of a programmed system for cell operations and maintenance; (vii) Use of established efficient cleaning methods in the rodding plant to recover fluorides and carbonl (viii) Storage of removed anodes in a compartment near the cell, connected to the treatment in BAT 67, or\nstorage of the butts in confined boxes\n\nIn order to reduce dust, metal and fluoride emissions to air from electrolytic cells, BAT is to use\none of the techniques given below: (i) Dry scrubber using alumina as the adsorbent agent\nfollowed by a bag filter; (ii) Dry scrubber using alumina as the adsorbent agent\nfollowed by a bag filter and a wet scrubber\n\n","kg/t Al","N/A",1.2,"Green","Continuous or\nonce per year",0,0,0,"As mass of pollutant emitted during a year from the electrolysis house divided by the mass of liquid aluminium produced in the same year.","\n\n These BAT-AELs are not applicable to plants that due to their configuration cannot measure roof emissions.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Alumina and Anode production","Primary aluminium production","Unspecified ","Existing","Unspecified","Unspecified","Electrolysis house (collected from the electrolytic cells and roof vents) ","Air","Particulates (PM10) (Annual Mean)","In order to prevent or collect diffuse emissions from electrolytic cells in primary aluminium production using the Søderberg technology, BAT is to use a combination of the techniques given below: (i) Use of paste with a pitch content between 25 % and 28 % (dry paste); (ii) Upgrade the manifold design to allow closed point feeding operations and improved off-gas collection\nefficiency; (iii) Alumina point feeding\n\nIn order to prevent or collect diffuse emissions from electrolytic cells in primary aluminium\nproduction using prebaked anodes, BAT is to use a combination of the techniques given below: (i) Automatic multiple point feeding of alumina; (ii) Complete hood coverage of the cell and adequate off-gas extraction rates (to lead the off-gas to the\ntreatment in BAT 67) taking into account fluoride generation from bath and carbon anode\nconsumption; (iii) Boosted suction system connected to the abatement techniques listed in BAT 67; (iv) Minimisation of the time for changing anodes and other activities that require cell hoods to be\nremoved; (v) Efficient process control system avoiding process deviations that might otherwise lead to increased cell\nevolution and emissions; (vi) Use of a programmed system for cell operations and maintenance; (vii) Use of established efficient cleaning methods in the rodding plant to recover fluorides and carbonl (viii) Storage of removed anodes in a compartment near the cell, connected to the treatment in BAT 67, or\nstorage of the butts in confined boxes\n\nIn order to reduce dust, metal and fluoride emissions to air from electrolytic cells, BAT is to use\none of the techniques given below: (i) Dry scrubber using alumina as the adsorbent agent\nfollowed by a bag filter; (ii) Dry scrubber using alumina as the adsorbent agent\nfollowed by a bag filter and a wet scrubber\n\n","kg/t Al","N/A",1.2,"Green","Continuous or\nonce per year",0,0,0,"As mass of pollutant emitted during a year from the electrolysis house divided by the mass of liquid aluminium produced in the same year.","\n\n These BAT-AELs are not applicable to plants that due to their configuration cannot measure roof emissions."]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Alumina and Anode production","Primary aluminium production","Unspecified ","New","Unspecified","Unspecified","Electrolysis house (collected from the electrolytic cells and roof vents) ","Air","Particulates (PM10) (Annual Mean)","In order to prevent or collect diffuse emissions from electrolytic cells in primary aluminium production using the Søderberg technology, BAT is to use a combination of the techniques given below: (i) Use of paste with a pitch content between 25 % and 28 % (dry paste); (ii) Upgrade the manifold design to allow closed point feeding operations and improved off-gas collection\nefficiency; (iii) Alumina point feeding\n\nIn order to prevent or collect diffuse emissions from electrolytic cells in primary aluminium\nproduction using prebaked anodes, BAT is to use a combination of the techniques given below: (i) Automatic multiple point feeding of alumina; (ii) Complete hood coverage of the cell and adequate off-gas extraction rates (to lead the off-gas to the\ntreatment in BAT 67) taking into account fluoride generation from bath and carbon anode\nconsumption; (iii) Boosted suction system connected to the abatement techniques listed in BAT 67; (iv) Minimisation of the time for changing anodes and other activities that require cell hoods to be\nremoved; (v) Efficient process control system avoiding process deviations that might otherwise lead to increased cell\nevolution and emissions; (vi) Use of a programmed system for cell operations and maintenance; (vii) Use of established efficient cleaning methods in the rodding plant to recover fluorides and carbonl (viii) Storage of removed anodes in a compartment near the cell, connected to the treatment in BAT 67, or\nstorage of the butts in confined boxes\n\nIn order to reduce dust, metal and fluoride emissions to air from electrolytic cells, BAT is to use\none of the techniques given below: (i) Dry scrubber using alumina as the adsorbent agent\nfollowed by a bag filter; (ii) Dry scrubber using alumina as the adsorbent agent\nfollowed by a bag filter and a wet scrubber\n\n","kg/t Al","N/A",0.6,"Green","Continuous or\nonce per year",0,0,0,"As mass of pollutant emitted during a year from the electrolysis house divided by the mass of liquid aluminium produced in the same year.",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Alumina and Anode production","Primary aluminium production","Unspecified ","New","Unspecified","Unspecified","Electrolysis house (collected from the electrolytic cells and roof vents) ","Air","Particulates (PM10) (Annual Mean)","In order to prevent or collect diffuse emissions from electrolytic cells in primary aluminium production using the Søderberg technology, BAT is to use a combination of the techniques given below: (i) Use of paste with a pitch content between 25 % and 28 % (dry paste); (ii) Upgrade the manifold design to allow closed point feeding operations and improved off-gas collection\nefficiency; (iii) Alumina point feeding\n\nIn order to prevent or collect diffuse emissions from electrolytic cells in primary aluminium\nproduction using prebaked anodes, BAT is to use a combination of the techniques given below: (i) Automatic multiple point feeding of alumina; (ii) Complete hood coverage of the cell and adequate off-gas extraction rates (to lead the off-gas to the\ntreatment in BAT 67) taking into account fluoride generation from bath and carbon anode\nconsumption; (iii) Boosted suction system connected to the abatement techniques listed in BAT 67; (iv) Minimisation of the time for changing anodes and other activities that require cell hoods to be\nremoved; (v) Efficient process control system avoiding process deviations that might otherwise lead to increased cell\nevolution and emissions; (vi) Use of a programmed system for cell operations and maintenance; (vii) Use of established efficient cleaning methods in the rodding plant to recover fluorides and carbonl (viii) Storage of removed anodes in a compartment near the cell, connected to the treatment in BAT 67, or\nstorage of the butts in confined boxes\n\nIn order to reduce dust, metal and fluoride emissions to air from electrolytic cells, BAT is to use\none of the techniques given below: (i) Dry scrubber using alumina as the adsorbent agent\nfollowed by a bag filter; (ii) Dry scrubber using alumina as the adsorbent agent\nfollowed by a bag filter and a wet scrubber\n\n","kg/t Al","N/A",0.6,"Green","Continuous or\nonce per year",0,0,0,"As mass of pollutant emitted during a year from the electrolysis house divided by the mass of liquid aluminium produced in the same year.",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Alumina and Anode production","Primary aluminium production","Unspecified","Unspecified","Unspecified","Unspecified","Electrolytic cells","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust, metal and fluoride emissions to air from electrolytic cells, BAT is to use one of the techniques given below: (i) Dry scrubber using alumina as the adsorbent agent\nfollowed by a bag filter; (ii) Dry scrubber using alumina as the adsorbent agent\nfollowed by a bag filter and a wet scrubber","mg/Nm3",2,5,"Green","Continuous or\nonce per year",0,0,0,"Daily average or average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Alumina and Anode production","Primary aluminium production","Unspecified","Unspecified","Unspecified","Unspecified","Electrolytic cells","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust, metal and fluoride emissions to air from electrolytic cells, BAT is to use one of the techniques given below: (i) Dry scrubber using alumina as the adsorbent agent\nfollowed by a bag filter; (ii) Dry scrubber using alumina as the adsorbent agent\nfollowed by a bag filter and a wet scrubber","mg/Nm3",2,5,"Green","Continuous or\nonce per year",0,0,0,"Daily average or average over the sampling period",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Alumina and Anode production","Primary aluminium production","Unspecified","Unspecified","Unspecified","Unspecified","Melting and molten metal treatment and casting","Air","Particulates (PM10) (Annual Mean)","In order to prevent or reduce dust and metal emissions to air from melting and molten metal\ntreatment and casting in primary aluminium production, BAT is to use one or both of the techniques given\nbelow","mg/Nm3",2,25,"Green","Once per year",0,0,0,"Average of the samples obtained over a year","The lower end of the range is associated with the use of a bag filter",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Alumina and Anode production","Primary aluminium production","Unspecified","Unspecified","Unspecified","Unspecified","Melting and molten metal treatment and casting","Air","Particulates (PM10) (Annual Mean)","In order to prevent or reduce dust and metal emissions to air from melting and molten metal\ntreatment and casting in primary aluminium production, BAT is to use one or both of the techniques given\nbelow","mg/Nm3",2,25,"Green","Once per year",0,0,0,"Average of the samples obtained over a year","The lower end of the range is associated with the use of a bag filter"]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Alumina and Anode production","Primary aluminium production","Unspecified","Unspecified","Unspecified","Unspecified","Storage, handling and transport of raw materials","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust emissions from the storage, handling and transport of raw materials, BAT is to use a bag filter.","mg/Nm3",5,10,"Green","Oncer per year ",0,0,0,"Average over sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Alumina and Anode production","Primary aluminium production","Unspecified","Unspecified","Unspecified","Unspecified","Storage, handling and transport of raw materials","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust emissions from the storage, handling and transport of raw materials, BAT is to use a bag filter.","mg/Nm3",5,10,"Green","Oncer per year ",0,0,0,"Average over sampling period",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Alumina and Anode production","Secondary aluminium production ","Unspecified","Unspecified","Unspecified","Unspecified","Furnace processes such as charging, melting, tapping and molten metal treatment","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air from furnace processes such as charging, melting, tapping and molten metal treatment in secondary aluminium production, BAT is to use a bag filter","mg/Nm3",2,5,"Green","Oncer per year ",0,0,0,"Daily average or average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Alumina and Anode production","Secondary aluminium production ","Unspecified","Unspecified","Unspecified","Unspecified","Furnace processes such as charging, melting, tapping and molten metal treatment","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air from furnace processes such as charging, melting, tapping and molten metal treatment in secondary aluminium production, BAT is to use a bag filter","mg/Nm3",2,5,"Green","Oncer per year ",0,0,0,"Daily average or average over the sampling period",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Alumina and Anode production","Secondary aluminium production ","Unspecified","Unspecified","Unspecified","Unspecified","Remelting","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air from remelting in secondary aluminium production, BAT is to use one or a combination of the techniques given below: (i) Use of uncontaminated aluminium material i.e. solid material free of substances such as paint, plastic\nor oil (e.g. billets); (ii) Optimise combustion conditions to reduce the emissions of dust; (iii) Bag filter","mg/Nm3",2,5,"Green","Once per year",0,0,0,"Average over the sampling period","For furnaces designed to use and using only uncontaminated raw material, for which dust emissions are below 1 kg/h, the upper end of the range is 25 mg/Nm3 as an average of the samples obtained over a year.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Alumina and Anode production","Secondary aluminium production ","Unspecified","Unspecified","Unspecified","Unspecified","Remelting","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air from remelting in secondary aluminium production, BAT is to use one or a combination of the techniques given below: (i) Use of uncontaminated aluminium material i.e. solid material free of substances such as paint, plastic\nor oil (e.g. billets); (ii) Optimise combustion conditions to reduce the emissions of dust; (iii) Bag filter","mg/Nm3",2,5,"Green","Once per year",0,0,0,"Average over the sampling period","For furnaces designed to use and using only uncontaminated raw material, for which dust emissions are below 1 kg/h, the upper end of the range is 25 mg/Nm3 as an average of the samples obtained over a year."]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Alumina and Anode production","Secondary aluminium production ","Unspecified","Unspecified","Unspecified","Unspecified","Swarf drying and the removal of oil and organic compounds from the swarf, from the crushing, milling and dry separation of non-metallic constituents and metals other than aluminium, and from the storage, handling and transport","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions from the swarf drying and the removal of oil and organic compounds from the swarf, from the crushing, milling and dry separation of non-metallic constituents and metals other than aluminium, and from the storage, handling and transport in secondary aluminium production, BAT is to use a bag filter.","mg/Nm3","N/A",5,"Green","Oncer per year ",0,0,0,"Average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Alumina and Anode production","Secondary aluminium production ","Unspecified","Unspecified","Unspecified","Unspecified","Swarf drying and the removal of oil and organic compounds from the swarf, from the crushing, milling and dry separation of non-metallic constituents and metals other than aluminium, and from the storage, handling and transport","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions from the swarf drying and the removal of oil and organic compounds from the swarf, from the crushing, milling and dry separation of non-metallic constituents and metals other than aluminium, and from the storage, handling and transport in secondary aluminium production, BAT is to use a bag filter.","mg/Nm3","N/A",5,"Green","Oncer per year ",0,0,0,"Average over the sampling period",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Aluminium Production","Salt slag recycling process","Unspecified","Unspecified","Unspecified","Unspecified","Crushing and dry milling associated with the salt slag recovery process","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air from crushing and dry milling associated with the salt slag recovery process, BAT is to use a bag filter.","mg/Nm3",2,5,"Green","Continuous",0,0,0,"Daily average or average over sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Aluminium Production","Salt slag recycling process","Unspecified","Unspecified","Unspecified","Unspecified","Crushing and dry milling associated with the salt slag recovery process","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air from crushing and dry milling associated with the salt slag recovery process, BAT is to use a bag filter.","mg/Nm3",2,5,"Green","Continuous",0,0,0,"Daily average or average over sampling period",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Carbon and Graphite Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Baking","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and PAH emissions to air from baking, BAT is to use one or a combination of the techniques given below: (i) ESP, in combination with a thermal oxidation step (e.g.\nregenerative thermal oxidiser) when highly volatile\ncompounds are expected; (ii) Regenerative thermal oxidiser, in combination with a\npretreatment (e.g. ESP) in cases of a high dust content\nin the exhaust gas; (iii) Thermal oxidiser","mg/Nm3",2,10,"Green","Once per year",0,0,0,"Average over the sampling period","The lower end of the range is associated with the use of a combination of an ESP and a regenerative thermal oxidiser. The higher end of the range is associated with the use of a thermal oxidiser.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Carbon and Graphite Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Baking","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and PAH emissions to air from baking, BAT is to use one or a combination of the techniques given below: (i) ESP, in combination with a thermal oxidation step (e.g.\nregenerative thermal oxidiser) when highly volatile\ncompounds are expected; (ii) Regenerative thermal oxidiser, in combination with a\npretreatment (e.g. ESP) in cases of a high dust content\nin the exhaust gas; (iii) Thermal oxidiser","mg/Nm3",2,10,"Green","Once per year",0,0,0,"Average over the sampling period","The lower end of the range is associated with the use of a combination of an ESP and a regenerative thermal oxidiser. The higher end of the range is associated with the use of a thermal oxidiser."]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Carbon and Graphite Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Impregnation","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and PAH emissions to air from impregnation, BAT is to use one or a combination of the techniques given below: (i) Dry scrubber followed by a bag filter; (ii) Coke filter; (iii) Thermal oxidiser","mg/Nm3",2,10,"Green","Once per year",0,0,0,"Average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Carbon and Graphite Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Impregnation","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and PAH emissions to air from impregnation, BAT is to use one or a combination of the techniques given below: (i) Dry scrubber followed by a bag filter; (ii) Coke filter; (iii) Thermal oxidiser","mg/Nm3",2,10,"Green","Once per year",0,0,0,"Average over the sampling period",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Carbon and Graphite Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Production of green paste and green shapes","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and PAH emissions to air from the production of green paste and green shapes, BAT is to use one or a combination of the techniques given below: (i) Dry scrubber using coke as the adsorbent agent and with or without precooling, followed by a bag\nfilter; (ii) Coke filter; (iii) Regenerative thermal oxidiser; (iv) Thermal oxidiser","mg/Nm3",2,10,"Green","Once per year",0,0,0,"Average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Carbon and Graphite Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Production of green paste and green shapes","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and PAH emissions to air from the production of green paste and green shapes, BAT is to use one or a combination of the techniques given below: (i) Dry scrubber using coke as the adsorbent agent and with or without precooling, followed by a bag\nfilter; (ii) Coke filter; (iii) Regenerative thermal oxidiser; (iv) Thermal oxidiser","mg/Nm3",2,10,"Green","Once per year",0,0,0,"Average over the sampling period",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Carbon and Graphite Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Storage, handling and transportation of coke and pitch, and mechanical processes (such as grinding) and graphitising and machining","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust emissions to air from the storage, handling and transportation of coke and pitch, and mechanical processes (such as grinding) and graphitising and machining, BAT is to use a bag filter.","mg/Nm3",2,5,"Green","Once per year",0,0,0,"Average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Carbon and Graphite Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Storage, handling and transportation of coke and pitch, and mechanical processes (such as grinding) and graphitising and machining","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust emissions to air from the storage, handling and transportation of coke and pitch, and mechanical processes (such as grinding) and graphitising and machining, BAT is to use a bag filter.","mg/Nm3",2,5,"Green","Once per year",0,0,0,"Average over the sampling period",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Copper production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Anode casting (in primary and secondary copper production)","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air from anode casting in primary and secondary copper production, BAT is to use a bag filter or, in the case of off-gases with a water content close to the dew point, a wet scrubber or a demister.","mg/Nm3",5,15,"Green","Once per year ",0,0,0,"Daily average or average over sampling period","The lower end of the range is associated with the use of a bag filter.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Copper production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Anode casting (in primary and secondary copper production)","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air from anode casting in primary and secondary copper production, BAT is to use a bag filter or, in the case of off-gases with a water content close to the dew point, a wet scrubber or a demister.","mg/Nm3",5,15,"Green","Once per year ",0,0,0,"Daily average or average over sampling period","The lower end of the range is associated with the use of a bag filter."]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Copper production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Anode furnace (in primary and secondary copper production)","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air from the anode furnace in primary and secondary copper production, BAT is to use a bag filter or a scrubber in combination with an ESP.","mg/Nm3",2,5,"Green","Once per year ",0,0,0,"Daily average or average over sampling period","Dust emissions are expected to be towards the lower end of the range when emissions of heavy metals are above the following levels: 1 mg/Nm3 for lead, 1 mg/Nm3 for copper, 0,05 mg/Nm3 for arsenic, 0,05 mg/Nm3 for cadmium",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Copper production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Anode furnace (in primary and secondary copper production)","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air from the anode furnace in primary and secondary copper production, BAT is to use a bag filter or a scrubber in combination with an ESP.","mg/Nm3",2,5,"Green","Once per year ",0,0,0,"Daily average or average over sampling period","Dust emissions are expected to be towards the lower end of the range when emissions of heavy metals are above the following levels: 1 mg/Nm3 for lead, 1 mg/Nm3 for copper, 0,05 mg/Nm3 for arsenic, 0,05 mg/Nm3 for cadmium"]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Copper production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Concentrate drying in primary copper production","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air from concentrate drying in primary copper production, BAT is to use a bag filter.","mg/Nm3",3,5,"Green","Once per year ",0,0,0,"Daily average or average over the sampling period","Dust emissions are expected to be towards the lower end of the range when emissions of heavy metals are above the\nfollowing levels: 1 mg/Nm3 for lead, 1 mg/Nm3 for copper, 0,05 mg/Nm3 for arsenic, 0,05 mg/Nm3 for cadmium. ",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Copper production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Concentrate drying in primary copper production","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air from concentrate drying in primary copper production, BAT is to use a bag filter.","mg/Nm3",3,5,"Green","Once per year ",0,0,0,"Daily average or average over the sampling period","Dust emissions are expected to be towards the lower end of the range when emissions of heavy metals are above the\nfollowing levels: 1 mg/Nm3 for lead, 1 mg/Nm3 for copper, 0,05 mg/Nm3 for arsenic, 0,05 mg/Nm3 for cadmium. "]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Copper production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Copper melting furnace","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air from a copper melting furnace, BAT is to select and feed the raw materials according to the furnace type and the abatement system used and to use a bag filter.","mg/Nm3",2,5,"Green","Once per year ",0,0,0,"Daily average or average over sampling period","Dust emissions are expected to be towards the lower end of the range when emissions of copper are above 1 mg/Nm3",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Copper production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Copper melting furnace","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air from a copper melting furnace, BAT is to select and feed the raw materials according to the furnace type and the abatement system used and to use a bag filter.","mg/Nm3",2,5,"Green","Once per year ",0,0,0,"Daily average or average over sampling period","Dust emissions are expected to be towards the lower end of the range when emissions of copper are above 1 mg/Nm3"]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Copper production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Copper-rich slag furnace processing","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air from copper-rich slag furnace processing, BAT is to use a bag filter or a scrubber in combination with an ESP.","mg/Nm3",2,5,"Green","Once per year ",0,0,0,"Average over sampling period","Dust emissions are expected to be towards the lower end of the range when emissions of lead are above 1 mg/Nm3",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Copper production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Copper-rich slag furnace processing","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air from copper-rich slag furnace processing, BAT is to use a bag filter or a scrubber in combination with an ESP.","mg/Nm3",2,5,"Green","Once per year ",0,0,0,"Average over sampling period","Dust emissions are expected to be towards the lower end of the range when emissions of lead are above 1 mg/Nm3"]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Copper production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Primary copper smelter and converter (emissions other than those that are routed to the sulphuric acid or liquid SO2 plant or power plant)","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air (other than those that are routed to the sulphuric acid or liquid SO2 plant or power plant) from the primary copper smelter and converter, BAT is to use a bag filter and/or a wet scrubber.","mg/Nm3",2,5,"Green","Once per year ",0,0,0,"Daily average","Dust emissions are expected to be towards the lower end of the range when emissions of heavy metals are above the following levels: 1 mg/Nm3 for lead, 1 mg/Nm3 for copper, 0,05 mg/Nm3 for arsenic, 0,05 mg/Nm3 for cadmium.\n\n When the concentrates used have a high organic carbon content (e.g. around 10 wt-%), emissions of up to 10 mg/Nm3\ncan be expected. ",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Copper production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Primary copper smelter and converter (emissions other than those that are routed to the sulphuric acid or liquid SO2 plant or power plant)","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air (other than those that are routed to the sulphuric acid or liquid SO2 plant or power plant) from the primary copper smelter and converter, BAT is to use a bag filter and/or a wet scrubber.","mg/Nm3",2,5,"Green","Once per year ",0,0,0,"Daily average","Dust emissions are expected to be towards the lower end of the range when emissions of heavy metals are above the following levels: 1 mg/Nm3 for lead, 1 mg/Nm3 for copper, 0,05 mg/Nm3 for arsenic, 0,05 mg/Nm3 for cadmium.\n\n When the concentrates used have a high organic carbon content (e.g. around 10 wt-%), emissions of up to 10 mg/Nm3\ncan be expected. "]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Copper production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Reception,           storage,           handling,           transport,           metering,           mixing,           \nblending,  crushing,  drying,  cutting  and  screening  of  raw  \nmaterials,  and  the  pyrolytic  treatment  of  copper  turnings  \nin  primary  and  secondary  copper  production","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air from the reception, storage, handling, transport, metering, mixing, blending, crushing, drying, cutting and screening of raw materials, and the pyrolytic treatment of copper turnings in primary and secondary copper production, BAT is to use a bag filter.","mg/Nm3",2,5,"Green","Once per year ",0,0,0,"Average over sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Copper production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Reception,           storage,           handling,           transport,           metering,           mixing,           \nblending,  crushing,  drying,  cutting  and  screening  of  raw  \nmaterials,  and  the  pyrolytic  treatment  of  copper  turnings  \nin  primary  and  secondary  copper  production","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air from the reception, storage, handling, transport, metering, mixing, blending, crushing, drying, cutting and screening of raw materials, and the pyrolytic treatment of copper turnings in primary and secondary copper production, BAT is to use a bag filter.","mg/Nm3",2,5,"Green","Once per year ",0,0,0,"Average over sampling period",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Copper production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Secondary copper holding furnace","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air from the secondary copper holding furnace, BAT is to use a bag filter","mg/Nm3","N/A",5,"Green","Once per year ",0,0,0,"Average over sampling period","Dust emissions are expected to be towards the lower end of the range when emissions of heavy metals are above the following levels: 1 mg/Nm3 for lead, 1 mg/Nm3 for copper, 0,05 mg/Nm3 for arsenic, 0,05 mg/Nm3 for cadmium",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Copper production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Secondary copper holding furnace","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air from the secondary copper holding furnace, BAT is to use a bag filter","mg/Nm3","N/A",5,"Green","Once per year ",0,0,0,"Average over sampling period","Dust emissions are expected to be towards the lower end of the range when emissions of heavy metals are above the following levels: 1 mg/Nm3 for lead, 1 mg/Nm3 for copper, 0,05 mg/Nm3 for arsenic, 0,05 mg/Nm3 for cadmium"]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Copper production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Secondary copper smelter and converter and processing of secondary copper intermediates (emissions other than those that are routed to the sulphuric acid plant)","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air (other than those that are routed to the sulphuric acid plant) from the secondary copper smelter and converter and from the processing of secondary copper intermediates, BAT is to use a bag filter.","mg/Nm3",2,4,"Green","Once per year ",0,0,0,"Daily average or average over the sampling period","Dust emissions are expected to be towards the lower end of the range when emissions of heavy metals are above the following levels: 1 mg/Nm3 for lead, 1 mg/Nm3 for copper, 0,05 mg/Nm3 for arsenic, 0,05 mg/Nm3 for cadmium",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Copper production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Secondary copper smelter and converter and processing of secondary copper intermediates (emissions other than those that are routed to the sulphuric acid plant)","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air (other than those that are routed to the sulphuric acid plant) from the secondary copper smelter and converter and from the processing of secondary copper intermediates, BAT is to use a bag filter.","mg/Nm3",2,4,"Green","Once per year ",0,0,0,"Daily average or average over the sampling period","Dust emissions are expected to be towards the lower end of the range when emissions of heavy metals are above the following levels: 1 mg/Nm3 for lead, 1 mg/Nm3 for copper, 0,05 mg/Nm3 for arsenic, 0,05 mg/Nm3 for cadmium"]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Ferro alloys Production","All","Unspecified","Unspecified","Unspecified","Unspecified","— Closed submerged arc furnace or closed plasma\ndust process\n— Refractory-lined crucible for the production of\nferro-molybdenum and ferro-vanadium","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air from a closed submerged arc furnace or a closed plasma dust process, BAT is to use one of the techniques given below: (i) Wet scrubber in combination with an ESP; (ii) Bag filter \n\nIn order to reduce dust and metal emissions to air from a refractory-lined crucible for the\nproduction of ferro-molybdenum and ferro-vanadium, BAT is to use a bag filter.","mg/Nm3",2,5,"Green","Continuous",0,0,0,"As a daily average or as an average over the sampling period.",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Ferro alloys Production","All","Unspecified","Unspecified","Unspecified","Unspecified","— Closed submerged arc furnace or closed plasma\ndust process\n— Refractory-lined crucible for the production of\nferro-molybdenum and ferro-vanadium","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air from a closed submerged arc furnace or a closed plasma dust process, BAT is to use one of the techniques given below: (i) Wet scrubber in combination with an ESP; (ii) Bag filter \n\nIn order to reduce dust and metal emissions to air from a refractory-lined crucible for the\nproduction of ferro-molybdenum and ferro-vanadium, BAT is to use a bag filter.","mg/Nm3",2,5,"Green","Continuous",0,0,0,"As a daily average or as an average over the sampling period.",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Ferro alloys Production","All","Unspecified","Unspecified","Unspecified","Unspecified","— Storage, handling and transport of solid materials — Pretreatment operations such as metering, mixing, blending and degreasing — Tapping, casting and packaging","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air from the storage, handling and transport of solid materials, and from pretreatment operations such as metering, mixing, blending and degreasing, and from tapping, casting and packaging, BAT is to use a bag filter.","mg/Nm3",2,5,"Green","Continuous",0,0,0,"As an average over the sampling period.",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Ferro alloys Production","All","Unspecified","Unspecified","Unspecified","Unspecified","— Storage, handling and transport of solid materials — Pretreatment operations such as metering, mixing, blending and degreasing — Tapping, casting and packaging","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air from the storage, handling and transport of solid materials, and from pretreatment operations such as metering, mixing, blending and degreasing, and from tapping, casting and packaging, BAT is to use a bag filter.","mg/Nm3",2,5,"Green","Continuous",0,0,0,"As an average over the sampling period.",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Ferro alloys Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Crushing, briquetting, pelletising and sintering","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air from crushing, briquetting, pelletising and sintering, BAT is to use a bag filter or a bag filter in combination with other techniques.","mg/Nm3",2,5,"Green","Continuous",0,0,0,"As a daily average or as an average over the sampling period.","\n\nThe upper end of the range can be up to 10 mg/Nm3 for cases where a bag filter cannot be used. ",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Ferro alloys Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Crushing, briquetting, pelletising and sintering","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air from crushing, briquetting, pelletising and sintering, BAT is to use a bag filter or a bag filter in combination with other techniques.","mg/Nm3",2,5,"Green","Continuous",0,0,0,"As a daily average or as an average over the sampling period.","\n\nThe upper end of the range can be up to 10 mg/Nm3 for cases where a bag filter cannot be used. "]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Ferro alloys Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Open or semi-closed submerged arc furnace","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air from an open or a semi-closed submerged arc furnace, BAT is to use a bag filter.","mg/Nm3",2,5,"Green","Continuous",0,0,0,"As a daily average or as an average over the sampling period.","\nThe upper end of the range may be up to 15 mg/Nm3 for the production of FeMn, SiMn, CaSi due to the sticky nature\nof the dust (caused e.g. by its hygroscopic capacity or chemical characteristics) affecting the efficiency of the bag filter. \n\nDust emissions are expected to be towards the lower end of the range when emissions of metals are above the\nfollowing levels: 1 mg/Nm3 for lead, 0,05 mg/Nm3 for cadmium, 0,05 mg/Nm3 for chromiumVI, 0,05 mg/Nm3 for\nthallium.\n",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Ferro alloys Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Open or semi-closed submerged arc furnace","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air from an open or a semi-closed submerged arc furnace, BAT is to use a bag filter.","mg/Nm3",2,5,"Green","Continuous",0,0,0,"As a daily average or as an average over the sampling period.","\nThe upper end of the range may be up to 15 mg/Nm3 for the production of FeMn, SiMn, CaSi due to the sticky nature\nof the dust (caused e.g. by its hygroscopic capacity or chemical characteristics) affecting the efficiency of the bag filter. \n\nDust emissions are expected to be towards the lower end of the range when emissions of metals are above the\nfollowing levels: 1 mg/Nm3 for lead, 0,05 mg/Nm3 for cadmium, 0,05 mg/Nm3 for chromiumVI, 0,05 mg/Nm3 for\nthallium.\n"]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Lead and Tin Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Battery preparation (crushing, screning and classifying) ","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air from battery preparation (crushing, screening and classifying), BAT is to use a bag filter or a wet scrubber.","mg/Nm3","N/A",5,"Green","Once per year",0,0,0,"Average over the sampling period ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Lead and Tin Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Battery preparation (crushing, screning and classifying) ","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air from battery preparation (crushing, screening and classifying), BAT is to use a bag filter or a wet scrubber.","mg/Nm3","N/A",5,"Green","Once per year",0,0,0,"Average over the sampling period ",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Lead and Tin Production","Primary and secondary ","Unspecified","Unspecified","Unspecified","Unspecified","Charging, smelting and tapping","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air (other than those that are routed to the sulphuric acid or liquid SO2 plant) from charging, smelting and tapping in primary and secondary lead and/or tin production, BAT is to use a bag filter.","mg/Nm3",2,4,"Green","Continuous",0,0,0,"Daily average or  average over the sampling period ","Dust emissions are expected to be towards the lower end of the range when emissions are above the following levels: 1 mg/Nm3 for copper, 0,05 mg/Nm3 for arsenic, 0,05 mg/Nm3 for cadmium.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Lead and Tin Production","Primary and secondary ","Unspecified","Unspecified","Unspecified","Unspecified","Charging, smelting and tapping","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air (other than those that are routed to the sulphuric acid or liquid SO2 plant) from charging, smelting and tapping in primary and secondary lead and/or tin production, BAT is to use a bag filter.","mg/Nm3",2,4,"Green","Continuous",0,0,0,"Daily average or  average over the sampling period ","Dust emissions are expected to be towards the lower end of the range when emissions are above the following levels: 1 mg/Nm3 for copper, 0,05 mg/Nm3 for arsenic, 0,05 mg/Nm3 for cadmium."]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Lead and Tin Production","Primary and secondary ","Unspecified","Unspecified","Unspecified","Unspecified","Raw material preparation","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air from raw material preparation (such as reception, handling, storage, metering, mixing, blending, drying, crushing, cutting and screening) in primary and secondary lead/or and tin production, BAT is to use a bag filter.","mg/Nm3","N/A",5,"Green","Continuous",0,0,0,"Daily average or average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Lead and Tin Production","Primary and secondary ","Unspecified","Unspecified","Unspecified","Unspecified","Raw material preparation","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air from raw material preparation (such as reception, handling, storage, metering, mixing, blending, drying, crushing, cutting and screening) in primary and secondary lead/or and tin production, BAT is to use a bag filter.","mg/Nm3","N/A",5,"Green","Continuous",0,0,0,"Daily average or average over the sampling period",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Lead and Tin Production","Primary and secondary ","Unspecified","Unspecified","Unspecified","Unspecified","Remelting, refining and casting","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air from remelting, refining and casting in primary and secondary lead and/or tin production, BAT is to use the techniques given below: (i) For pyrometallurgical processes: maintain the temperature of the melt bath at the lowest possible level\naccording to the process stage in combination with a bag filter; (ii) For hydrometallurgical processes: use a wet scrubber","mg/Nm3",2,4,"Green","Continous",0,0,0,"Daily average or  average over the sampling period ","Dust emissions are expected to be towards the lower end of the range when emissions are above the following levels: 1 mg/Nm3 for copper, 1 mg/Nm3 for antimony, 0,05 mg/Nm3 for arsenic, 0,05 mg/Nm3 for cadmium.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Lead and Tin Production","Primary and secondary ","Unspecified","Unspecified","Unspecified","Unspecified","Remelting, refining and casting","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air from remelting, refining and casting in primary and secondary lead and/or tin production, BAT is to use the techniques given below: (i) For pyrometallurgical processes: maintain the temperature of the melt bath at the lowest possible level\naccording to the process stage in combination with a bag filter; (ii) For hydrometallurgical processes: use a wet scrubber","mg/Nm3",2,4,"Green","Continous",0,0,0,"Daily average or  average over the sampling period ","Dust emissions are expected to be towards the lower end of the range when emissions are above the following levels: 1 mg/Nm3 for copper, 1 mg/Nm3 for antimony, 0,05 mg/Nm3 for arsenic, 0,05 mg/Nm3 for cadmium."]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Metals Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Crushing, sieving, mixing, melting, smelting, incineration, calcining, drying and refining","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air from all dusty operations, such as crushing, sieving, mixing, melting, smelting, incineration, calcining, drying and refining, BAT is to use one of the techniques given below: (i) Bag filter; (ii) Wet scrubber in combination with an ESP, allowing\nthe recovery of selenium","mg/Nm3",2,5,"Green","Continuous",0,0,0,"Daily average or average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Metals Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Crushing, sieving, mixing, melting, smelting, incineration, calcining, drying and refining","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air from all dusty operations, such as crushing, sieving, mixing, melting, smelting, incineration, calcining, drying and refining, BAT is to use one of the techniques given below: (i) Bag filter; (ii) Wet scrubber in combination with an ESP, allowing\nthe recovery of selenium","mg/Nm3",2,5,"Green","Continuous",0,0,0,"Daily average or average over the sampling period",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Nickel and Cobalt Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Handling and storage of raw materials, material pretreatment processes (such as ore preparation and ore/concentrate drying), furnace charging, smelting, converting, thermal refining and nickel powder and briquette production","Air","Particulates (PM10) (24 hr Mean)","When processing sulphidic ores, in order to reduce dust and metal emissions to air from the\nhandling and storage of raw materials, material pretreatment processes (such as ore preparation and ore/concentrate\ndrying), furnace charging, smelting, converting, thermal refining and nickel powder and briquette\nproduction, BAT is to use a bag filter or a combination of an ESP and a bag filter.","mg/Nm3",2,5,"Green","Continuous",0,0,0,"Daily average or average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Nickel and Cobalt Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Handling and storage of raw materials, material pretreatment processes (such as ore preparation and ore/concentrate drying), furnace charging, smelting, converting, thermal refining and nickel powder and briquette production","Air","Particulates (PM10) (24 hr Mean)","When processing sulphidic ores, in order to reduce dust and metal emissions to air from the\nhandling and storage of raw materials, material pretreatment processes (such as ore preparation and ore/concentrate\ndrying), furnace charging, smelting, converting, thermal refining and nickel powder and briquette\nproduction, BAT is to use a bag filter or a combination of an ESP and a bag filter.","mg/Nm3",2,5,"Green","Continuous",0,0,0,"Daily average or average over the sampling period",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Zinc and Cadmium Production","Cadmium Production","Unspecified","Unspecified","Unspecified","Unspecified","Pyrometallurgical cadmium production and the melting, alloying and casting of cadmium ingots","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air from pyrometallurgical cadmium production and the melting, alloying and casting of cadmium ingots, BAT is to use one or a combination of the techniques given below: (i) Bag filter; (ii) ESP; (iii) Wet scrubber ","mg/Nm3",2,3,"Green","Once per year",0,0,0,"Average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Zinc and Cadmium Production","Cadmium Production","Unspecified","Unspecified","Unspecified","Unspecified","Pyrometallurgical cadmium production and the melting, alloying and casting of cadmium ingots","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air from pyrometallurgical cadmium production and the melting, alloying and casting of cadmium ingots, BAT is to use one or a combination of the techniques given below: (i) Bag filter; (ii) ESP; (iii) Wet scrubber ","mg/Nm3",2,3,"Green","Once per year",0,0,0,"Average over the sampling period",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Zinc and Cadmium Production","Hydrometallurgical zinc production","Unspecified","Unspecified","Unspecified","Unspecified","Handling and storage of raw materials, dry roaster feed preparation, dry roaster feeding and calcine processing","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air from the handling and storage of raw materials, dry roaster feed preparation, dry roaster feeding and calcine processing, BAT is to use a bag filter.","mg/Nm3","N/A",5,"Green","Once per year",0,0,0,"Average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Zinc and Cadmium Production","Hydrometallurgical zinc production","Unspecified","Unspecified","Unspecified","Unspecified","Handling and storage of raw materials, dry roaster feed preparation, dry roaster feeding and calcine processing","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air from the handling and storage of raw materials, dry roaster feed preparation, dry roaster feeding and calcine processing, BAT is to use a bag filter.","mg/Nm3","N/A",5,"Green","Once per year",0,0,0,"Average over the sampling period",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Zinc and Cadmium Production","Melting, alloying and casting of zinc ingots and zinc power production","Unspecified","Unspecified","Unspecified","Unspecified","Melting, alloying and casting of zinc ingots and zinc powder production","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air from the melting, alloying and casting of zinc ingots and zinc powder production, BAT is to use a bag filter.","mg/Nm3","N/A",5,"Green","Once per year",0,0,0,"Average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Zinc and Cadmium Production","Melting, alloying and casting of zinc ingots and zinc power production","Unspecified","Unspecified","Unspecified","Unspecified","Melting, alloying and casting of zinc ingots and zinc powder production","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air from the melting, alloying and casting of zinc ingots and zinc powder production, BAT is to use a bag filter.","mg/Nm3","N/A",5,"Green","Once per year",0,0,0,"Average over the sampling period",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Zinc and Cadmium Production","Pyrometallurgical zinc production","Unspecified","Unspecified","Unspecified","Unspecified","Pyrometallurgical zinc production","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air (other than those that are routed to the sulphuric acid plant) from pyrometallurgical zinc production, BAT is to use a bag filter.","mg/Nm3",2,5,"Green","Continuous",0,0,0,"Daily average or average over the sampling period","When a bag filter is not applicable, the upper end of the range is 10 mg/Nm3",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Zinc and Cadmium Production","Pyrometallurgical zinc production","Unspecified","Unspecified","Unspecified","Unspecified","Pyrometallurgical zinc production","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air (other than those that are routed to the sulphuric acid plant) from pyrometallurgical zinc production, BAT is to use a bag filter.","mg/Nm3",2,5,"Green","Continuous",0,0,0,"Daily average or average over the sampling period","When a bag filter is not applicable, the upper end of the range is 10 mg/Nm3"]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Zinc and Cadmium Production","Secondary ","Unspecified","Unspecified","Unspecified","Unspecified","Melting of metallic and mixed metallic/oxidic streams, and from the slag fuming furnace and the Waelz kiln","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air from the melting of metallic and mixed metallic/oxidic streams, and from the slag fuming furnace and the Waelz kiln, BAT is to use a bag filter.","mg/Nm3",2,5,"Green","Once per year",0,0,0,"Daily average or average over the sampling period","A bag filter may not be applicable for a clinker operation (where chlorides need to be abated instead of metal oxides).\n\nWhen a bag filter is not applicable, the upper end of the range may be higher, up to 15 mg/Nm3. \n\n Dust emissions are expected to be towards the lower end of the range when emissions of arsenic or cadmium are\nabove 0,05 mg/Nm3.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Zinc and Cadmium Production","Secondary ","Unspecified","Unspecified","Unspecified","Unspecified","Melting of metallic and mixed metallic/oxidic streams, and from the slag fuming furnace and the Waelz kiln","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air from the melting of metallic and mixed metallic/oxidic streams, and from the slag fuming furnace and the Waelz kiln, BAT is to use a bag filter.","mg/Nm3",2,5,"Green","Once per year",0,0,0,"Daily average or average over the sampling period","A bag filter may not be applicable for a clinker operation (where chlorides need to be abated instead of metal oxides).\n\nWhen a bag filter is not applicable, the upper end of the range may be higher, up to 15 mg/Nm3. \n\n Dust emissions are expected to be towards the lower end of the range when emissions of arsenic or cadmium are\nabove 0,05 mg/Nm3."]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Zinc and Cadmium Production","Secondary ","Unspecified","Unspecified","Unspecified","Unspecified","Pelletising and slag processing","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air from pelletising and slag processing, BAT is to use a bag filter.","mg/Nm3","N/A",5,"Green","Once per year",0,0,0,"Average over the sampling period ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Zinc and Cadmium Production","Secondary ","Unspecified","Unspecified","Unspecified","Unspecified","Pelletising and slag processing","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metal emissions to air from pelletising and slag processing, BAT is to use a bag filter.","mg/Nm3","N/A",5,"Green","Once per year",0,0,0,"Average over the sampling period ",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Aluminium Production","Salt slag recycling process","Unspecified","Unspecified","Unspecified","Unspecified","Wet milling and leaching from the salt slag recovery process","Air","Hydrogen sulphide","In order to reduce gaseous emissions to air from wet milling and leaching from the salt slag recovery process, BAT is to use one or a combination of the techniques given below: (i) Activated carbon injection; (ii) Afterburner; (iii) Wet scrubber with H2SO4 solution","mg/Nm3","N/A",2,"Green","Once per year",0,0,0,"Average over the sampling period ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Aluminium Production","Salt slag recycling process","Unspecified","Unspecified","Unspecified","Unspecified","Wet milling and leaching from the salt slag recovery process","Air","Hydrogen sulphide","In order to reduce gaseous emissions to air from wet milling and leaching from the salt slag recovery process, BAT is to use one or a combination of the techniques given below: (i) Activated carbon injection; (ii) Afterburner; (iii) Wet scrubber with H2SO4 solution","mg/Nm3","N/A",2,"Green","Once per year",0,0,0,"Average over the sampling period ",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Zinc and Cadmium Production","Hydrometallurgical zinc production","Unspecified","Unspecified","Unspecified","Unspecified","Leaching, purification and electrolysis, and to reduce arsane and stibane emissions from purification","Air","Sulphuric acid","In order to reduce zinc and sulphuric acid emissions to air from leaching, purification and electrolysis, and to reduce arsane and stibane emissions from purification, BAT is to use one or a combination of the techniques given below: (i) Wet scrubber; (ii) Demister; (iii) Centrifugal system","mg/Nm3","N/A",10,"Green","Once per year",0,0,0,"Average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Zinc and Cadmium Production","Hydrometallurgical zinc production","Unspecified","Unspecified","Unspecified","Unspecified","Leaching, purification and electrolysis, and to reduce arsane and stibane emissions from purification","Air","Sulphuric acid","In order to reduce zinc and sulphuric acid emissions to air from leaching, purification and electrolysis, and to reduce arsane and stibane emissions from purification, BAT is to use one or a combination of the techniques given below: (i) Wet scrubber; (ii) Demister; (iii) Centrifugal system","mg/Nm3","N/A",10,"Green","Once per year",0,0,0,"Average over the sampling period",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Alumina and Anode production","Secondary aluminium production ","Unspecified","Unspecified","Unspecified","Unspecified","Thermal treatment of contaminated secondary raw materials (e.g. swarf), the melting furnace, and remelting and molten metal treatment","Air","Hydrogen chloride","In order to reduce emissions to air of HCl, Cl2 and HF from the thermal treatment of contaminated secondary raw materials (e.g. swarf), the melting furnace, and remelting and molten metal treatment, BAT is to use one or a combination of the techniques given below: (i) Select and feed the raw materials according to the furnace and the abatement techniques used; (ii) Ca(OH)2 or sodium bicarbonate injection in combination with a bag filter; (iii) Control of the refining process, adapting the quantity of refining gas used to remove the contaminants\npresent into the molten metals; (iv) Use of dilute chlorine with inert gas in the refining process","mg/Nm3",5,10,"Green","Continuous or\nonce per year",0,0,0,"Daily average or  an average over the sampling period","For refining carried out with chemicals containing chlorine, the BAT-AEL refers to the average concentration during chlorination.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Alumina and Anode production","Secondary aluminium production ","Unspecified","Unspecified","Unspecified","Unspecified","Thermal treatment of contaminated secondary raw materials (e.g. swarf), the melting furnace, and remelting and molten metal treatment","Air","Hydrogen chloride","In order to reduce emissions to air of HCl, Cl2 and HF from the thermal treatment of contaminated secondary raw materials (e.g. swarf), the melting furnace, and remelting and molten metal treatment, BAT is to use one or a combination of the techniques given below: (i) Select and feed the raw materials according to the furnace and the abatement techniques used; (ii) Ca(OH)2 or sodium bicarbonate injection in combination with a bag filter; (iii) Control of the refining process, adapting the quantity of refining gas used to remove the contaminants\npresent into the molten metals; (iv) Use of dilute chlorine with inert gas in the refining process","mg/Nm3",5,10,"Green","Continuous or\nonce per year",0,0,0,"Daily average or  an average over the sampling period","For refining carried out with chemicals containing chlorine, the BAT-AEL refers to the average concentration during chlorination."]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Metals Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Hydrometallurgical operation, including the associated incineration, calcining and drying operations","Air","Hydrogen chloride","In order to reduce HCl and Cl2 emissions to air from a hydrometallurgical operation, including the associated incineration, calcining and drying operations, BAT is to use an alkaline scrubber.","mg/Nm3",5,10,"Green","Once per year",0,0,0,"Average over the sampling period ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Metals Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Hydrometallurgical operation, including the associated incineration, calcining and drying operations","Air","Hydrogen chloride","In order to reduce HCl and Cl2 emissions to air from a hydrometallurgical operation, including the associated incineration, calcining and drying operations, BAT is to use an alkaline scrubber.","mg/Nm3",5,10,"Green","Once per year",0,0,0,"Average over the sampling period ",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Zinc and Cadmium Production","Secondary ","Unspecified","Unspecified","Unspecified","Unspecified","Melting of metallic and mixed metallic/oxidic streams, and from the slag fuming furnace and the Waelz kiln","Air","Hydrogen chloride","In order to reduce emissions of HCl and HF to air from the melting of metallic and mixed metallic/oxidic streams, and from the slag fuming furnace and the Waelz kiln, BAT is to use one of the techniques given below: (i) Injection of adsorbent followed by a bag filter; (ii) Wet scrubber ","mg/Nm3","N/A",1.5,"Green","Once per year",0,0,0,"Average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Zinc and Cadmium Production","Secondary ","Unspecified","Unspecified","Unspecified","Unspecified","Melting of metallic and mixed metallic/oxidic streams, and from the slag fuming furnace and the Waelz kiln","Air","Hydrogen chloride","In order to reduce emissions of HCl and HF to air from the melting of metallic and mixed metallic/oxidic streams, and from the slag fuming furnace and the Waelz kiln, BAT is to use one of the techniques given below: (i) Injection of adsorbent followed by a bag filter; (ii) Wet scrubber ","mg/Nm3","N/A",1.5,"Green","Once per year",0,0,0,"Average over the sampling period",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Alumina and Anode production","Anode production","Unspecified ","Unspecified","Unspecified","Unspecified","Baking plant in a stand-alone anode production plant","Air","Hydrogen fluoride (as F) (Ecological - Daily Mean)","In order to reduce dust, PAH and fluoride emissions to air from a baking plant in a stand-alone anode production plant, BAT is to use a pre-filtration unit and a regenerative thermal oxidiser followed by a dry scrubber (e.g. lime bed)","mg/Nm3","N/A",3,"Green","Continuous",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Alumina and Anode production","Anode production","Unspecified ","Unspecified","Unspecified","Unspecified","Baking plant in a stand-alone anode production plant","Air","Hydrogen fluoride (as F) (Ecological - Daily Mean)","In order to reduce dust, PAH and fluoride emissions to air from a baking plant in a stand-alone anode production plant, BAT is to use a pre-filtration unit and a regenerative thermal oxidiser followed by a dry scrubber (e.g. lime bed)","mg/Nm3","N/A",3,"Green","Continuous",0,0,0,"Daily average",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Alumina and Anode production","Anode production","Unspecified ","Unspecified","Unspecified","Unspecified","Baking plant with a primary aluminium smelter ","Air","Hydrogen fluoride (as F) (Ecological - Daily Mean)","In order to reduce dust, sulphur dioxide, PAH and fluoride emissions to air from a baking plant in an anode production plant integrated with a primary aluminium smelter, BAT is to use one or a combination of the techniques given below: (i) Use of raw materials and fuels containing a\nlow amount of sulphur; (ii) Dry scrubber using alumina as the adsorbent\nagent followed by a bag filter; (iii) Wet scrubber; (iv) Regenerative thermal oxidiser in combination\nwith a dust abatement system","mg/Nm3",0.3,0.5,"Green","Continuous",0,0,0,"Daily average or as an average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Alumina and Anode production","Anode production","Unspecified ","Unspecified","Unspecified","Unspecified","Baking plant with a primary aluminium smelter ","Air","Hydrogen fluoride (as F) (Ecological - Daily Mean)","In order to reduce dust, sulphur dioxide, PAH and fluoride emissions to air from a baking plant in an anode production plant integrated with a primary aluminium smelter, BAT is to use one or a combination of the techniques given below: (i) Use of raw materials and fuels containing a\nlow amount of sulphur; (ii) Dry scrubber using alumina as the adsorbent\nagent followed by a bag filter; (iii) Wet scrubber; (iv) Regenerative thermal oxidiser in combination\nwith a dust abatement system","mg/Nm3",0.3,0.5,"Green","Continuous",0,0,0,"Daily average or as an average over the sampling period",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Alumina and Anode production","Primary aluminium production","Unspecified","Unspecified","Unspecified","Unspecified","Electrolytic cells","Air","Hydrogen fluoride (as F) (Ecological - Daily Mean)","In order to reduce dust, metal and fluoride emissions to air from electrolytic cells, BAT is to use one of the techniques given below: (i) Dry scrubber using alumina as the adsorbent agent\nfollowed by a bag filter; (ii) Dry scrubber using alumina as the adsorbent agent\nfollowed by a bag filter and a wet scrubber","mg/Nm3","N/A",1,"Green","Continuous or\nonce per year",0,0,0,"Daily average or average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Alumina and Anode production","Primary aluminium production","Unspecified","Unspecified","Unspecified","Unspecified","Electrolytic cells","Air","Hydrogen fluoride (as F) (Ecological - Daily Mean)","In order to reduce dust, metal and fluoride emissions to air from electrolytic cells, BAT is to use one of the techniques given below: (i) Dry scrubber using alumina as the adsorbent agent\nfollowed by a bag filter; (ii) Dry scrubber using alumina as the adsorbent agent\nfollowed by a bag filter and a wet scrubber","mg/Nm3","N/A",1,"Green","Continuous or\nonce per year",0,0,0,"Daily average or average over the sampling period",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Alumina and Anode production","Secondary aluminium production ","Unspecified","Unspecified","Unspecified","Unspecified","Thermal treatment of contaminated secondary raw materials (e.g. swarf), the melting furnace, and remelting and molten metal treatment","Air","Hydrogen fluoride (as F) (Ecological - Daily Mean)","In order to reduce emissions to air of HCl, Cl2 and HF from the thermal treatment of contaminated secondary raw materials (e.g. swarf), the melting furnace, and remelting and molten metal treatment, BAT is to use one or a combination of the techniques given below: (i) Select and feed the raw materials according to the furnace and the abatement techniques used; (ii) Ca(OH)2 or sodium bicarbonate injection in combination with a bag filter; (iii) Control of the refining process, adapting the quantity of refining gas used to remove the contaminants\npresent into the molten metals; (iv) Use of dilute chlorine with inert gas in the refining process","mg/Nm3","N/A",1,"Green","Once per year",0,0,0,"Average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Alumina and Anode production","Secondary aluminium production ","Unspecified","Unspecified","Unspecified","Unspecified","Thermal treatment of contaminated secondary raw materials (e.g. swarf), the melting furnace, and remelting and molten metal treatment","Air","Hydrogen fluoride (as F) (Ecological - Daily Mean)","In order to reduce emissions to air of HCl, Cl2 and HF from the thermal treatment of contaminated secondary raw materials (e.g. swarf), the melting furnace, and remelting and molten metal treatment, BAT is to use one or a combination of the techniques given below: (i) Select and feed the raw materials according to the furnace and the abatement techniques used; (ii) Ca(OH)2 or sodium bicarbonate injection in combination with a bag filter; (iii) Control of the refining process, adapting the quantity of refining gas used to remove the contaminants\npresent into the molten metals; (iv) Use of dilute chlorine with inert gas in the refining process","mg/Nm3","N/A",1,"Green","Once per year",0,0,0,"Average over the sampling period",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Zinc and Cadmium Production","Secondary ","Unspecified","Unspecified","Unspecified","Unspecified","Melting of metallic and mixed metallic/oxidic streams, and from the slag fuming furnace and the Waelz kiln","Air","Hydrogen fluoride (as F) (Ecological - Daily Mean)","In order to reduce emissions of HCl and HF to air from the melting of metallic and mixed metallic/oxidic streams, and from the slag fuming furnace and the Waelz kiln, BAT is to use one of the techniques given below: (i) Injection of adsorbent followed by a bag filter; (ii) Wet scrubber ","mg/Nm3","N/A",0.3,"Green","Once per year",0,0,0,"Average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Zinc and Cadmium Production","Secondary ","Unspecified","Unspecified","Unspecified","Unspecified","Melting of metallic and mixed metallic/oxidic streams, and from the slag fuming furnace and the Waelz kiln","Air","Hydrogen fluoride (as F) (Ecological - Daily Mean)","In order to reduce emissions of HCl and HF to air from the melting of metallic and mixed metallic/oxidic streams, and from the slag fuming furnace and the Waelz kiln, BAT is to use one of the techniques given below: (i) Injection of adsorbent followed by a bag filter; (ii) Wet scrubber ","mg/Nm3","N/A",0.3,"Green","Once per year",0,0,0,"Average over the sampling period",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","All","All","Unspecified ","Unspecified","Unspecified","Unspecified","Pyrometallurgical process","Air","Mercury and compounds, except mercury alkyls, (as","In order to reduce mercury emissions to air (other than those that are routed to the sulphuric acid plant) from a pyrometallurgical process, BAT is to use one or both of the techniques given below: (i) Use raw materials with a low mercury content, including by cooperating with providers in order to\nremove mercury from secondary materials; (ii) Use adsorbents (e.g. activated carbon, selenium) in combination with dust filtration","mg/Nm3",0.01,0.05,"Green","Continuous or\nonce per year",0,0,0,"Daily average or average over the sampling period","As a daily average or as an average over the sampling period.\n\nThe lower end of the range is associated with the use of adsorbents (e.g. activated carbon, selenium) in combination\nwith dust filtration, except for processes using Waelz kilns.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","All","All","Unspecified ","Unspecified","Unspecified","Unspecified","Pyrometallurgical process","Air","Mercury and compounds, except mercury alkyls, (as","In order to reduce mercury emissions to air (other than those that are routed to the sulphuric acid plant) from a pyrometallurgical process, BAT is to use one or both of the techniques given below: (i) Use raw materials with a low mercury content, including by cooperating with providers in order to\nremove mercury from secondary materials; (ii) Use adsorbents (e.g. activated carbon, selenium) in combination with dust filtration","mg/Nm3",0.01,0.05,"Green","Continuous or\nonce per year",0,0,0,"Daily average or average over the sampling period","As a daily average or as an average over the sampling period.\n\nThe lower end of the range is associated with the use of adsorbents (e.g. activated carbon, selenium) in combination\nwith dust filtration, except for processes using Waelz kilns."]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Aluminium Production","Salt slag recycling process","Unspecified","Unspecified","Unspecified","Unspecified","Wet milling and leaching from the salt slag recovery process","Air","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce gaseous emissions to air from wet milling and leaching from the salt slag recovery process, BAT is to use one or a combination of the techniques given below: (i) Activated carbon injection; (ii) Afterburner; (iii) Wet scrubber with H2SO4 solution","mg/Nm3","N/A",10,"Green","Once per year",0,0,0,"Average over the sampling period ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Aluminium Production","Salt slag recycling process","Unspecified","Unspecified","Unspecified","Unspecified","Wet milling and leaching from the salt slag recovery process","Air","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce gaseous emissions to air from wet milling and leaching from the salt slag recovery process, BAT is to use one or a combination of the techniques given below: (i) Activated carbon injection; (ii) Afterburner; (iii) Wet scrubber with H2SO4 solution","mg/Nm3","N/A",10,"Green","Once per year",0,0,0,"Average over the sampling period ",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Metals Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Hydrometallurgical operation using ammonia or ammonium chloride","Air","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce NH3 emissions to air from a hydrometallurgical operation using ammonia or ammonium chloride, BAT is to use a wet scrubber with sulphuric acid.","mg/Nm3",1,3,"Green","Once per year",0,0,0,"Average over the sampling period ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Metals Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Hydrometallurgical operation using ammonia or ammonium chloride","Air","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce NH3 emissions to air from a hydrometallurgical operation using ammonia or ammonium chloride, BAT is to use a wet scrubber with sulphuric acid.","mg/Nm3",1,3,"Green","Once per year",0,0,0,"Average over the sampling period ",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Nickel and Cobalt Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Atmospheric or pressure leaching processes","Air","Nickel (total Ni compounds in the PM10 fraction)","In order to reduce nickel and chlorine emissions to air from the atmospheric or pressure leaching processes, BAT is to use a wet scrubber.","mg/Nm3","N/A",1,"Green","Once per year",0,0,0,"Average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Nickel and Cobalt Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Atmospheric or pressure leaching processes","Air","Nickel (total Ni compounds in the PM10 fraction)","In order to reduce nickel and chlorine emissions to air from the atmospheric or pressure leaching processes, BAT is to use a wet scrubber.","mg/Nm3","N/A",1,"Green","Once per year",0,0,0,"Average over the sampling period",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Nickel and Cobalt Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Nickel matte refining process using ferric\nchloride with chlorine","Air","Nickel (total Ni compounds in the PM10 fraction)","In order to reduce nickel emissions to air from the nickel matte refining process using ferric chloride with chlorine, BAT is to use a bag filter.","mg/Nm3","N/A",1,"Green","Once per year",0,0,0,"Average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Nickel and Cobalt Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Nickel matte refining process using ferric\nchloride with chlorine","Air","Nickel (total Ni compounds in the PM10 fraction)","In order to reduce nickel emissions to air from the nickel matte refining process using ferric chloride with chlorine, BAT is to use a bag filter.","mg/Nm3","N/A",1,"Green","Once per year",0,0,0,"Average over the sampling period",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Metals Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Hydrometallurgical operation involving dissolving/leaching with nitric acid","Air","Nitrogen dioxide","In order to reduce NOX emissions to air from a hydrometallurgical operation involving dissolving/leaching with nitric acid, BAT is to use one or both of the techniques given below: (i)Alkaline scrubber with caustic soda; (ii) Scrubber with oxidation agents (e.g. oxygen, hydrogen peroxide) and reducing agents (e.g. nitric acid,\nurea) for those vessels in hydrometallurgical operations with the potential to generate high concentrations\nof NOX. It is often applied in combination with (i) \n","mg/Nm3",70,150,"Green","Continuous or once per year",0,0,0,"Hourly average or average over the sampling period ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Metals Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Hydrometallurgical operation involving dissolving/leaching with nitric acid","Air","Nitrogen dioxide","In order to reduce NOX emissions to air from a hydrometallurgical operation involving dissolving/leaching with nitric acid, BAT is to use one or both of the techniques given below: (i)Alkaline scrubber with caustic soda; (ii) Scrubber with oxidation agents (e.g. oxygen, hydrogen peroxide) and reducing agents (e.g. nitric acid,\nurea) for those vessels in hydrometallurgical operations with the potential to generate high concentrations\nof NOX. It is often applied in combination with (i) \n","mg/Nm3",70,150,"Green","Continuous or once per year",0,0,0,"Hourly average or average over the sampling period ",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Lead and Tin Production","Primary and secondary ","Unspecified","Unspecified","Unspecified","Unspecified","Charging, smelting and tapping","Air","Lead","In order to reduce dust and metal emissions to air (other than those that are routed to the sulphuric acid or liquid SO2 plant) from charging, smelting and tapping in primary and secondary lead and/or tin production, BAT is to use a bag filter.","mg/Nm3","N/A",1,"Green","Once per year",0,0,0,"Average over the sampling period ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Lead and Tin Production","Primary and secondary ","Unspecified","Unspecified","Unspecified","Unspecified","Charging, smelting and tapping","Air","Lead","In order to reduce dust and metal emissions to air (other than those that are routed to the sulphuric acid or liquid SO2 plant) from charging, smelting and tapping in primary and secondary lead and/or tin production, BAT is to use a bag filter.","mg/Nm3","N/A",1,"Green","Once per year",0,0,0,"Average over the sampling period ",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Lead and Tin Production","Primary and secondary ","Unspecified","Unspecified","Unspecified","Unspecified","Remelting, refining and casting","Air","Lead","In order to reduce dust and metal emissions to air from remelting, refining and casting in primary and secondary lead and/or tin production, BAT is to use the techniques given below: (i) For pyrometallurgical processes: maintain the temperature of the melt bath at the lowest possible level\naccording to the process stage in combination with a bag filter; (ii) For hydrometallurgical processes: use a wet scrubber","mg/Nm3","N/A",1,"Green","Once per year",0,0,0,"Average over the sampling period ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Lead and Tin Production","Primary and secondary ","Unspecified","Unspecified","Unspecified","Unspecified","Remelting, refining and casting","Air","Lead","In order to reduce dust and metal emissions to air from remelting, refining and casting in primary and secondary lead and/or tin production, BAT is to use the techniques given below: (i) For pyrometallurgical processes: maintain the temperature of the melt bath at the lowest possible level\naccording to the process stage in combination with a bag filter; (ii) For hydrometallurgical processes: use a wet scrubber","mg/Nm3","N/A",1,"Green","Once per year",0,0,0,"Average over the sampling period ",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Alumina and Anode production","Secondary aluminium production ","Unspecified","Unspecified","Unspecified","Unspecified","Thermal treatment of contaminated secondary raw materials (e.g. swarf) and from the melting furnace","Air","PCDD/F","In order to reduce emissions to air of organic compounds and PCDD/F from the thermal treatment of contaminated secondary raw materials (e.g. swarf) and from the melting furnace, BAT is to use a bag filter in combination with at least one of the techniques given below: (i) Select and feed the raw materials according to the furnace and the abatement techniques used; (ii) Internal burner system for melting furnaces; (iii) Afterburner; (iv) Rapid quenching; (v) Activated carbon injection","ng I-TEQ/Nm3","N/A",0.1,"Green","Once per year",0,0,0,"Average over sampling period of atleast 6 hours"," ",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Alumina and Anode production","Secondary aluminium production ","Unspecified","Unspecified","Unspecified","Unspecified","Thermal treatment of contaminated secondary raw materials (e.g. swarf) and from the melting furnace","Air","PCDD/F","In order to reduce emissions to air of organic compounds and PCDD/F from the thermal treatment of contaminated secondary raw materials (e.g. swarf) and from the melting furnace, BAT is to use a bag filter in combination with at least one of the techniques given below: (i) Select and feed the raw materials according to the furnace and the abatement techniques used; (ii) Internal burner system for melting furnaces; (iii) Afterburner; (iv) Rapid quenching; (v) Activated carbon injection","ng I-TEQ/Nm3","N/A",0.1,"Green","Once per year",0,0,0,"Average over sampling period of atleast 6 hours"," "]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Copper production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Pyrolytic treatment of copper turnings, smelting, melting, fire refining and converting operations in secondary copper production","Air","PCDD/F","In order to reduce PCDD/F emissions to air from the pyrolytic treatment of copper turnings, smelting, melting, fire refining and converting operations in secondary copper production, BAT is to use one or a combination of the techniques given below: (i) Select and feed the raw materials according to the furnace and the abatement techniques used; (ii) Optimise combustion conditions to reduce the emissions of organic compounds; (iii) Use charging systems, for a semi-closed furnace, to give small additions of raw material; (iv) Thermal destruction of PCDD/F in the furnace at high temperatures (> 850 °C); (v) Use oxygen injection in the upper zone of the furnace; (vi) Internal burner system; (vi) Post-combustion chamber or afterburner or regenerative thermal oxidiser; (vii) Avoid exhaust systems with a high dust build-up for temperatures > 250 °C; (viii) Rapid quenching; (ix) Injection of adsorption agent in combination with an efficient dust collection system\n\n","ng I-TEQ/Nm3","N/A",0.1,"Green","Once per year ",0,0,0,"Average over a sampling period of at least six hours",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Copper production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Pyrolytic treatment of copper turnings, smelting, melting, fire refining and converting operations in secondary copper production","Air","PCDD/F","In order to reduce PCDD/F emissions to air from the pyrolytic treatment of copper turnings, smelting, melting, fire refining and converting operations in secondary copper production, BAT is to use one or a combination of the techniques given below: (i) Select and feed the raw materials according to the furnace and the abatement techniques used; (ii) Optimise combustion conditions to reduce the emissions of organic compounds; (iii) Use charging systems, for a semi-closed furnace, to give small additions of raw material; (iv) Thermal destruction of PCDD/F in the furnace at high temperatures (> 850 °C); (v) Use oxygen injection in the upper zone of the furnace; (vi) Internal burner system; (vi) Post-combustion chamber or afterburner or regenerative thermal oxidiser; (vii) Avoid exhaust systems with a high dust build-up for temperatures > 250 °C; (viii) Rapid quenching; (ix) Injection of adsorption agent in combination with an efficient dust collection system\n\n","ng I-TEQ/Nm3","N/A",0.1,"Green","Once per year ",0,0,0,"Average over a sampling period of at least six hours",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Ferro alloys Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Furnace producing ferro-alloys","Air","PCDD/F","In order to reduce PCDD/F emissions to air from a furnace producing ferro-alloys, BAT is to inject adsorbents and to use an ESP and/or a bag filter.","ng I-TEQ/Nm3","N/A",0.05,"Green","Once per year",0,0,0,"As an average over the sampling period.",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Ferro alloys Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Furnace producing ferro-alloys","Air","PCDD/F","In order to reduce PCDD/F emissions to air from a furnace producing ferro-alloys, BAT is to inject adsorbents and to use an ESP and/or a bag filter.","ng I-TEQ/Nm3","N/A",0.05,"Green","Once per year",0,0,0,"As an average over the sampling period.",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Lead and Tin Production","Secondary ","Unspecified","Unspecified","Unspecified","Unspecified","Smelting of raw materials","Air","PCDD/F","In order to reduce PCDD/F emissions to air from the smelting of secondary lead and/or tin raw materials, BAT is to use one or a combination of the techniques given below: (i) Select and feed the raw materials according to the furnace and the abatement techniques used; (ii) Use charging systems, for a semi-closed furnace, to give small additions of raw material; (iii) Internal burner system for melting furnaces; (iv) Afterburner or regenerative thermal oxidiser; (v) Avoid exhaust systems with a high dust build-up at temperatures > 250 °C; (vi) Rapid quenching; (vii) Injection of adsorption agent in combination with efficient dust collection system; (viii) Use of efficient dust collection system; (ix) Use of oxygen injection in the upper zone of the furnace; (x) Optimise combustion conditions to reduce the emissions of organic compounds","ng I-TEQ/Nm3","N/A",0.1,"Green","Once per year",0,0,0,"Average over a sampling period of at least six hours",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Lead and Tin Production","Secondary ","Unspecified","Unspecified","Unspecified","Unspecified","Smelting of raw materials","Air","PCDD/F","In order to reduce PCDD/F emissions to air from the smelting of secondary lead and/or tin raw materials, BAT is to use one or a combination of the techniques given below: (i) Select and feed the raw materials according to the furnace and the abatement techniques used; (ii) Use charging systems, for a semi-closed furnace, to give small additions of raw material; (iii) Internal burner system for melting furnaces; (iv) Afterburner or regenerative thermal oxidiser; (v) Avoid exhaust systems with a high dust build-up at temperatures > 250 °C; (vi) Rapid quenching; (vii) Injection of adsorption agent in combination with efficient dust collection system; (viii) Use of efficient dust collection system; (ix) Use of oxygen injection in the upper zone of the furnace; (x) Optimise combustion conditions to reduce the emissions of organic compounds","ng I-TEQ/Nm3","N/A",0.1,"Green","Once per year",0,0,0,"Average over a sampling period of at least six hours",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Metals Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Drying operation where the raw materials contain organic compounds, halogens or other PCDD/F precursors, from an incineration operation, and from a calcining operation","Air","PCDD/F","In order to reduce PCDD/F emissions to air from a drying operation where the raw materials contain organic compounds, halogens or other PCDD/F precursors, from an incineration operation, and from a calcining operation, BAT is to use one or a combination of the techniques given below: (i) Afterburner or regenerative thermal oxidiser; (ii) Injection of adsorption agent in combination with an efficient dust collection system; (iii) Optimise combustion or process conditions for the abatement of emissions of organic compounds; (iv) Avoid exhaust systems with a high dust build-up for temperatures > 250 °C; (v) Rapid quenching; (vi) Thermal destruction of PCDD/F in the furnace at high temperatures (> 850 °C); (vii) Use of oxygen injection in the upper zone of the furnace; (viii) Internal burner system","ng I-TEQ/Nm3","N/A",0.1,"Green","Once per year",0,0,0,"Average over a sampling period of at least six hours",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Metals Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Drying operation where the raw materials contain organic compounds, halogens or other PCDD/F precursors, from an incineration operation, and from a calcining operation","Air","PCDD/F","In order to reduce PCDD/F emissions to air from a drying operation where the raw materials contain organic compounds, halogens or other PCDD/F precursors, from an incineration operation, and from a calcining operation, BAT is to use one or a combination of the techniques given below: (i) Afterburner or regenerative thermal oxidiser; (ii) Injection of adsorption agent in combination with an efficient dust collection system; (iii) Optimise combustion or process conditions for the abatement of emissions of organic compounds; (iv) Avoid exhaust systems with a high dust build-up for temperatures > 250 °C; (v) Rapid quenching; (vi) Thermal destruction of PCDD/F in the furnace at high temperatures (> 850 °C); (vii) Use of oxygen injection in the upper zone of the furnace; (viii) Internal burner system","ng I-TEQ/Nm3","N/A",0.1,"Green","Once per year",0,0,0,"Average over a sampling period of at least six hours",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Zinc and Cadmium Production","Secondary ","Unspecified","Unspecified","Unspecified","Unspecified","Melting of metallic and mixed metallic/oxidic streams, and from the slag fuming furnace and the Waelz kiln","Air","PCDD/F","Melting of metallic and mixed metallic/oxidic streams, and from the slag fuming furnace and the Waelz kiln: (i) Injection of adsorbent (activated carbon or lignite coke)\nfollowed by a bag filter and/or ESP; (ii) Thermal oxidiser; (iii) Regenerative thermal oxidiser ","ng I-TEQ/Nm3","N/A",0.1,"Green","Once per year",0,0,0,"Average over sampling period of atleast 6 hours",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Zinc and Cadmium Production","Secondary ","Unspecified","Unspecified","Unspecified","Unspecified","Melting of metallic and mixed metallic/oxidic streams, and from the slag fuming furnace and the Waelz kiln","Air","PCDD/F","Melting of metallic and mixed metallic/oxidic streams, and from the slag fuming furnace and the Waelz kiln: (i) Injection of adsorbent (activated carbon or lignite coke)\nfollowed by a bag filter and/or ESP; (ii) Thermal oxidiser; (iii) Regenerative thermal oxidiser ","ng I-TEQ/Nm3","N/A",0.1,"Green","Once per year",0,0,0,"Average over sampling period of atleast 6 hours",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Aluminium Production","Salt slag recycling process","Unspecified","Unspecified","Unspecified","Unspecified","Wet milling and leaching from the salt slag recovery process","Air","Phosphine","In order to reduce gaseous emissions to air from wet milling and leaching from the salt slag recovery process, BAT is to use one or a combination of the techniques given below: (i) Activated carbon injection; (ii) Afterburner; (iii) Wet scrubber with H2SO4 solution","mg/Nm3","N/A",0.5,"Green","Once per year",0,0,0,"Average over the sampling period ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Aluminium Production","Salt slag recycling process","Unspecified","Unspecified","Unspecified","Unspecified","Wet milling and leaching from the salt slag recovery process","Air","Phosphine","In order to reduce gaseous emissions to air from wet milling and leaching from the salt slag recovery process, BAT is to use one or a combination of the techniques given below: (i) Activated carbon injection; (ii) Afterburner; (iii) Wet scrubber with H2SO4 solution","mg/Nm3","N/A",0.5,"Green","Once per year",0,0,0,"Average over the sampling period ",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Alumina and Anode production","Primary aluminium production","Unspecified","Unspecified","Unspecified","Unspecified","Electrolytic cells","Air","Sulphur Dioxide (24 Hour Mean)","In order to reduce emissions to air from electrolytic cells, BAT is to use one or both of the techniques given below: (i) Use of low-sulphur anodes; (ii) Wet scrubber","kg/t Al",2.5,15,"Green","Continuous or\nonce per year",0,0,0,"As mass of pollutant emitted during a year divided by the mass of liquid aluminium produced in the same year.","Anodes containing less than 1,5 % sulphur as a yearly average can be produced by an appropriate\ncombination of the raw materials used. A minimum sulphur content of 0,9 % as a yearly average is required\nfor the viability of the electrolysis process.\n\n The lower end of the range is associated with the use of a wet scrubber. The higher end of the range is associated with\nthe use of low-sulphur anodes.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Alumina and Anode production","Primary aluminium production","Unspecified","Unspecified","Unspecified","Unspecified","Electrolytic cells","Air","Sulphur Dioxide (24 Hour Mean)","In order to reduce emissions to air from electrolytic cells, BAT is to use one or both of the techniques given below: (i) Use of low-sulphur anodes; (ii) Wet scrubber","kg/t Al",2.5,15,"Green","Continuous or\nonce per year",0,0,0,"As mass of pollutant emitted during a year divided by the mass of liquid aluminium produced in the same year.","Anodes containing less than 1,5 % sulphur as a yearly average can be produced by an appropriate\ncombination of the raw materials used. A minimum sulphur content of 0,9 % as a yearly average is required\nfor the viability of the electrolysis process.\n\n The lower end of the range is associated with the use of a wet scrubber. The higher end of the range is associated with\nthe use of low-sulphur anodes."]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Copper production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Primary copper production ","Air","Sulphur Dioxide (24 Hour Mean)","In order to reduce SO2 emissions (other than those that are routed to the sulphuric acid or liquid SO2 plant or power plant) from primary and secondary copper production, BAT is to use one or a combination of the techniques given below: (i) Dry or semi-dry scrubber; (ii) Wet scrubber ; (iii) Polyether-based absorption/desorption system ","mg/Nm3",50,500,"Green","Continuous or\nonce per year",0,0,0,"Daily average or as an average over the sampling period","In the case of using a wet scrubber or a concentrate with a low sulphur content, the BAT-AEL can be up to 350 mg/Nm3",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Copper production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Primary copper production ","Air","Sulphur Dioxide (24 Hour Mean)","In order to reduce SO2 emissions (other than those that are routed to the sulphuric acid or liquid SO2 plant or power plant) from primary and secondary copper production, BAT is to use one or a combination of the techniques given below: (i) Dry or semi-dry scrubber; (ii) Wet scrubber ; (iii) Polyether-based absorption/desorption system ","mg/Nm3",50,500,"Green","Continuous or\nonce per year",0,0,0,"Daily average or as an average over the sampling period","In the case of using a wet scrubber or a concentrate with a low sulphur content, the BAT-AEL can be up to 350 mg/Nm3"]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Copper production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Secondary copper production ","Air","Sulphur Dioxide (24 Hour Mean)","In order to reduce SO2 emissions (other than those that are routed to the sulphuric acid or liquid SO2 plant or power plant) from primary and secondary copper production, BAT is to use one or a combination of the techniques given below: (i) Dry or semi-dry scrubber; (ii) Wet scrubber ; (iii) Polyether-based absorption/desorption system ","mg/Nm3",50,300,"Green","Continuous or\nonce per year",0,0,0,"Daily average or as an average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Copper production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Secondary copper production ","Air","Sulphur Dioxide (24 Hour Mean)","In order to reduce SO2 emissions (other than those that are routed to the sulphuric acid or liquid SO2 plant or power plant) from primary and secondary copper production, BAT is to use one or a combination of the techniques given below: (i) Dry or semi-dry scrubber; (ii) Wet scrubber ; (iii) Polyether-based absorption/desorption system ","mg/Nm3",50,300,"Green","Continuous or\nonce per year",0,0,0,"Daily average or as an average over the sampling period",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Lead and Tin Production","Primary and secondary ","Unspecified","Unspecified","Unspecified","Unspecified","Charging, smelting and tapping","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SO2 emissions to air (other than those that are routed to the sulphuric acid or liquid SO2 plant) from charging, smelting and tapping in primary and secondary lead and/or tin production, BAT is to use one or a combination of the techniques given below: (i) Alkaline leaching of raw materials that contain sulphur\nin the form of sulphate; (ii) Dry or semi-dry scrubber; (iii) Wet scrubber; (iv) Fixation of sulphur in the smelt phase ","mg/Nm3",50,350,"Green","Continuous or once per year",0,0,0,"Daily average or average over the sampling period","When wet scrubbers are not applicable, the upper end of the range is 500 mg/Nm3.\n\nAn alkali salt solution is used to remove sulphates from secondary materials prior to smelting.\n\nThe fixation of sulphur in the smelt phase is achieved by adding iron and soda (Na2CO3) in the\nsmelters which react with the sulphur contained in the raw materials to form Na2S-FeS slag",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Lead and Tin Production","Primary and secondary ","Unspecified","Unspecified","Unspecified","Unspecified","Charging, smelting and tapping","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SO2 emissions to air (other than those that are routed to the sulphuric acid or liquid SO2 plant) from charging, smelting and tapping in primary and secondary lead and/or tin production, BAT is to use one or a combination of the techniques given below: (i) Alkaline leaching of raw materials that contain sulphur\nin the form of sulphate; (ii) Dry or semi-dry scrubber; (iii) Wet scrubber; (iv) Fixation of sulphur in the smelt phase ","mg/Nm3",50,350,"Green","Continuous or once per year",0,0,0,"Daily average or average over the sampling period","When wet scrubbers are not applicable, the upper end of the range is 500 mg/Nm3.\n\nAn alkali salt solution is used to remove sulphates from secondary materials prior to smelting.\n\nThe fixation of sulphur in the smelt phase is achieved by adding iron and soda (Na2CO3) in the\nsmelters which react with the sulphur contained in the raw materials to form Na2S-FeS slag"]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Metals Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Hydrometallurgical operation, including the associated incineration, calcining and drying operations","Air","Sulphur Dioxide (24 Hour Mean)","In order to reduce SO2 emissions to air from a hydrometallurgical operation, including the associated incineration, calcining and drying operations, BAT is to use a wet scrubber.","mg/Nm3",50,100,"Green","Continuous or once per year",0,0,0,"Daily average or average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Metals Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Hydrometallurgical operation, including the associated incineration, calcining and drying operations","Air","Sulphur Dioxide (24 Hour Mean)","In order to reduce SO2 emissions to air from a hydrometallurgical operation, including the associated incineration, calcining and drying operations, BAT is to use a wet scrubber.","mg/Nm3",50,100,"Green","Continuous or once per year",0,0,0,"Daily average or average over the sampling period",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Metals Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Melting and smelting operation for the production of Doré metal, including the associated incineration, calcining and drying operations","Air","Sulphur Dioxide (24 Hour Mean)","In order to reduce SO2 emissions to air (other than those that are routed to the sulphuric acid plant) from a melting and smelting operation for the production of Doré metal, including the associated incineration, calcining and drying operations, BAT is to use one or a combination of the techniques given below: (i) Lime injection in combination with a bag filter; (ii) Wet scrubber","mg/Nm3",50,480,"Green","Continuous or once per year",0,0,0,"Daily average or average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Metals Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Melting and smelting operation for the production of Doré metal, including the associated incineration, calcining and drying operations","Air","Sulphur Dioxide (24 Hour Mean)","In order to reduce SO2 emissions to air (other than those that are routed to the sulphuric acid plant) from a melting and smelting operation for the production of Doré metal, including the associated incineration, calcining and drying operations, BAT is to use one or a combination of the techniques given below: (i) Lime injection in combination with a bag filter; (ii) Wet scrubber","mg/Nm3",50,480,"Green","Continuous or once per year",0,0,0,"Daily average or average over the sampling period",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Zinc and Cadmium Production","Pyrometallurgical zinc production","Unspecified","Unspecified","Unspecified","Unspecified","Pyrometallurgical zinc production","Air","Sulphur Dioxide (24 Hour Mean)","In order to reduce SO2 emissions to air (other than those that are routed to the sulphuric acid plant) from pyrometallurgical zinc production, BAT is to use a wet desulphurisation technique.","mg/Nm3","N/A",500,"Green","Continuous",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Zinc and Cadmium Production","Pyrometallurgical zinc production","Unspecified","Unspecified","Unspecified","Unspecified","Pyrometallurgical zinc production","Air","Sulphur Dioxide (24 Hour Mean)","In order to reduce SO2 emissions to air (other than those that are routed to the sulphuric acid plant) from pyrometallurgical zinc production, BAT is to use a wet desulphurisation technique.","mg/Nm3","N/A",500,"Green","Continuous",0,0,0,"Daily average",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Zinc and Cadmium Production","Hydrometallurgical zinc production","Unspecified","Unspecified","Unspecified","Unspecified","Leaching, purification and electrolysis, and to reduce arsane and stibane emissions from purification","Air","Sum of AsH3 and SbH3","In order to reduce zinc and sulphuric acid emissions to air from leaching, purification and electrolysis, and to reduce arsane and stibane emissions from purification, BAT is to use one or a combination of the techniques given below: (i) Wet scrubber; (ii) Demister; (iii) Centrifugal system","mg/Nm3","N/A",0.5,"Green","Once per year",0,0,0,"Average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Zinc and Cadmium Production","Hydrometallurgical zinc production","Unspecified","Unspecified","Unspecified","Unspecified","Leaching, purification and electrolysis, and to reduce arsane and stibane emissions from purification","Air","Sum of AsH3 and SbH3","In order to reduce zinc and sulphuric acid emissions to air from leaching, purification and electrolysis, and to reduce arsane and stibane emissions from purification, BAT is to use one or a combination of the techniques given below: (i) Wet scrubber; (ii) Demister; (iii) Centrifugal system","mg/Nm3","N/A",0.5,"Green","Once per year",0,0,0,"Average over the sampling period",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Alumina and Anode production","Anode production","Unspecified ","Unspecified","Unspecified","Unspecified","Baking plant with in an anode production plant with a primary aluminium smelter ","Air","Total fluorides","In order to reduce dust, sulphur dioxide, PAH and fluoride emissions to air from a baking plant in an anode production plant integrated with a primary aluminium smelter, BAT is to use one or a combination of the techniques given below: (i) Use of raw materials and fuels containing a\nlow amount of sulphur; (ii) Dry scrubber using alumina as the adsorbent\nagent followed by a bag filter; (iii) Wet scrubber; (iv) Regenerative thermal oxidiser in combination\nwith a dust abatement system","mg/Nm3","N/A",0.8,"Green","Once per year",0,0,0,"Average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Alumina and Anode production","Anode production","Unspecified ","Unspecified","Unspecified","Unspecified","Baking plant with in an anode production plant with a primary aluminium smelter ","Air","Total fluorides","In order to reduce dust, sulphur dioxide, PAH and fluoride emissions to air from a baking plant in an anode production plant integrated with a primary aluminium smelter, BAT is to use one or a combination of the techniques given below: (i) Use of raw materials and fuels containing a\nlow amount of sulphur; (ii) Dry scrubber using alumina as the adsorbent\nagent followed by a bag filter; (iii) Wet scrubber; (iv) Regenerative thermal oxidiser in combination\nwith a dust abatement system","mg/Nm3","N/A",0.8,"Green","Once per year",0,0,0,"Average over the sampling period",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Alumina and Anode production","Primary aluminium production","Unspecified","Existing","Unspecified","Unspecified","Electrolysis house (collected from the electrolytic cells and roof vents) ","Air","Total fluorides","In order to prevent or collect diffuse emissions from electrolytic cells in primary aluminium production using the Søderberg technology, BAT is to use a combination of the techniques given below: (i) Use of paste with a pitch content between 25 % and 28 % (dry paste); (ii) Upgrade the manifold design to allow closed point feeding operations and improved off-gas collection\nefficiency; (iii) Alumina point feeding\n\nIn order to prevent or collect diffuse emissions from electrolytic cells in primary aluminium\nproduction using prebaked anodes, BAT is to use a combination of the techniques given below: (i) Automatic multiple point feeding of alumina; (ii) Complete hood coverage of the cell and adequate off-gas extraction rates (to lead the off-gas to the\ntreatment in BAT 67) taking into account fluoride generation from bath and carbon anode\nconsumption; (iii) Boosted suction system connected to the abatement techniques listed in BAT 67; (iv) Minimisation of the time for changing anodes and other activities that require cell hoods to be\nremoved; (v) Efficient process control system avoiding process deviations that might otherwise lead to increased cell\nevolution and emissions; (vi) Use of a programmed system for cell operations and maintenance; (vii) Use of established efficient cleaning methods in the rodding plant to recover fluorides and carbonl (viii) Storage of removed anodes in a compartment near the cell, connected to the treatment in BAT 67, or\nstorage of the butts in confined boxes\n\nIn order to reduce dust, metal and fluoride emissions to air from electrolytic cells, BAT is to use\none of the techniques given below: (i) Dry scrubber using alumina as the adsorbent agent\nfollowed by a bag filter; (ii) Dry scrubber using alumina as the adsorbent agent\nfollowed by a bag filter and a wet scrubber\n\n","kg/t Al","N/A",0.6,"Green","Continuous or\nonce per year",0,0,0,"As mass of pollutant emitted during a year from the electrolysis house divided by the mass of liquid aluminium produced in the same year.","\n\n These BAT-AELs are not applicable to plants that due to their configuration cannot measure roof emissions.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Alumina and Anode production","Primary aluminium production","Unspecified","Existing","Unspecified","Unspecified","Electrolysis house (collected from the electrolytic cells and roof vents) ","Air","Total fluorides","In order to prevent or collect diffuse emissions from electrolytic cells in primary aluminium production using the Søderberg technology, BAT is to use a combination of the techniques given below: (i) Use of paste with a pitch content between 25 % and 28 % (dry paste); (ii) Upgrade the manifold design to allow closed point feeding operations and improved off-gas collection\nefficiency; (iii) Alumina point feeding\n\nIn order to prevent or collect diffuse emissions from electrolytic cells in primary aluminium\nproduction using prebaked anodes, BAT is to use a combination of the techniques given below: (i) Automatic multiple point feeding of alumina; (ii) Complete hood coverage of the cell and adequate off-gas extraction rates (to lead the off-gas to the\ntreatment in BAT 67) taking into account fluoride generation from bath and carbon anode\nconsumption; (iii) Boosted suction system connected to the abatement techniques listed in BAT 67; (iv) Minimisation of the time for changing anodes and other activities that require cell hoods to be\nremoved; (v) Efficient process control system avoiding process deviations that might otherwise lead to increased cell\nevolution and emissions; (vi) Use of a programmed system for cell operations and maintenance; (vii) Use of established efficient cleaning methods in the rodding plant to recover fluorides and carbonl (viii) Storage of removed anodes in a compartment near the cell, connected to the treatment in BAT 67, or\nstorage of the butts in confined boxes\n\nIn order to reduce dust, metal and fluoride emissions to air from electrolytic cells, BAT is to use\none of the techniques given below: (i) Dry scrubber using alumina as the adsorbent agent\nfollowed by a bag filter; (ii) Dry scrubber using alumina as the adsorbent agent\nfollowed by a bag filter and a wet scrubber\n\n","kg/t Al","N/A",0.6,"Green","Continuous or\nonce per year",0,0,0,"As mass of pollutant emitted during a year from the electrolysis house divided by the mass of liquid aluminium produced in the same year.","\n\n These BAT-AELs are not applicable to plants that due to their configuration cannot measure roof emissions."]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Alumina and Anode production","Primary aluminium production","Unspecified","New","Unspecified","Unspecified","Electrolysis house (collected from the electrolytic cells and roof vents) ","Air","Total fluorides","In order to prevent or collect diffuse emissions from electrolytic cells in primary aluminium production using the Søderberg technology, BAT is to use a combination of the techniques given below: (i) Use of paste with a pitch content between 25 % and 28 % (dry paste); (ii) Upgrade the manifold design to allow closed point feeding operations and improved off-gas collection\nefficiency; (iii) Alumina point feeding\n\nIn order to prevent or collect diffuse emissions from electrolytic cells in primary aluminium\nproduction using prebaked anodes, BAT is to use a combination of the techniques given below: (i) Automatic multiple point feeding of alumina; (ii) Complete hood coverage of the cell and adequate off-gas extraction rates (to lead the off-gas to the\ntreatment in BAT 67) taking into account fluoride generation from bath and carbon anode\nconsumption; (iii) Boosted suction system connected to the abatement techniques listed in BAT 67; (iv) Minimisation of the time for changing anodes and other activities that require cell hoods to be\nremoved; (v) Efficient process control system avoiding process deviations that might otherwise lead to increased cell\nevolution and emissions; (vi) Use of a programmed system for cell operations and maintenance; (vii) Use of established efficient cleaning methods in the rodding plant to recover fluorides and carbonl (viii) Storage of removed anodes in a compartment near the cell, connected to the treatment in BAT 67, or\nstorage of the butts in confined boxes\n\nIn order to reduce dust, metal and fluoride emissions to air from electrolytic cells, BAT is to use\none of the techniques given below: (i) Dry scrubber using alumina as the adsorbent agent\nfollowed by a bag filter; (ii) Dry scrubber using alumina as the adsorbent agent\nfollowed by a bag filter and a wet scrubber\n\n","kg/t Al","N/A",0.35,"Green","Continuous or\nonce per year",0,0,0,"As mass of pollutant emitted during a year from the electrolysis house divided by the mass of liquid aluminium produced in the same year.",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Alumina and Anode production","Primary aluminium production","Unspecified","New","Unspecified","Unspecified","Electrolysis house (collected from the electrolytic cells and roof vents) ","Air","Total fluorides","In order to prevent or collect diffuse emissions from electrolytic cells in primary aluminium production using the Søderberg technology, BAT is to use a combination of the techniques given below: (i) Use of paste with a pitch content between 25 % and 28 % (dry paste); (ii) Upgrade the manifold design to allow closed point feeding operations and improved off-gas collection\nefficiency; (iii) Alumina point feeding\n\nIn order to prevent or collect diffuse emissions from electrolytic cells in primary aluminium\nproduction using prebaked anodes, BAT is to use a combination of the techniques given below: (i) Automatic multiple point feeding of alumina; (ii) Complete hood coverage of the cell and adequate off-gas extraction rates (to lead the off-gas to the\ntreatment in BAT 67) taking into account fluoride generation from bath and carbon anode\nconsumption; (iii) Boosted suction system connected to the abatement techniques listed in BAT 67; (iv) Minimisation of the time for changing anodes and other activities that require cell hoods to be\nremoved; (v) Efficient process control system avoiding process deviations that might otherwise lead to increased cell\nevolution and emissions; (vi) Use of a programmed system for cell operations and maintenance; (vii) Use of established efficient cleaning methods in the rodding plant to recover fluorides and carbonl (viii) Storage of removed anodes in a compartment near the cell, connected to the treatment in BAT 67, or\nstorage of the butts in confined boxes\n\nIn order to reduce dust, metal and fluoride emissions to air from electrolytic cells, BAT is to use\none of the techniques given below: (i) Dry scrubber using alumina as the adsorbent agent\nfollowed by a bag filter; (ii) Dry scrubber using alumina as the adsorbent agent\nfollowed by a bag filter and a wet scrubber\n\n","kg/t Al","N/A",0.35,"Green","Continuous or\nonce per year",0,0,0,"As mass of pollutant emitted during a year from the electrolysis house divided by the mass of liquid aluminium produced in the same year.",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Alumina and Anode production","Primary aluminium production","Unspecified","Unspecified","Unspecified","Unspecified","Electrolytic cells","Air","Total fluorides","In order to reduce dust, metal and fluoride emissions to air from electrolytic cells, BAT is to use one of the techniques given below: (i) Dry scrubber using alumina as the adsorbent agent\nfollowed by a bag filter; (ii) Dry scrubber using alumina as the adsorbent agent\nfollowed by a bag filter and a wet scrubber","mg/Nm3","N/A",1.5,"Green","Continuous or\nonce per year",0,0,0,"Average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Alumina and Anode production","Primary aluminium production","Unspecified","Unspecified","Unspecified","Unspecified","Electrolytic cells","Air","Total fluorides","In order to reduce dust, metal and fluoride emissions to air from electrolytic cells, BAT is to use one of the techniques given below: (i) Dry scrubber using alumina as the adsorbent agent\nfollowed by a bag filter; (ii) Dry scrubber using alumina as the adsorbent agent\nfollowed by a bag filter and a wet scrubber","mg/Nm3","N/A",1.5,"Green","Continuous or\nonce per year",0,0,0,"Average over the sampling period",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Alumina and Anode production","Secondary aluminium production ","Unspecified","Unspecified","Unspecified","Unspecified","Thermal treatment of contaminated secondary raw materials (e.g. swarf) and from the melting furnace","Air","VOC","In order to reduce emissions to air of organic compounds and PCDD/F from the thermal treatment of contaminated secondary raw materials (e.g. swarf) and from the melting furnace, BAT is to use a bag filter in combination with at least one of the techniques given below: (i) Select and feed the raw materials according to the furnace and the abatement techniques used; (ii) Internal burner system for melting furnaces; (iii) Afterburner; (iv) Rapid quenching; (v) Activated carbon injection","mg/Nm3",10,30,"Green","Continuous or\nonce per year",0,0,0,"Daily average or average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Alumina and Anode production","Secondary aluminium production ","Unspecified","Unspecified","Unspecified","Unspecified","Thermal treatment of contaminated secondary raw materials (e.g. swarf) and from the melting furnace","Air","VOC","In order to reduce emissions to air of organic compounds and PCDD/F from the thermal treatment of contaminated secondary raw materials (e.g. swarf) and from the melting furnace, BAT is to use a bag filter in combination with at least one of the techniques given below: (i) Select and feed the raw materials according to the furnace and the abatement techniques used; (ii) Internal burner system for melting furnaces; (iii) Afterburner; (iv) Rapid quenching; (v) Activated carbon injection","mg/Nm3",10,30,"Green","Continuous or\nonce per year",0,0,0,"Daily average or average over the sampling period",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Carbon and Graphite Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Impregnation stage where special impregnation agents such as resins and biodegradable solvents are used","Air","VOC","In order to reduce emissions of organic compounds to air, including phenol and the formaldehyde from the impregnation stage where special impregnation agents such as resins and biodegradable solvents are used, BAT is to use one of the techniques given below: (i) Regenerative thermal oxidiser in combination with an ESP for the mixing, baking and impregnation\nstages; (ii) Biofilter and/or bioscrubber for the impregnation stage where special impregnation agents such as\nresins and biodegradable solvents are used","mg/Nm3",10,40,"Green","Once per year",0,0,0,"Average over the sampling period","The lower end of the range is associated with the use of an ESP in combination with a regenerative thermal oxidiser. The upper end of the range is associated with the use of a biofilter and/or a bioscrubber.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Carbon and Graphite Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Impregnation stage where special impregnation agents such as resins and biodegradable solvents are used","Air","VOC","In order to reduce emissions of organic compounds to air, including phenol and the formaldehyde from the impregnation stage where special impregnation agents such as resins and biodegradable solvents are used, BAT is to use one of the techniques given below: (i) Regenerative thermal oxidiser in combination with an ESP for the mixing, baking and impregnation\nstages; (ii) Biofilter and/or bioscrubber for the impregnation stage where special impregnation agents such as\nresins and biodegradable solvents are used","mg/Nm3",10,40,"Green","Once per year",0,0,0,"Average over the sampling period","The lower end of the range is associated with the use of an ESP in combination with a regenerative thermal oxidiser. The upper end of the range is associated with the use of a biofilter and/or a bioscrubber."]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Copper production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Pyrolytic treatment of copper turnings, and the drying, smelting and melting of secondary raw materials","Air","VOC","In  order  to  reduce  organic  compound  emissions  to  air  from  the  pyrolytic  treatment  of  copper  \nturnings,   and   the   drying,   smelting   and   melting   of   secondary   raw   materials,   BAT   is   to   use   one   of   the   \ntechniques  given  below: (i) Afterburner or post-combustion chamber or\nregenerative thermal oxidiser; (ii) Injection of adsorbent in combination with a bag\nfilter; (iii) Design of furnace and the abatement techniques\naccording to the raw materials available; (iv) Select and feed the raw materials according to the\nfurnace and the abatement techniques used; (v) Thermal destruction of TVOC at high\ntemperatures in the furnace","mg/Nm3",3,30,"Green","Continuous or\nonce per year",0,0,0,"Daily average or average over sampling period","The lower end of the range is associated with the use of a regenerative thermal oxidiser.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Copper production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Pyrolytic treatment of copper turnings, and the drying, smelting and melting of secondary raw materials","Air","VOC","In  order  to  reduce  organic  compound  emissions  to  air  from  the  pyrolytic  treatment  of  copper  \nturnings,   and   the   drying,   smelting   and   melting   of   secondary   raw   materials,   BAT   is   to   use   one   of   the   \ntechniques  given  below: (i) Afterburner or post-combustion chamber or\nregenerative thermal oxidiser; (ii) Injection of adsorbent in combination with a bag\nfilter; (iii) Design of furnace and the abatement techniques\naccording to the raw materials available; (iv) Select and feed the raw materials according to the\nfurnace and the abatement techniques used; (v) Thermal destruction of TVOC at high\ntemperatures in the furnace","mg/Nm3",3,30,"Green","Continuous or\nonce per year",0,0,0,"Daily average or average over sampling period","The lower end of the range is associated with the use of a regenerative thermal oxidiser."]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Lead and Tin Production","Secondary ","Unspecified","Unspecified","Unspecified","Unspecified","Raw material drying and smelting process","Air","VOC","In order to reduce emissions of organic compounds to air from the raw material drying and smelting process in secondary lead and/or tin production, BAT is to use one or a combination of the techniques given below: (i) Select and feed the raw materials according to the\nfurnace and the abatement techniques used; (ii) Optimise combustion conditions to reduce the\nemissions of organic compounds; (iii) Afterburner or regenerative thermal oxidiser ","mg/Nm3",10,40,"Green","Continuous or\nonce per year",0,0,0,"Daily average or  average over the sampling period ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Lead and Tin Production","Secondary ","Unspecified","Unspecified","Unspecified","Unspecified","Raw material drying and smelting process","Air","VOC","In order to reduce emissions of organic compounds to air from the raw material drying and smelting process in secondary lead and/or tin production, BAT is to use one or a combination of the techniques given below: (i) Select and feed the raw materials according to the\nfurnace and the abatement techniques used; (ii) Optimise combustion conditions to reduce the\nemissions of organic compounds; (iii) Afterburner or regenerative thermal oxidiser ","mg/Nm3",10,40,"Green","Continuous or\nonce per year",0,0,0,"Daily average or  average over the sampling period ",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Zinc and Cadmium Production","Secondary ","Unspecified","Unspecified","Unspecified","Unspecified","Melting of metallic and mixed metallic/oxidic streams, and from the slag fuming furnace and the Waelz kiln","Air","VOC","In order to reduce emissions of organic compounds to air from the melting of metallic and\nmixed metallic/oxidic streams, and from the slag fuming furnace and the Waelz kiln, BAT is to use one or a\ncombination of the techniques given below: (i) Injection of adsorbent (activated carbon or lignite coke)\nfollowed by a bag filter and/or ESP\n (ii) Thermal oxidiser; (iii) Regenerative thermal oxidiser ","mg/Nm3",2,20,"Green","Continuous or once per year",0,0,0,"Daily average or average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Zinc and Cadmium Production","Secondary ","Unspecified","Unspecified","Unspecified","Unspecified","Melting of metallic and mixed metallic/oxidic streams, and from the slag fuming furnace and the Waelz kiln","Air","VOC","In order to reduce emissions of organic compounds to air from the melting of metallic and\nmixed metallic/oxidic streams, and from the slag fuming furnace and the Waelz kiln, BAT is to use one or a\ncombination of the techniques given below: (i) Injection of adsorbent (activated carbon or lignite coke)\nfollowed by a bag filter and/or ESP\n (ii) Thermal oxidiser; (iii) Regenerative thermal oxidiser ","mg/Nm3",2,20,"Green","Continuous or once per year",0,0,0,"Daily average or average over the sampling period",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Zinc and Cadmium Production","Hydrometallurgical zinc production","Unspecified","Unspecified","Unspecified","Unspecified","Leaching, purification and electrolysis, and to reduce arsane and stibane emissions from purification","Air","Zinc","In order to reduce zinc and sulphuric acid emissions to air from leaching, purification and electrolysis, and to reduce arsane and stibane emissions from purification, BAT is to use one or a combination of the techniques given below: (i) Wet scrubber; (ii) Demister; (iii) Centrifugal system","mg/Nm3","N/A",1,"Green","Once per year",0,0,0,"Average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Zinc and Cadmium Production","Hydrometallurgical zinc production","Unspecified","Unspecified","Unspecified","Unspecified","Leaching, purification and electrolysis, and to reduce arsane and stibane emissions from purification","Air","Zinc","In order to reduce zinc and sulphuric acid emissions to air from leaching, purification and electrolysis, and to reduce arsane and stibane emissions from purification, BAT is to use one or a combination of the techniques given below: (i) Wet scrubber; (ii) Demister; (iii) Centrifugal system","mg/Nm3","N/A",1,"Green","Once per year",0,0,0,"Average over the sampling period",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Copper","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.1,"Green","Once per month",0,0,0,"Daily average","In the case of a high arsenic content in the total input of the plant, the BAT-AEL may be up to 0,2 mg/l.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Copper","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.1,"Green","Once per month",0,0,0,"Daily average","In the case of a high arsenic content in the total input of the plant, the BAT-AEL may be up to 0,2 mg/l."]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Ferro alloys Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.1,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Ferro alloys Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.1,"Green","Once per month",0,0,0,"Daily average",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Lead and Tin Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.1,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Lead and Tin Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.1,"Green","Once per month",0,0,0,"Daily average",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Nickel and Cobalt Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.3,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Nickel and Cobalt Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.3,"Green","Once per month",0,0,0,"Daily average",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Precious metals","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.1,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Precious metals","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.1,"Green","Once per month",0,0,0,"Daily average",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Zinc and Cadmium Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.1,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Zinc and Cadmium Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.1,"Green","Once per month",0,0,0,"Daily average",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Copper","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l",0.02,0.1,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Copper","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l",0.02,0.1,"Green","Once per month",0,0,0,"Daily average",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Ferro alloys Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.05,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Ferro alloys Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.05,"Green","Once per month",0,0,0,"Daily average",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Lead and Tin Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.1,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Lead and Tin Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.1,"Green","Once per month",0,0,0,"Daily average",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Nickel and Cobalt Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.1,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Nickel and Cobalt Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.1,"Green","Once per month",0,0,0,"Daily average",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Precious metals","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.05,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Precious metals","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.05,"Green","Once per month",0,0,0,"Daily average",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Zinc and Cadmium Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.1,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Zinc and Cadmium Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.1,"Green","Once per month",0,0,0,"Daily average",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Ferro alloys Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.2,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Ferro alloys Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.2,"Green","Once per month",0,0,0,"Daily average",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Ferro alloys Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.05,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Ferro alloys Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.05,"Green","Once per month",0,0,0,"Daily average",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Lead and Tin Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.1,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Lead and Tin Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.1,"Green","Once per month",0,0,0,"Daily average",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Nickel and Cobalt Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l",0.1,0.5,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Nickel and Cobalt Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l",0.1,0.5,"Green","Once per month",0,0,0,"Daily average",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Copper","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l",0.05,0.5,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Copper","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l",0.05,0.5,"Green","Once per month",0,0,0,"Daily average",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Ferro alloys Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.5,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Ferro alloys Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.5,"Green","Once per month",0,0,0,"Daily average",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Lead and Tin Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.2,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Lead and Tin Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.2,"Green","Once per month",0,0,0,"Daily average",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Nickel and Cobalt Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.5,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Nickel and Cobalt Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.5,"Green","Once per month",0,0,0,"Daily average",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Precious metals","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.3,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Precious metals","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.3,"Green","Once per month",0,0,0,"Daily average",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Zinc and Cadmium Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.1,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Zinc and Cadmium Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.1,"Green","Once per month",0,0,0,"Daily average",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Copper","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.5,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Copper","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.5,"Green","Once per month",0,0,0,"Daily average",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Ferro alloys Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.2,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Ferro alloys Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.2,"Green","Once per month",0,0,0,"Daily average",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Lead and Tin Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.5,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Lead and Tin Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.5,"Green","Once per month",0,0,0,"Daily average",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Nickel and Cobalt Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.5,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Nickel and Cobalt Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.5,"Green","Once per month",0,0,0,"Daily average",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Precious metals","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.5,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Precious metals","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.5,"Green","Once per month",0,0,0,"Daily average",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Zinc and Cadmium Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.2,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Zinc and Cadmium Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.2,"Green","Once per month",0,0,0,"Daily average",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Copper","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l",5.0000000000000001E-3,0.02,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Copper","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l",5.0000000000000001E-3,0.02,"Green","Once per month",0,0,0,"Daily average",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Ferro alloys Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.05,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Ferro alloys Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.05,"Green","Once per month",0,0,0,"Daily average",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Lead and Tin Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.05,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Lead and Tin Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.05,"Green","Once per month",0,0,0,"Daily average",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Nickel and Cobalt Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.05,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Nickel and Cobalt Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.05,"Green","Once per month",0,0,0,"Daily average",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Precious metals","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.05,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Precious metals","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.05,"Green","Once per month",0,0,0,"Daily average",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Zinc and Cadmium Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.05,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Zinc and Cadmium Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.05,"Green","Once per month",0,0,0,"Daily average",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Copper","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.5,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Copper","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.5,"Green","Once per month",0,0,0,"Daily average",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Ferro alloys Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",2,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Ferro alloys Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",2,"Green","Once per month",0,0,0,"Daily average",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Lead and Tin Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.5,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Lead and Tin Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.5,"Green","Once per month",0,0,0,"Daily average",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Nickel and Cobalt Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",2,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Nickel and Cobalt Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",2,"Green","Once per month",0,0,0,"Daily average",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Precious metals","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.5,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Precious metals","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.5,"Green","Once per month",0,0,0,"Daily average",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Zinc and Cadmium Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.1,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Zinc and Cadmium Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.1,"Green","Once per month",0,0,0,"Daily average",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Precious metals","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.6,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Precious metals","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.6,"Green","Once per month",0,0,0,"Daily average",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Copper","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",1,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Copper","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",1,"Green","Once per month",0,0,0,"Daily average",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Ferro alloys Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",1,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Ferro alloys Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",1,"Green","Once per month",0,0,0,"Daily average",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Lead and Tin Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",1,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Lead and Tin Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",1,"Green","Once per month",0,0,0,"Daily average",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Nickel and Cobalt Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",1,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Nickel and Cobalt Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",1,"Green","Once per month",0,0,0,"Daily average",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Precious metals","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.4,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Precious metals","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.4,"Green","Once per month",0,0,0,"Daily average",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Zinc and Cadmium Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",1,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Zinc and Cadmium Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",1,"Green","Once per month",0,0,0,"Daily average",0]
["Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Lime kilns","Air","Particulates (PM10) (Annual Mean)","Existing","mg/Nm3",10,30,"Green","Continuous",0,0,0.06,"Yearly","For an existing lime kiln equipped with an ESP approaching the end of its operational life, emission levels may increase over time up to 50 mg/Nm3 (corresponding to 0,05 kg/ADt).",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Lime kilns","Air","Particulates (PM10) (Annual Mean)","Existing","mg/Nm3",10,30,"Green","Continuous",0,0,0.06,"Yearly","For an existing lime kiln equipped with an ESP approaching the end of its operational life, emission levels may increase over time up to 50 mg/Nm3 (corresponding to 0,05 kg/ADt)."]
["Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Lime kilns","Air","Particulates (PM10) (Annual Mean)","Existing","kg dust/ADt",5.0000000000000001E-3,0.03,"Green","Continuous",0,0,"Unspecified","Yearly","For an existing lime kiln equipped with an ESP approaching the end of its operational life, emission levels may increase over time up to 50 mg/Nm3 (corresponding to 0,05 kg/ADt).",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Lime kilns","Air","Particulates (PM10) (Annual Mean)","Existing","kg dust/ADt",5.0000000000000001E-3,0.03,"Green","Continuous",0,0,"Unspecified","Yearly","For an existing lime kiln equipped with an ESP approaching the end of its operational life, emission levels may increase over time up to 50 mg/Nm3 (corresponding to 0,05 kg/ADt)."]
["Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Lime kilns","Air","Particulates (PM10) (Annual Mean)","New or major refurbishment","mg/Nm3",10,25,"Green","Continuous",0,0,0.06,"Yearly",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Lime kilns","Air","Particulates (PM10) (Annual Mean)","New or major refurbishment","mg/Nm3",10,25,"Green","Continuous",0,0,0.06,"Yearly",0]
["Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Lime kilns","Air","Particulates (PM10) (Annual Mean)","New or major refurbishment","kg dust/ADt",5.0000000000000001E-3,0.02,"Green","Continuous",0,0,"Unspecified","Yearly",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Lime kilns","Air","Particulates (PM10) (Annual Mean)","New or major refurbishment","kg dust/ADt",5.0000000000000001E-3,0.02,"Green","Continuous",0,0,"Unspecified","Yearly",0]
["Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Recovery boiler","Air","Particulates (PM10) (Annual Mean)","Existing","mg/Nm3",10,40,"Green","Continuous",0,0,0.06,"Yearly","For an existing recovery boiler equipped with an ESP approaching the end of its operational life, emission levels may increase over time up to 50 mg/Nm3 (corresponding to 0,4 kg/ADt).",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Recovery boiler","Air","Particulates (PM10) (Annual Mean)","Existing","mg/Nm3",10,40,"Green","Continuous",0,0,0.06,"Yearly","For an existing recovery boiler equipped with an ESP approaching the end of its operational life, emission levels may increase over time up to 50 mg/Nm3 (corresponding to 0,4 kg/ADt)."]
["Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Recovery boiler","Air","Particulates (PM10) (Annual Mean)","Existing","kg dust/ADt",0.02,0.3,"Green","Continuous",0,0,"Unspecified","Yearly","For an existing recovery boiler equipped with an ESP approaching the end of its operational life, emission levels may increase over time up to 50 mg/Nm3 (corresponding to 0,4 kg/ADt).",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Recovery boiler","Air","Particulates (PM10) (Annual Mean)","Existing","kg dust/ADt",0.02,0.3,"Green","Continuous",0,0,"Unspecified","Yearly","For an existing recovery boiler equipped with an ESP approaching the end of its operational life, emission levels may increase over time up to 50 mg/Nm3 (corresponding to 0,4 kg/ADt)."]
["Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Recovery boiler","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and SO2 emissions from a recovery boiler, BAT is to use one of the techniques given below and to limit ‘acid operation’ of the scrubbers to the minimum required to ensure their proper functioning: (i) ESP or multicyclones with multistage venturi scrubbers; (ii) ESP or multicyclones with multistage double inlet downstream scrubbers","mg/Nm3",5,20,"Green","Periodic ",0,0," ","Average over the sampling period","For recovery boilers operated in mills using more than 25 % of hardwood (potassium-rich) in raw materials, higher dust emissions up to 30 mg/Nm3 may occur.\n\nThe BAT-AEL for dust does not apply for ammonium-based mills.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Recovery boiler","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and SO2 emissions from a recovery boiler, BAT is to use one of the techniques given below and to limit ‘acid operation’ of the scrubbers to the minimum required to ensure their proper functioning: (i) ESP or multicyclones with multistage venturi scrubbers; (ii) ESP or multicyclones with multistage double inlet downstream scrubbers","mg/Nm3",5,20,"Green","Periodic ",0,0," ","Average over the sampling period","For recovery boilers operated in mills using more than 25 % of hardwood (potassium-rich) in raw materials, higher dust emissions up to 30 mg/Nm3 may occur.\n\nThe BAT-AEL for dust does not apply for ammonium-based mills."]
["Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Recovery boiler","Air","Particulates (PM10) (Annual Mean)","New or major refurbishment","mg/Nm3",10,25,"Green","Continuous",0,0,0.06,"Yearly",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Recovery boiler","Air","Particulates (PM10) (Annual Mean)","New or major refurbishment","mg/Nm3",10,25,"Green","Continuous",0,0,0.06,"Yearly",0]
["Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Recovery boiler","Air","Particulates (PM10) (Annual Mean)","New or major refurbishment","kg dust/ADt",0.02,0.2,"Green","Continuous",0,0,"Unspecified","Yearly",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Recovery boiler","Air","Particulates (PM10) (Annual Mean)","New or major refurbishment","kg dust/ADt",0.02,0.2,"Green","Continuous",0,0,"Unspecified","Yearly",0]
["Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Recovery boiler","Air","Gaseous S (TRS- S + SO2-S) DS 75- 83%","In order to reduce SO2 and TRS emissions from a recovery boiler, BAT is to use a combination of the techniques given below: (i) Increasing the dry solids (DS) content of black liquor; (ii) Optimised firing; (iii) Wet scrubber","kg S/ADt",0.03,0.13,"Green","Continuous",0,0,"Unspecified","Yearly","Increasing the DS content of the black liquor results in lower SO2 emissions and higher NOx emissions. Due to this, a recovery boiler with low emission levels for SO2, may be on the higher end of the range for NOx and vice versa. \n\nIf a recovery boiler were to burn black liquor with a DS > 83 %, then SO2 and gaseous S emission levels should be reconsidered on a case-by-case basis.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Recovery boiler","Air","Gaseous S (TRS- S + SO2-S) DS 75- 83%","In order to reduce SO2 and TRS emissions from a recovery boiler, BAT is to use a combination of the techniques given below: (i) Increasing the dry solids (DS) content of black liquor; (ii) Optimised firing; (iii) Wet scrubber","kg S/ADt",0.03,0.13,"Green","Continuous",0,0,"Unspecified","Yearly","Increasing the DS content of the black liquor results in lower SO2 emissions and higher NOx emissions. Due to this, a recovery boiler with low emission levels for SO2, may be on the higher end of the range for NOx and vice versa. \n\nIf a recovery boiler were to burn black liquor with a DS > 83 %, then SO2 and gaseous S emission levels should be reconsidered on a case-by-case basis."]
["Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Recovery boiler","Air","Gaseous S (TRS- S + SO2-S) DS< 75%","In order to reduce SO2 and TRS emissions from a recovery boiler, BAT is to use a combination of the techniques given below: (i) Increasing the dry solids (DS) content of black liquor; (ii) Optimised firing; (iii) Wet scrubber","kg S/ADt",0.03,0.17,"Green","Continuous",0,0,"Unspecified","Yearly","Increasing the DS content of the black liquor results in lower SO2 emissions and higher NOx emissions. Due to this, a recovery boiler with low emission levels for SO2, may be on the higher end of the range for NOx and vice versa. ",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Recovery boiler","Air","Gaseous S (TRS- S + SO2-S) DS< 75%","In order to reduce SO2 and TRS emissions from a recovery boiler, BAT is to use a combination of the techniques given below: (i) Increasing the dry solids (DS) content of black liquor; (ii) Optimised firing; (iii) Wet scrubber","kg S/ADt",0.03,0.17,"Green","Continuous",0,0,"Unspecified","Yearly","Increasing the DS content of the black liquor results in lower SO2 emissions and higher NOx emissions. Due to this, a recovery boiler with low emission levels for SO2, may be on the higher end of the range for NOx and vice versa. "]
["Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","TRS burner for strong odorous gases ","Air","Gaseous S (TRS-S + SO2-S)","In order to reduce SO2 emissions from the incineration of strong odorous gases in a dedicated TRS burner, BAT is to use an alkaline SO2 scrubber.","kg S/Adt",2E-3,0.05,"Green","Continuous",0,0,"Unspecified","Yearly","This BAT-AEL is based on a gas flow in the range of 100-200 Nm3/ADt.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","TRS burner for strong odorous gases ","Air","Gaseous S (TRS-S + SO2-S)","In order to reduce SO2 emissions from the incineration of strong odorous gases in a dedicated TRS burner, BAT is to use an alkaline SO2 scrubber.","kg S/Adt",2E-3,0.05,"Green","Continuous",0,0,"Unspecified","Yearly","This BAT-AEL is based on a gas flow in the range of 100-200 Nm3/ADt."]
["Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Lime kilns","Air","Gaseous S (TRS-S + SO2-S) when strong gases are burnt in the lime kiln","In order to reduce SO2 emissions from a lime kiln, BAT is to apply one or a combination of the techniques given below: (i) Fuel selection/low sulphur fuel; (ii) Limit incineration of sulphur-containing odorous strong gases in the lime kiln; (iii) Control of Na2S content in lime mud feed; (iv) Alkaline scrubber\n","kg S/ADt",5.5E-2,0.12,"Green","Continuous",0,0,"Unspecified","Yearly","‘strong gases’ includes methanol and turpentine",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Lime kilns","Air","Gaseous S (TRS-S + SO2-S) when strong gases are burnt in the lime kiln","In order to reduce SO2 emissions from a lime kiln, BAT is to apply one or a combination of the techniques given below: (i) Fuel selection/low sulphur fuel; (ii) Limit incineration of sulphur-containing odorous strong gases in the lime kiln; (iii) Control of Na2S content in lime mud feed; (iv) Alkaline scrubber\n","kg S/ADt",5.5E-2,0.12,"Green","Continuous",0,0,"Unspecified","Yearly","‘strong gases’ includes methanol and turpentine"]
["Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Lime kilns","Air","Gaseous S (TRS-S + SO2-S) when strong gases are not burnt in the lime kiln","In order to reduce SO2 emissions from a lime kiln, BAT is to apply one or a combination of the techniques given below: (i) Fuel selection/low sulphur fuel; (ii) Limit incineration of sulphur-containing odorous strong gases in the lime kiln; (iii) Control of Na2S content in lime mud feed; (iv) Alkaline scrubber\n","kg S/ADt",5.0000000000000001E-3,7.0000000000000007E-2,"Green","Continuous",0,0,"Unspecified","Yearly","‘strong gases’ includes methanol and turpentine",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Lime kilns","Air","Gaseous S (TRS-S + SO2-S) when strong gases are not burnt in the lime kiln","In order to reduce SO2 emissions from a lime kiln, BAT is to apply one or a combination of the techniques given below: (i) Fuel selection/low sulphur fuel; (ii) Limit incineration of sulphur-containing odorous strong gases in the lime kiln; (iii) Control of Na2S content in lime mud feed; (iv) Alkaline scrubber\n","kg S/ADt",5.0000000000000001E-3,7.0000000000000007E-2,"Green","Continuous",0,0,"Unspecified","Yearly","‘strong gases’ includes methanol and turpentine"]
["Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Recovery boiler","Air","NH3 (ammonia slip from SNCR)","In order to reduce NOx emissions from a recovery boiler, BAT is to use an optimised firing system including one or a combination of the techniques given below: (i) Optimising the recovery boiler by controlling the firing conditions; (ii) Staged injection of spent liquor; (iii) Selective non-catalytic reduction (SNCR)","mg/Nm3","N/A",5,"Green","Periodic ",0,0,0.05,"Yearly",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Recovery boiler","Air","NH3 (ammonia slip from SNCR)","In order to reduce NOx emissions from a recovery boiler, BAT is to use an optimised firing system including one or a combination of the techniques given below: (i) Optimising the recovery boiler by controlling the firing conditions; (ii) Staged injection of spent liquor; (iii) Selective non-catalytic reduction (SNCR)","mg/Nm3","N/A",5,"Green","Periodic ",0,0,0.05,"Yearly",0]
["Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Gaseous fuels ","Lime kilns","Air","Nitrogen dioxide","In order to reduce NOx emissions from a lime kiln, BAT is to apply a combination of the techniques given below: (i) Optimised combustion and combustion control; (ii) Good mixing of fuel and air; (iii) Low-NOx burner; (iv) Fuel selection/low-N fuel","mg /nm3",100,350,"Green","Continuous",0,0,0.06,"Yearly","When using gaseous fuels originating from vegetable matter (e.g. non-condensable gases), including those obtained as by-products of the pulping process, emission levels up to 450 mg/Nm3 (corresponding to 0,45 kg NOx/ADt) may occur.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Gaseous fuels ","Lime kilns","Air","Nitrogen dioxide","In order to reduce NOx emissions from a lime kiln, BAT is to apply a combination of the techniques given below: (i) Optimised combustion and combustion control; (ii) Good mixing of fuel and air; (iii) Low-NOx burner; (iv) Fuel selection/low-N fuel","mg /nm3",100,350,"Green","Continuous",0,0,0.06,"Yearly","When using gaseous fuels originating from vegetable matter (e.g. non-condensable gases), including those obtained as by-products of the pulping process, emission levels up to 450 mg/Nm3 (corresponding to 0,45 kg NOx/ADt) may occur."]
["Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Gaseous fuels ","Lime kilns","Air","Nitrogen dioxide","In order to reduce NOx emissions from a lime kiln, BAT is to apply a combination of the techniques given below: (i) Optimised combustion and combustion control; (ii) Good mixing of fuel and air; (iii) Low-NOx burner; (iv) Fuel selection/low-N fuel","kg NOx/Adt",0.1,0.3,"Green","Continuous",0,0,"Unspecified","Yearly","When using gaseous fuels originating from vegetable matter (e.g. non-condensable gases), including those obtained as by-products of the pulping process, emission levels up to 450 mg/Nm3 (corresponding to 0,45 kg NOx/ADt) may occur.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Gaseous fuels ","Lime kilns","Air","Nitrogen dioxide","In order to reduce NOx emissions from a lime kiln, BAT is to apply a combination of the techniques given below: (i) Optimised combustion and combustion control; (ii) Good mixing of fuel and air; (iii) Low-NOx burner; (iv) Fuel selection/low-N fuel","kg NOx/Adt",0.1,0.3,"Green","Continuous",0,0,"Unspecified","Yearly","When using gaseous fuels originating from vegetable matter (e.g. non-condensable gases), including those obtained as by-products of the pulping process, emission levels up to 450 mg/Nm3 (corresponding to 0,45 kg NOx/ADt) may occur."]
["Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Liquid fuels","Lime kilns","Air","Nitrogen dioxide","In order to reduce NOx emissions from a lime kiln, BAT is to apply a combination of the techniques given below: (i) Optimised combustion and combustion control; (ii) Good mixing of fuel and air; (iii) Low-NOx burner; (iv) Fuel selection/low-N fuel","mg /nm3",100,200,"Green","Continuous",0,0,0.06,"Yearly","When using liquid fuels originating from vegetable matter (e.g. turpentine, methanol, tall-oil), including those obtained as by-products of the pulping process, emission levels up to 350 mg/Nm3 (corresponding to 0,35 kg NOx/ADt) may occur.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Liquid fuels","Lime kilns","Air","Nitrogen dioxide","In order to reduce NOx emissions from a lime kiln, BAT is to apply a combination of the techniques given below: (i) Optimised combustion and combustion control; (ii) Good mixing of fuel and air; (iii) Low-NOx burner; (iv) Fuel selection/low-N fuel","mg /nm3",100,200,"Green","Continuous",0,0,0.06,"Yearly","When using liquid fuels originating from vegetable matter (e.g. turpentine, methanol, tall-oil), including those obtained as by-products of the pulping process, emission levels up to 350 mg/Nm3 (corresponding to 0,35 kg NOx/ADt) may occur."]
["Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Liquid fuels","Lime kilns","Air","Nitrogen dioxide","In order to reduce NOx emissions from a lime kiln, BAT is to apply a combination of the techniques given below: (i) Optimised combustion and combustion control; (ii) Good mixing of fuel and air; (iii) Low-NOx burner; (iv) Fuel selection/low-N fuel","kg NOx/Adt",0.1,0.2,"Green","Continuous",0,0,"Unspecified","Yearly","When using liquid fuels originating from vegetable matter (e.g. turpentine, methanol, tall-oil), including those obtained as by-products of the pulping process, emission levels up to 350 mg/Nm3 (corresponding to 0,35 kg NOx/ADt) may occur.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Liquid fuels","Lime kilns","Air","Nitrogen dioxide","In order to reduce NOx emissions from a lime kiln, BAT is to apply a combination of the techniques given below: (i) Optimised combustion and combustion control; (ii) Good mixing of fuel and air; (iii) Low-NOx burner; (iv) Fuel selection/low-N fuel","kg NOx/Adt",0.1,0.2,"Green","Continuous",0,0,"Unspecified","Yearly","When using liquid fuels originating from vegetable matter (e.g. turpentine, methanol, tall-oil), including those obtained as by-products of the pulping process, emission levels up to 350 mg/Nm3 (corresponding to 0,35 kg NOx/ADt) may occur."]
["Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","TRS burner for strong odorous gases ","Air","Nitrogen dioxide","In order to reduce NOx emissions from the incineration of strong odorous gases in a dedicated TRS burner, BAT is to use one or a combination of the techniques given below: (i) Burner/firing optimisation; (ii) Staged incineration","mg/Nm3",50,400,"Green","Continuous",0,0,0.09,"Yearly","Where at existing plants a switch to staged incineration is not feasible, emissions levels up to 1 000 mg/Nm3 (corresponding to 0,2 kg/ADt) may occur.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","TRS burner for strong odorous gases ","Air","Nitrogen dioxide","In order to reduce NOx emissions from the incineration of strong odorous gases in a dedicated TRS burner, BAT is to use one or a combination of the techniques given below: (i) Burner/firing optimisation; (ii) Staged incineration","mg/Nm3",50,400,"Green","Continuous",0,0,0.09,"Yearly","Where at existing plants a switch to staged incineration is not feasible, emissions levels up to 1 000 mg/Nm3 (corresponding to 0,2 kg/ADt) may occur."]
["Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","TRS burner for strong odorous gases ","Air","Nitrogen dioxide","In order to reduce NOx emissions from the incineration of strong odorous gases in a dedicated TRS burner, BAT is to use one or a combination of the techniques given below: (i) Burner/firing optimisation; (ii) Staged incineration","kg NOx/Adt",0.01,0.1,"Green","Continuous",0,0,"Unspecified","Yearly","Where at existing plants a switch to staged incineration is not feasible, emissions levels up to 1 000 mg/Nm3 (corresponding to 0,2 kg/ADt) may occur.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","TRS burner for strong odorous gases ","Air","Nitrogen dioxide","In order to reduce NOx emissions from the incineration of strong odorous gases in a dedicated TRS burner, BAT is to use one or a combination of the techniques given below: (i) Burner/firing optimisation; (ii) Staged incineration","kg NOx/Adt",0.01,0.1,"Green","Continuous",0,0,"Unspecified","Yearly","Where at existing plants a switch to staged incineration is not feasible, emissions levels up to 1 000 mg/Nm3 (corresponding to 0,2 kg/ADt) may occur."]
["Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Recovery boiler","Air","Nitrogen dioxide","In order to reduce NOx emissions from a recovery boiler, BAT is to use an optimised firing system including one or a combination of the techniques given below: (i) Optimising the recovery boiler by controlling the firing conditions; (ii) Staged injection of spent liquor; (iii) Selective non-catalytic reduction (SNCR)","mg/Nm3",100,350,"Green","Continuous",0,0,0.05,"Daily","For ammonium-based mills, higher emission levels of NOx may occur: up to 580 mg/Nm3 as daily average and up to 450 mg/Nm3 as yearly average.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Recovery boiler","Air","Nitrogen dioxide","In order to reduce NOx emissions from a recovery boiler, BAT is to use an optimised firing system including one or a combination of the techniques given below: (i) Optimising the recovery boiler by controlling the firing conditions; (ii) Staged injection of spent liquor; (iii) Selective non-catalytic reduction (SNCR)","mg/Nm3",100,350,"Green","Continuous",0,0,0.05,"Daily","For ammonium-based mills, higher emission levels of NOx may occur: up to 580 mg/Nm3 as daily average and up to 450 mg/Nm3 as yearly average."]
["Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Recovery boiler","Air","Nitrogen dioxide","In order to reduce NOx emissions from a recovery boiler, BAT is to use an optimised firing system including one or a combination of the techniques given below: (i) Optimising the recovery boiler by controlling the firing conditions; (ii) Staged injection of spent liquor; (iii) Selective non-catalytic reduction (SNCR)","mg/Nm3",100,270,"Green","Continuous",0,0,0.05,"Yearly","For ammonium-based mills, higher emission levels of NOx may occur: up to 580 mg/Nm3 as daily average and up to 450 mg/Nm3 as yearly average.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Recovery boiler","Air","Nitrogen dioxide","In order to reduce NOx emissions from a recovery boiler, BAT is to use an optimised firing system including one or a combination of the techniques given below: (i) Optimising the recovery boiler by controlling the firing conditions; (ii) Staged injection of spent liquor; (iii) Selective non-catalytic reduction (SNCR)","mg/Nm3",100,270,"Green","Continuous",0,0,0.05,"Yearly","For ammonium-based mills, higher emission levels of NOx may occur: up to 580 mg/Nm3 as daily average and up to 450 mg/Nm3 as yearly average."]
["Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Recovery boiler","Air","NOx (Hardwood)","In order to reduce NOx emissions from a recovery boiler, BAT is to use an optimised firing system including all of the features given below: (i) Computerised combustion control; (ii) Good mixing of fuel and air; (iii) Staged air feed systems, e.g. by using different air registers and air inlet ports","mg/Nm3",120,200,"Green","Continuous",0,0,0.06,"Yearly","Increasing the DS content of the black liquor results in lower SO2 emissions and higher NOx emissions. Due to this, a recovery boiler with low emission levels for SO2, may be on the higher end of the range for NOx and vice versa.\n\nThe actual NOx emission level of a recovery boiler depends on the DS content and the nitrogen content of the black liquor, and the amount and combination of NCG and other nitrogen containing flows (e.g. dissolving tank vent gas, methanol separated from the condensate, biosludge) burnt. The higher the DS content, the nitrogen content in the black liquor, and the amount of NCG and other nitrogen containing flows burnt, the closer the emissions will be to the upper end of the BAT-AEL range.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Recovery boiler","Air","NOx (Hardwood)","In order to reduce NOx emissions from a recovery boiler, BAT is to use an optimised firing system including all of the features given below: (i) Computerised combustion control; (ii) Good mixing of fuel and air; (iii) Staged air feed systems, e.g. by using different air registers and air inlet ports","mg/Nm3",120,200,"Green","Continuous",0,0,0.06,"Yearly","Increasing the DS content of the black liquor results in lower SO2 emissions and higher NOx emissions. Due to this, a recovery boiler with low emission levels for SO2, may be on the higher end of the range for NOx and vice versa.\n\nThe actual NOx emission level of a recovery boiler depends on the DS content and the nitrogen content of the black liquor, and the amount and combination of NCG and other nitrogen containing flows (e.g. dissolving tank vent gas, methanol separated from the condensate, biosludge) burnt. The higher the DS content, the nitrogen content in the black liquor, and the amount of NCG and other nitrogen containing flows burnt, the closer the emissions will be to the upper end of the BAT-AEL range."]
["Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Recovery boiler","Air","NOx (Hardwood) DS < 75%","In order to reduce NOx emissions from a recovery boiler, BAT is to use an optimised firing system including all of the features given below: (i) Computerised combustion control; (ii) Good mixing of fuel and air; (iii) Staged air feed systems, e.g. by using different air registers and air inlet ports","kg NOx/Adt",0.8,1.4,"Green","Continuous",0,0,"Unspecified","Yearly","Increasing the DS content of the black liquor results in lower SO2 emissions and higher NOx emissions. Due to this, a recovery boiler with low emission levels for SO2, may be on the higher end of the range for NOx and vice versa.\n\nIf a recovery boiler were to burn black liquor with a DS > 83 %, then NOx emission levels should be reconsidered on a case-by-case basis.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Recovery boiler","Air","NOx (Hardwood) DS < 75%","In order to reduce NOx emissions from a recovery boiler, BAT is to use an optimised firing system including all of the features given below: (i) Computerised combustion control; (ii) Good mixing of fuel and air; (iii) Staged air feed systems, e.g. by using different air registers and air inlet ports","kg NOx/Adt",0.8,1.4,"Green","Continuous",0,0,"Unspecified","Yearly","Increasing the DS content of the black liquor results in lower SO2 emissions and higher NOx emissions. Due to this, a recovery boiler with low emission levels for SO2, may be on the higher end of the range for NOx and vice versa.\n\nIf a recovery boiler were to burn black liquor with a DS > 83 %, then NOx emission levels should be reconsidered on a case-by-case basis."]
["Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Recovery boiler","Air","NOx (Hardwood) DS 75-83%","In order to reduce NOx emissions from a recovery boiler, BAT is to use an optimised firing system including all of the features given below: (i) Computerised combustion control; (ii) Good mixing of fuel and air; (iii) Staged air feed systems, e.g. by using different air registers and air inlet ports","kg NOx/Adt",1,1.7,"Green","Continuous",0,0,"Unspecified","Yearly","Increasing the DS content of the black liquor results in lower SO2 emissions and higher NOx emissions. Due to this, a recovery boiler with low emission levels for SO2, may be on the higher end of the range for NOx and vice versa.\n\nIf a recovery boiler were to burn black liquor with a DS > 83 %, then NOx emission levels should be reconsidered on a case-by-case basis.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Recovery boiler","Air","NOx (Hardwood) DS 75-83%","In order to reduce NOx emissions from a recovery boiler, BAT is to use an optimised firing system including all of the features given below: (i) Computerised combustion control; (ii) Good mixing of fuel and air; (iii) Staged air feed systems, e.g. by using different air registers and air inlet ports","kg NOx/Adt",1,1.7,"Green","Continuous",0,0,"Unspecified","Yearly","Increasing the DS content of the black liquor results in lower SO2 emissions and higher NOx emissions. Due to this, a recovery boiler with low emission levels for SO2, may be on the higher end of the range for NOx and vice versa.\n\nIf a recovery boiler were to burn black liquor with a DS > 83 %, then NOx emission levels should be reconsidered on a case-by-case basis."]
["Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Recovery boiler","Air","NOx (softwood)","In order to reduce NOx emissions from a recovery boiler, BAT is to use an optimised firing system including all of the features given below: (i) Computerised combustion control; (ii) Good mixing of fuel and air; (iii) Staged air feed systems, e.g. by using different air registers and air inlet ports","mg/Nm3",120,200,"Green","Continuous",0,0,0.06,"Yearly","Increasing the DS content of the black liquor results in lower SO2 emissions and higher NOx emissions. Due to this, a recovery boiler with low emission levels for SO2, may be on the higher end of the range for NOx and vice versa.\n\nThe actual NOx emission level of a recovery boiler depends on the DS content and the nitrogen content of the black liquor, and the amount and combination of NCG and other nitrogen containing flows (e.g. dissolving tank vent gas, methanol separated from the condensate, biosludge) burnt. The higher the DS content, the nitrogen content in the black liquor, and the amount of NCG and other nitrogen containing flows burnt, the closer the emissions will be to the upper end of the BAT-AEL range.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Recovery boiler","Air","NOx (softwood)","In order to reduce NOx emissions from a recovery boiler, BAT is to use an optimised firing system including all of the features given below: (i) Computerised combustion control; (ii) Good mixing of fuel and air; (iii) Staged air feed systems, e.g. by using different air registers and air inlet ports","mg/Nm3",120,200,"Green","Continuous",0,0,0.06,"Yearly","Increasing the DS content of the black liquor results in lower SO2 emissions and higher NOx emissions. Due to this, a recovery boiler with low emission levels for SO2, may be on the higher end of the range for NOx and vice versa.\n\nThe actual NOx emission level of a recovery boiler depends on the DS content and the nitrogen content of the black liquor, and the amount and combination of NCG and other nitrogen containing flows (e.g. dissolving tank vent gas, methanol separated from the condensate, biosludge) burnt. The higher the DS content, the nitrogen content in the black liquor, and the amount of NCG and other nitrogen containing flows burnt, the closer the emissions will be to the upper end of the BAT-AEL range."]
["Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Recovery boiler","Air","NOx (softwood) DS 75- 83%","In order to reduce NOx emissions from a recovery boiler, BAT is to use an optimised firing system including all of the features given below: (i) Computerised combustion control; (ii) Good mixing of fuel and air; (iii) Staged air feed systems, e.g. by using different air registers and air inlet ports","kg NOx/Adt",1,1.6,"Green","Continuous",0,0,"Unspecified","Yearly","Increasing the DS content of the black liquor results in lower SO2 emissions and higher NOx emissions. Due to this, a recovery boiler with low emission levels for SO2, may be on the higher end of the range for NOx and vice versa.\n\nIf a recovery boiler were to burn black liquor with a DS > 83 %, then NOx emission levels should be reconsidered on a case-by-case basis.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Recovery boiler","Air","NOx (softwood) DS 75- 83%","In order to reduce NOx emissions from a recovery boiler, BAT is to use an optimised firing system including all of the features given below: (i) Computerised combustion control; (ii) Good mixing of fuel and air; (iii) Staged air feed systems, e.g. by using different air registers and air inlet ports","kg NOx/Adt",1,1.6,"Green","Continuous",0,0,"Unspecified","Yearly","Increasing the DS content of the black liquor results in lower SO2 emissions and higher NOx emissions. Due to this, a recovery boiler with low emission levels for SO2, may be on the higher end of the range for NOx and vice versa.\n\nIf a recovery boiler were to burn black liquor with a DS > 83 %, then NOx emission levels should be reconsidered on a case-by-case basis."]
["Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Recovery boiler","Air","NOx (softwood) DS< 75%","In order to reduce NOx emissions from a recovery boiler, BAT is to use an optimised firing system including all of the features given below: (i) Computerised combustion control; (ii) Good mixing of fuel and air; (iii) Staged air feed systems, e.g. by using different air registers and air inlet ports","kg NOx/Adt",0.8,1.4,"Green","Continuous",0,0,"Unspecified","Yearly","Increasing the DS content of the black liquor results in lower SO2 emissions and higher NOx emissions. Due to this, a recovery boiler with low emission levels for SO2, may be on the higher end of the range for NOx and vice versa.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Recovery boiler","Air","NOx (softwood) DS< 75%","In order to reduce NOx emissions from a recovery boiler, BAT is to use an optimised firing system including all of the features given below: (i) Computerised combustion control; (ii) Good mixing of fuel and air; (iii) Staged air feed systems, e.g. by using different air registers and air inlet ports","kg NOx/Adt",0.8,1.4,"Green","Continuous",0,0,"Unspecified","Yearly","Increasing the DS content of the black liquor results in lower SO2 emissions and higher NOx emissions. Due to this, a recovery boiler with low emission levels for SO2, may be on the higher end of the range for NOx and vice versa."]
["Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Recovery boiler","Air","Sulphur Dioxide (24 Hour Mean)","In order to reduce dust and SO2 emissions from a recovery boiler, BAT is to use one of the techniques given below and to limit ‘acid operation’ of the scrubbers to the minimum required to ensure their proper functioning: (i) ESP or multicyclones with multistage venturi scrubbers; (ii) ESP or multicyclones with multistage double inlet downstream scrubbers","mg/Nm3",100,300,"Green","Continuous",0,0,0.05,"Daily","Due to process-specific higher emissions, the BAT-AEL for SO2 does not apply for recovery boilers operated permanently under ‘acidic’ conditions, i.e. using sulphite liquor as wet-scrubber washing media as part of the sulphite recovery process.\n\n For existing multistage venturi scrubbers, higher emissions of SO2 up to 400 mg/Nm3 as a daily average value and up to 350 mg/Nm3 as a yearly average may occur.\n\nNot applicable during ‘acid operation’, i.e. periods in which preventive flushing and cleaning of incrustation in the scrubbers takes place. During these periods emissions can be up to 300 – 500 mg SO2/Nm3 (at 5 % O2) for cleaning of one of the scrubbers and up to 1 200 mg SO2/Nm3 (half-hourly mean values, at 5 % O2) when cleaning the final washer.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Recovery boiler","Air","Sulphur Dioxide (24 Hour Mean)","In order to reduce dust and SO2 emissions from a recovery boiler, BAT is to use one of the techniques given below and to limit ‘acid operation’ of the scrubbers to the minimum required to ensure their proper functioning: (i) ESP or multicyclones with multistage venturi scrubbers; (ii) ESP or multicyclones with multistage double inlet downstream scrubbers","mg/Nm3",100,300,"Green","Continuous",0,0,0.05,"Daily","Due to process-specific higher emissions, the BAT-AEL for SO2 does not apply for recovery boilers operated permanently under ‘acidic’ conditions, i.e. using sulphite liquor as wet-scrubber washing media as part of the sulphite recovery process.\n\n For existing multistage venturi scrubbers, higher emissions of SO2 up to 400 mg/Nm3 as a daily average value and up to 350 mg/Nm3 as a yearly average may occur.\n\nNot applicable during ‘acid operation’, i.e. periods in which preventive flushing and cleaning of incrustation in the scrubbers takes place. During these periods emissions can be up to 300 – 500 mg SO2/Nm3 (at 5 % O2) for cleaning of one of the scrubbers and up to 1 200 mg SO2/Nm3 (half-hourly mean values, at 5 % O2) when cleaning the final washer."]
["Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Recovery boiler","Air","Sulphur Dioxide (24 Hour Mean)","In order to reduce dust and SO2 emissions from a recovery boiler, BAT is to use one of the techniques given below and to limit ‘acid operation’ of the scrubbers to the minimum required to ensure their proper functioning: (i) ESP or multicyclones with multistage venturi scrubbers; (ii) ESP or multicyclones with multistage double inlet downstream scrubbers","mg/Nm3",50,250,"Green","Continuous",0,0,0.05,"Yearly","Due to process-specific higher emissions, the BAT-AEL for SO2 does not apply for recovery boilers operated permanently under ‘acidic’ conditions, i.e. using sulphite liquor as wet-scrubber washing media as part of the sulphite recovery process.\n\nFor existing multistage venturi scrubbers, higher emissions of SO2 up to 400 mg/Nm3 as a daily average value and up to 350 mg/Nm3 as a yearly average may occur.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Recovery boiler","Air","Sulphur Dioxide (24 Hour Mean)","In order to reduce dust and SO2 emissions from a recovery boiler, BAT is to use one of the techniques given below and to limit ‘acid operation’ of the scrubbers to the minimum required to ensure their proper functioning: (i) ESP or multicyclones with multistage venturi scrubbers; (ii) ESP or multicyclones with multistage double inlet downstream scrubbers","mg/Nm3",50,250,"Green","Continuous",0,0,0.05,"Yearly","Due to process-specific higher emissions, the BAT-AEL for SO2 does not apply for recovery boilers operated permanently under ‘acidic’ conditions, i.e. using sulphite liquor as wet-scrubber washing media as part of the sulphite recovery process.\n\nFor existing multistage venturi scrubbers, higher emissions of SO2 up to 400 mg/Nm3 as a daily average value and up to 350 mg/Nm3 as a yearly average may occur."]
["Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","TRS burner for strong odorous gases ","Air","Sulphur Dioxide (24 Hour Mean)","In order to reduce SO2 emissions from the incineration of strong odorous gases in a dedicated TRS burner, BAT is to use an alkaline SO2 scrubber.","mg/Nm3",20,120,"Green","Continuous",0,0,0.09,"Yearly",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","TRS burner for strong odorous gases ","Air","Sulphur Dioxide (24 Hour Mean)","In order to reduce SO2 emissions from the incineration of strong odorous gases in a dedicated TRS burner, BAT is to use an alkaline SO2 scrubber.","mg/Nm3",20,120,"Green","Continuous",0,0,0.09,"Yearly",0]
["Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Recovery boiler","Air","Sulphur Dioxide (24 Hour Mean)","In order to reduce SO2 and TRS emissions from a recovery boiler, BAT is to use a combination of the techniques given below: (i) Increasing the dry solids (DS) content of black liquor; (ii) Optimised firing; (iii) Wet scrubber","mg/Nm3",10,70,"Green","Continuous",0,0,0.06,"Daily","Increasing the DS content of the black liquor results in lower SO2 emissions and higher NOx emissions. Due to this, a recovery boiler with low emission levels for SO2, may be on the higher end of the range for NOx and vice versa.\n\nBAT-AELs do not cover periods during which the recovery boiler is run on a DS content much lower than the normal DS content due to shut down or maintenance of the black liquor concentration plant.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Recovery boiler","Air","Sulphur Dioxide (24 Hour Mean)","In order to reduce SO2 and TRS emissions from a recovery boiler, BAT is to use a combination of the techniques given below: (i) Increasing the dry solids (DS) content of black liquor; (ii) Optimised firing; (iii) Wet scrubber","mg/Nm3",10,70,"Green","Continuous",0,0,0.06,"Daily","Increasing the DS content of the black liquor results in lower SO2 emissions and higher NOx emissions. Due to this, a recovery boiler with low emission levels for SO2, may be on the higher end of the range for NOx and vice versa.\n\nBAT-AELs do not cover periods during which the recovery boiler is run on a DS content much lower than the normal DS content due to shut down or maintenance of the black liquor concentration plant."]
["Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Recovery boiler","Air","Sulphur Dioxide (24 Hour Mean)","In order to reduce SO2 and TRS emissions from a recovery boiler, BAT is to use a combination of the techniques given below: (i) Increasing the dry solids (DS) content of black liquor; (ii) Optimised firing; (iii) Wet scrubber","mg/Nm3",5,50,"Green","Continuous",0,0,0.06,"Yearly","Increasing the DS content of the black liquor results in lower SO2 emissions and higher NOx emissions. Due to this, a recovery boiler with low emission levels for SO2, may be on the higher end of the range for NOx and vice versa.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Recovery boiler","Air","Sulphur Dioxide (24 Hour Mean)","In order to reduce SO2 and TRS emissions from a recovery boiler, BAT is to use a combination of the techniques given below: (i) Increasing the dry solids (DS) content of black liquor; (ii) Optimised firing; (iii) Wet scrubber","mg/Nm3",5,50,"Green","Continuous",0,0,0.06,"Yearly","Increasing the DS content of the black liquor results in lower SO2 emissions and higher NOx emissions. Due to this, a recovery boiler with low emission levels for SO2, may be on the higher end of the range for NOx and vice versa."]
["Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Recovery boiler","Air","Sulphur Dioxide (24 Hour Mean)","In order to reduce SO2 and TRS emissions from a recovery boiler, BAT is to use a combination of the techniques given below: (i) Increasing the dry solids (DS) content of black liquor; (ii) Optimised firing; (iii) Wet scrubber","mg/Nm3",10,50,"Green","Continuous",0,0,0.06,"Daily","Increasing the DS content of the black liquor results in lower SO2 emissions and higher NOx emissions. Due to this, a recovery boiler with low emission levels for SO2, may be on the higher end of the range for NOx and vice versa.\n\nBAT-AELs do not cover periods during which the recovery boiler is run on a DS content much lower than the normal DS content due to shut down or maintenance of the black liquor concentration plant.\n\nIf a recovery boiler were to burn black liquor with a DS > 83 %, then SO2 and gaseous S emission levels should be reconsidered on a case-by-case basis.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Recovery boiler","Air","Sulphur Dioxide (24 Hour Mean)","In order to reduce SO2 and TRS emissions from a recovery boiler, BAT is to use a combination of the techniques given below: (i) Increasing the dry solids (DS) content of black liquor; (ii) Optimised firing; (iii) Wet scrubber","mg/Nm3",10,50,"Green","Continuous",0,0,0.06,"Daily","Increasing the DS content of the black liquor results in lower SO2 emissions and higher NOx emissions. Due to this, a recovery boiler with low emission levels for SO2, may be on the higher end of the range for NOx and vice versa.\n\nBAT-AELs do not cover periods during which the recovery boiler is run on a DS content much lower than the normal DS content due to shut down or maintenance of the black liquor concentration plant.\n\nIf a recovery boiler were to burn black liquor with a DS > 83 %, then SO2 and gaseous S emission levels should be reconsidered on a case-by-case basis."]
["Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Recovery boiler","Air","Sulphur Dioxide (24 Hour Mean)","In order to reduce SO2 and TRS emissions from a recovery boiler, BAT is to use a combination of the techniques given below: (i) Increasing the dry solids (DS) content of black liquor; (ii) Optimised firing; (iii) Wet scrubber","mg/Nm3",5,25,"Green","Continuous",0,0,0.06,"Yearly","Increasing the DS content of the black liquor results in lower SO2 emissions and higher NOx emissions. Due to this, a recovery boiler with low emission levels for SO2, may be on the higher end of the range for NOx and vice versa.\n\nIf a recovery boiler were to burn black liquor with a DS > 83 %, then SO2 and gaseous S emission levels should be reconsidered on a case-by-case basis.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Recovery boiler","Air","Sulphur Dioxide (24 Hour Mean)","In order to reduce SO2 and TRS emissions from a recovery boiler, BAT is to use a combination of the techniques given below: (i) Increasing the dry solids (DS) content of black liquor; (ii) Optimised firing; (iii) Wet scrubber","mg/Nm3",5,25,"Green","Continuous",0,0,0.06,"Yearly","Increasing the DS content of the black liquor results in lower SO2 emissions and higher NOx emissions. Due to this, a recovery boiler with low emission levels for SO2, may be on the higher end of the range for NOx and vice versa.\n\nIf a recovery boiler were to burn black liquor with a DS > 83 %, then SO2 and gaseous S emission levels should be reconsidered on a case-by-case basis."]
["Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Lime kilns","Air","Sulphur Dioxide (24 Hour Mean)","In order to reduce SO2 emissions from a lime kiln, BAT is to apply one or a combination of the techniques given below: (i) Fuel selection/low sulphur fuel; (ii) Limit incineration of sulphur-containing odorous strong gases in the lime kiln; (iii) Control of Na2S content in lime mud feed; (iv) Alkaline scrubber\n","mg/Nm3",5,70,"Green","Continuous",0,0,0.06,"Yearly","‘strong gases’ includes methanol and turpentine",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Lime kilns","Air","Sulphur Dioxide (24 Hour Mean)","In order to reduce SO2 emissions from a lime kiln, BAT is to apply one or a combination of the techniques given below: (i) Fuel selection/low sulphur fuel; (ii) Limit incineration of sulphur-containing odorous strong gases in the lime kiln; (iii) Control of Na2S content in lime mud feed; (iv) Alkaline scrubber\n","mg/Nm3",5,70,"Green","Continuous",0,0,0.06,"Yearly","‘strong gases’ includes methanol and turpentine"]
["Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Lime kilns","Air","Sulphur Dioxide (24 Hour Mean)","In order to reduce SO2 emissions from a lime kiln, BAT is to apply one or a combination of the techniques given below: (i) Fuel selection/low sulphur fuel; (ii) Limit incineration of sulphur-containing odorous strong gases in the lime kiln; (iii) Control of Na2S content in lime mud feed; (iv) Alkaline scrubber\n","mg/Nm3",55,120,"Green","Continuous",0,0,0.06,"Yearly","‘strong gases’ includes methanol and turpentine",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Lime kilns","Air","Sulphur Dioxide (24 Hour Mean)","In order to reduce SO2 emissions from a lime kiln, BAT is to apply one or a combination of the techniques given below: (i) Fuel selection/low sulphur fuel; (ii) Limit incineration of sulphur-containing odorous strong gases in the lime kiln; (iii) Control of Na2S content in lime mud feed; (iv) Alkaline scrubber\n","mg/Nm3",55,120,"Green","Continuous",0,0,0.06,"Yearly","‘strong gases’ includes methanol and turpentine"]
["Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Lime kilns","Air","Total Reduced Sulphur (TRS) ","In order to reduce TRS emissions from a lime kiln, BAT is to apply one or a combination of the techniques given below: (i) Control of the excess oxygen; (ii) Control of Na2S content in lime mud feed; (iii) Combination of ESP and alkaline scrubber","mg S/nm3",1,10,"Green","Unspeciified",0,0,0.06,"Yearly","For lime kilns burning strong gases (including methanol and turpentine), the upper end of the AEL range may be up to 40 mg/Nm3.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Lime kilns","Air","Total Reduced Sulphur (TRS) ","In order to reduce TRS emissions from a lime kiln, BAT is to apply one or a combination of the techniques given below: (i) Control of the excess oxygen; (ii) Control of Na2S content in lime mud feed; (iii) Combination of ESP and alkaline scrubber","mg S/nm3",1,10,"Green","Unspeciified",0,0,0.06,"Yearly","For lime kilns burning strong gases (including methanol and turpentine), the upper end of the AEL range may be up to 40 mg/Nm3."]
["Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Air","Total Reduced Sulphur (TRS) ","In order to reduce odour emissions and total reduced sulphur emissions due to strong and weak odorous gases, BAT is to prevent diffuse emissions by capturing all process-based sulphur containing off-gases, including all vents with sulphur-containing emissions, by applying all of the techniques given below: (i) Collection systems for strong and weak odorous gases; (ii) Incineration of strong and weak non-condensable gases; (iii) Recording unavailability of the incineration system and any resulting emissions","kg S/Adt",0.05,0.2,"Green","Unspeciified",0,0,"Unspecified","Unspeciified",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Air","Total Reduced Sulphur (TRS) ","In order to reduce odour emissions and total reduced sulphur emissions due to strong and weak odorous gases, BAT is to prevent diffuse emissions by capturing all process-based sulphur containing off-gases, including all vents with sulphur-containing emissions, by applying all of the techniques given below: (i) Collection systems for strong and weak odorous gases; (ii) Incineration of strong and weak non-condensable gases; (iii) Recording unavailability of the incineration system and any resulting emissions","kg S/Adt",0.05,0.2,"Green","Unspeciified",0,0,"Unspecified","Unspeciified",0]
["Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","TRS burner for strong odorous gases ","Air","Total Reduced Sulphur (TRS) ","In order to reduce SO2 emissions from the incineration of strong odorous gases in a dedicated TRS burner, BAT is to use an alkaline SO2 scrubber.","mg/Nm3",1,5,"Green","Continuous",0,0,0.09,"Yearly",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","TRS burner for strong odorous gases ","Air","Total Reduced Sulphur (TRS) ","In order to reduce SO2 emissions from the incineration of strong odorous gases in a dedicated TRS burner, BAT is to use an alkaline SO2 scrubber.","mg/Nm3",1,5,"Green","Continuous",0,0,0.09,"Yearly",0]
["Pulp and paper","6. Other activities","Excluding speciality paper ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.","kg/t","N/A",0.05,"Green","Once every 2 months",0,0,"Unspecified","Yearly",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Excluding speciality paper ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.","kg/t","N/A",0.05,"Green","Once every 2 months",0,0,"Unspecified","Yearly",0]
["Pulp and paper","6. Other activities","Bleached kraft pulp mill","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions of pollutants into receiving waters from the whole mill, BAT is to use TCF or modern ECF bleaching (see description in Section 1.7.2.1), and a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Modified cooking before bleaching; (ii) Oxygen delignification before bleaching; (iii) Closed brown stock screening and efficient brown stock washing; (iv) Partial process water recycling in the bleach plant; (v) Effective spill monitoring and containment with a suitable recovery system; (vi) Maintaining sufficient black liquor evaporation and recovery boiler capacity to cope with peak loads; (vii) Stripping the contaminated (foul) condensates and reusing the condensates in the process","kg/Adt",0,0.2,"Green","Monthly",0,0,"Unspecified","Yearly","The BAT-AEL ranges refer to market pulp production and the pulp production part of integrated mills (emissions from papermaking are not included).\n\nApplicable for mills using chlorine containing bleaching chemicals.\n\nFor mills producing pulp with high strength, stiffness and high purity properties (e.g. for liquid packaging board and LWC), emissions level of AOX up to 0,25 kg/ADt may occur.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Bleached kraft pulp mill","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions of pollutants into receiving waters from the whole mill, BAT is to use TCF or modern ECF bleaching (see description in Section 1.7.2.1), and a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Modified cooking before bleaching; (ii) Oxygen delignification before bleaching; (iii) Closed brown stock screening and efficient brown stock washing; (iv) Partial process water recycling in the bleach plant; (v) Effective spill monitoring and containment with a suitable recovery system; (vi) Maintaining sufficient black liquor evaporation and recovery boiler capacity to cope with peak loads; (vii) Stripping the contaminated (foul) condensates and reusing the condensates in the process","kg/Adt",0,0.2,"Green","Monthly",0,0,"Unspecified","Yearly","The BAT-AEL ranges refer to market pulp production and the pulp production part of integrated mills (emissions from papermaking are not included).\n\nApplicable for mills using chlorine containing bleaching chemicals.\n\nFor mills producing pulp with high strength, stiffness and high purity properties (e.g. for liquid packaging board and LWC), emissions level of AOX up to 0,25 kg/ADt may occur."]
["Pulp and paper","6. Other activities","Bleached sulphite paper grade pulp   ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Pulp mill","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce emissions of pollutants into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Extended modified cooking before bleaching.; (ii) Oxygen delignification before bleaching; (iii) Closed brown stock screening and efficient brown stock washing.; (iv) Evaporation of effluents from the hot alkaline extraction stage and incineration of concentrates in a soda boiler; (v) TCF bleaching; (vi) Closed-loop bleaching; (vii) MgO-based pre-bleaching and recirculation of washing liquids from pre- bleaching to brown stock washing; (viii) pH adjustment of weak liquor before/ inside the evaporation plant; (ix) Anaerobic treatment of the condensates from the evaporators; (x) Stripping and recovery of SO2 from the condensates of evaporators; (xi) Effective spill monitoring and containment, also with chemical and energy recovery system","mg/l",0.5,1.5,"Green","Once every 2 months",0,0,"Unspecified","Yearly","The BAT-AEL ranges refer to market pulp production and the pulp production part of integrated mills (emissions from papermaking are not included).\n\nThe BAT-AELs do not apply to natural greaseproof pulp mills).\n\nSulphite market pulp mills may apply a gentle ClO2 bleaching stage in order to meet product requirements, thus resulting in AOX emissions.\n\nNot applicable to TCF mills",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Bleached sulphite paper grade pulp   ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Pulp mill","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce emissions of pollutants into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Extended modified cooking before bleaching.; (ii) Oxygen delignification before bleaching; (iii) Closed brown stock screening and efficient brown stock washing.; (iv) Evaporation of effluents from the hot alkaline extraction stage and incineration of concentrates in a soda boiler; (v) TCF bleaching; (vi) Closed-loop bleaching; (vii) MgO-based pre-bleaching and recirculation of washing liquids from pre- bleaching to brown stock washing; (viii) pH adjustment of weak liquor before/ inside the evaporation plant; (ix) Anaerobic treatment of the condensates from the evaporators; (x) Stripping and recovery of SO2 from the condensates of evaporators; (xi) Effective spill monitoring and containment, also with chemical and energy recovery system","mg/l",0.5,1.5,"Green","Once every 2 months",0,0,"Unspecified","Yearly","The BAT-AEL ranges refer to market pulp production and the pulp production part of integrated mills (emissions from papermaking are not included).\n\nThe BAT-AELs do not apply to natural greaseproof pulp mills).\n\nSulphite market pulp mills may apply a gentle ClO2 bleaching stage in order to meet product requirements, thus resulting in AOX emissions.\n\nNot applicable to TCF mills"]
["Pulp and paper","6. Other activities","Excluding speciality paper ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Non-integrated speciality paper mill ","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.","kg/t","N/A",0.05,"Green","Once every 2 months",0,0,"Unspecified","Yearly",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Excluding speciality paper ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Non-integrated speciality paper mill ","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.","kg/t","N/A",0.05,"Green","Once every 2 months",0,0,"Unspecified","Yearly",0]
["Pulp and paper","6. Other activities","Paper and board from recycled fibres pulp produced with deinking on site ","Wet strength paper ","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.","kg/t","N/A",0.05,"Green","Once every 2 months",0,0,"Unspecified","Yearly",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Paper and board from recycled fibres pulp produced with deinking on site ","Wet strength paper ","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.","kg/t","N/A",0.05,"Green","Once every 2 months",0,0,"Unspecified","Yearly",0]
["Pulp and paper","6. Other activities","Paper and board from recycled fibres pulp produced without deinking on site ","Wet strength paper ","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.","kg/t","N/A",0.05,"Green","Once every 2 months",0,0,"Unspecified","Yearly",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Paper and board from recycled fibres pulp produced without deinking on site ","Wet strength paper ","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.","kg/t","N/A",0.05,"Green","Once every 2 months",0,0,"Unspecified","Yearly",0]
["Pulp and paper","6. Other activities","Bleached kraft pulp mill","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions of pollutants into receiving waters from the whole mill, BAT is to use TCF or modern ECF bleaching (see description in Section 1.7.2.1), and a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Modified cooking before bleaching; (ii) Oxygen delignification before bleaching; (iii) Closed brown stock screening and efficient brown stock washing; (iv) Partial process water recycling in the bleach plant; (v) Effective spill monitoring and containment with a suitable recovery system; (vi) Maintaining sufficient black liquor evaporation and recovery boiler capacity to cope with peak loads; (vii) Stripping the contaminated (foul) condensates and reusing the condensates in the process","kg/Adt",7,20,"Green","Daily",0,0,"Unspecified","Yearly","The BAT-AEL ranges refer to market pulp production and the pulp production part of integrated mills (emissions from papermaking are not included).",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Bleached kraft pulp mill","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions of pollutants into receiving waters from the whole mill, BAT is to use TCF or modern ECF bleaching (see description in Section 1.7.2.1), and a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Modified cooking before bleaching; (ii) Oxygen delignification before bleaching; (iii) Closed brown stock screening and efficient brown stock washing; (iv) Partial process water recycling in the bleach plant; (v) Effective spill monitoring and containment with a suitable recovery system; (vi) Maintaining sufficient black liquor evaporation and recovery boiler capacity to cope with peak loads; (vii) Stripping the contaminated (foul) condensates and reusing the condensates in the process","kg/Adt",7,20,"Green","Daily",0,0,"Unspecified","Yearly","The BAT-AEL ranges refer to market pulp production and the pulp production part of integrated mills (emissions from papermaking are not included)."]
["Pulp and paper","6. Other activities","Bleached sulphite paper grade pulp   ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Pulp mill","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce emissions of pollutants into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Extended modified cooking before bleaching.; (ii) Oxygen delignification before bleaching; (iii) Closed brown stock screening and efficient brown stock washing.; (iv) Evaporation of effluents from the hot alkaline extraction stage and incineration of concentrates in a soda boiler; (v) TCF bleaching; (vi) Closed-loop bleaching; (vii) MgO-based pre-bleaching and recirculation of washing liquids from pre- bleaching to brown stock washing; (viii) pH adjustment of weak liquor before/ inside the evaporation plant; (ix) Anaerobic treatment of the condensates from the evaporators; (x) Stripping and recovery of SO2 from the condensates of evaporators; (xi) Effective spill monitoring and containment, also with chemical and energy recovery system","kg/ADt",10,30,"Green","Daily",0,0,"Unspecified","Yearly","The BAT-AEL ranges refer to market pulp production and the pulp production part of integrated mills (emissions from papermaking are not included).\n\nThe BAT-AELs do not apply to natural greaseproof pulp mills).\n\nThe BAT-AEL for COD and total phosphorus do not apply to eucalyptus based market pulp",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Bleached sulphite paper grade pulp   ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Pulp mill","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce emissions of pollutants into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Extended modified cooking before bleaching.; (ii) Oxygen delignification before bleaching; (iii) Closed brown stock screening and efficient brown stock washing.; (iv) Evaporation of effluents from the hot alkaline extraction stage and incineration of concentrates in a soda boiler; (v) TCF bleaching; (vi) Closed-loop bleaching; (vii) MgO-based pre-bleaching and recirculation of washing liquids from pre- bleaching to brown stock washing; (viii) pH adjustment of weak liquor before/ inside the evaporation plant; (ix) Anaerobic treatment of the condensates from the evaporators; (x) Stripping and recovery of SO2 from the condensates of evaporators; (xi) Effective spill monitoring and containment, also with chemical and energy recovery system","kg/ADt",10,30,"Green","Daily",0,0,"Unspecified","Yearly","The BAT-AEL ranges refer to market pulp production and the pulp production part of integrated mills (emissions from papermaking are not included).\n\nThe BAT-AELs do not apply to natural greaseproof pulp mills).\n\nThe BAT-AEL for COD and total phosphorus do not apply to eucalyptus based market pulp"]
["Pulp and paper","6. Other activities","Excluding speciality paper ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.","kg/t",0.15,1.5,"Green","Daily",0,0,"Unspecified","Yearly","For graphic paper mills, the upper end of the range refers to mills manufacturing paper that use starch for the coating process.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Excluding speciality paper ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.","kg/t",0.15,1.5,"Green","Daily",0,0,"Unspecified","Yearly","For graphic paper mills, the upper end of the range refers to mills manufacturing paper that use starch for the coating process."]
["Pulp and paper","6. Other activities","Excluding speciality paper ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Non-integrated speciality paper mill ","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.","kg/t",0.3,5,"Green","Daily",0,0,"Unspecified","Yearly","Mills having special characteristics, such as a high number of grade changes (e.g. of ≥ 5 per day as a yearly average) or producing very light-weight speciality papers (≤ 30 g/m2 as yearly average) might have higher emissions than the upper end of the range.\n\nThe upper end of the BAT-AEL range refers to mills producing highly comminuted paper which requires intensive refining and to mills with frequent changes of paper grades (e.g. ≥ 1 – 2 changes/day as yearly average).",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Excluding speciality paper ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Non-integrated speciality paper mill ","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.","kg/t",0.3,5,"Green","Daily",0,0,"Unspecified","Yearly","Mills having special characteristics, such as a high number of grade changes (e.g. of ≥ 5 per day as a yearly average) or producing very light-weight speciality papers (≤ 30 g/m2 as yearly average) might have higher emissions than the upper end of the range.\n\nThe upper end of the BAT-AEL range refers to mills producing highly comminuted paper which requires intensive refining and to mills with frequent changes of paper grades (e.g. ≥ 1 – 2 changes/day as yearly average)."]
["Pulp and paper","6. Other activities","Magnefite paper grade pulp","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Pulp mill","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce emissions of pollutants into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Extended modified cooking before bleaching.; (ii) Oxygen delignification before bleaching; (iii) Closed brown stock screening and efficient brown stock washing.; (iv) Evaporation of effluents from the hot alkaline extraction stage and incineration of concentrates in a soda boiler; (v) TCF bleaching; (vi) Closed-loop bleaching; (vii) MgO-based pre-bleaching and recirculation of washing liquids from pre- bleaching to brown stock washing; (viii) pH adjustment of weak liquor before/ inside the evaporation plant; (ix) Anaerobic treatment of the condensates from the evaporators; (x) Stripping and recovery of SO2 from the condensates of evaporators; (xi) Effective spill monitoring and containment, also with chemical and energy recovery system","kg/ADt",20,35,"Green","Daily",0,0,"Unspecified","Yearly","The BAT-AEL ranges refer to market pulp production and the pulp production part of integrated mills (emissions from papermaking are not included).",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Magnefite paper grade pulp","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Pulp mill","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce emissions of pollutants into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Extended modified cooking before bleaching.; (ii) Oxygen delignification before bleaching; (iii) Closed brown stock screening and efficient brown stock washing.; (iv) Evaporation of effluents from the hot alkaline extraction stage and incineration of concentrates in a soda boiler; (v) TCF bleaching; (vi) Closed-loop bleaching; (vii) MgO-based pre-bleaching and recirculation of washing liquids from pre- bleaching to brown stock washing; (viii) pH adjustment of weak liquor before/ inside the evaporation plant; (ix) Anaerobic treatment of the condensates from the evaporators; (x) Stripping and recovery of SO2 from the condensates of evaporators; (xi) Effective spill monitoring and containment, also with chemical and energy recovery system","kg/ADt",20,35,"Green","Daily",0,0,"Unspecified","Yearly","The BAT-AEL ranges refer to market pulp production and the pulp production part of integrated mills (emissions from papermaking are not included)."]
["Pulp and paper","6. Other activities","NSSC pulp","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Sulphite pulp mill","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce emissions of pollutants into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Extended modified cooking before bleaching.; (ii) Oxygen delignification before bleaching; (iii) Closed brown stock screening and efficient brown stock washing.; (iv) Evaporation of effluents from the hot alkaline extraction stage and incineration of concentrates in a soda boiler; (v) TCF bleaching; (vi) Closed-loop bleaching; (vii) MgO-based pre-bleaching and recirculation of washing liquids from pre- bleaching to brown stock washing; (viii) pH adjustment of weak liquor before/ inside the evaporation plant; (ix) Anaerobic treatment of the condensates from the evaporators; (x) Stripping and recovery of SO2 from the condensates of evaporators; (xi) Effective spill monitoring and containment, also with chemical and energy recovery system","kg/ADt",3.2,11,"Green","Daily",0,0,"Unspecified","Yearly","The BAT-AEL ranges refer to market pulp production and the pulp production part of integrated mills (emissions from papermaking are not included).",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","NSSC pulp","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Sulphite pulp mill","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce emissions of pollutants into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Extended modified cooking before bleaching.; (ii) Oxygen delignification before bleaching; (iii) Closed brown stock screening and efficient brown stock washing.; (iv) Evaporation of effluents from the hot alkaline extraction stage and incineration of concentrates in a soda boiler; (v) TCF bleaching; (vi) Closed-loop bleaching; (vii) MgO-based pre-bleaching and recirculation of washing liquids from pre- bleaching to brown stock washing; (viii) pH adjustment of weak liquor before/ inside the evaporation plant; (ix) Anaerobic treatment of the condensates from the evaporators; (x) Stripping and recovery of SO2 from the condensates of evaporators; (xi) Effective spill monitoring and containment, also with chemical and energy recovery system","kg/ADt",3.2,11,"Green","Daily",0,0,"Unspecified","Yearly","The BAT-AEL ranges refer to market pulp production and the pulp production part of integrated mills (emissions from papermaking are not included)."]
["Pulp and paper","6. Other activities","Paper and board","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Mechanical pulps prdouced on site ","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce fresh water use, waste water flow, and the pollution load, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Counter-current flow of process water and separation of water systems; (ii) High consistency bleaching.; (iii) Washing stage before the refining of softwood mechanical pulp using chip pre-treatment; (iv) Substitution of NaOH by Ca(OH)2 or Mg(OH)2 as alkali in peroxide bleaching; (v) Fibre and filler recovery and treatment of white water (papermaking); (vi) Optimum design and construction of tanks and chests (papermaking).","kg/ADt",12,20,"Green","Daily",0,0,"Unspecified","Yearly","In the case of highly bleached mechanical pulp (70-100 % of fibre in final paper), emission levels of up to 8 kg/t may occur.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Paper and board","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Mechanical pulps prdouced on site ","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce fresh water use, waste water flow, and the pollution load, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Counter-current flow of process water and separation of water systems; (ii) High consistency bleaching.; (iii) Washing stage before the refining of softwood mechanical pulp using chip pre-treatment; (iv) Substitution of NaOH by Ca(OH)2 or Mg(OH)2 as alkali in peroxide bleaching; (v) Fibre and filler recovery and treatment of white water (papermaking); (vi) Optimum design and construction of tanks and chests (papermaking).","kg/ADt",12,20,"Green","Daily",0,0,"Unspecified","Yearly","In the case of highly bleached mechanical pulp (70-100 % of fibre in final paper), emission levels of up to 8 kg/t may occur."]
["Pulp and paper","6. Other activities","Paper and board from recycled fibres pulp produced with deinking on site ","Tissue Paper","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.","kg/t",0.9,4,"Green","Daily",0,0,"Unspecified","Yearly",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Paper and board from recycled fibres pulp produced with deinking on site ","Tissue Paper","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.","kg/t",0.9,4,"Green","Daily",0,0,"Unspecified","Yearly",0]
["Pulp and paper","6. Other activities","Paper and board from recycled fibres pulp produced with deinking on site ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.","kg/t",0.9,3,"Green","Daily",0,0,"Unspecified","Yearly",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Paper and board from recycled fibres pulp produced with deinking on site ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.","kg/t",0.9,3,"Green","Daily",0,0,"Unspecified","Yearly",0]
["Pulp and paper","6. Other activities","Paper and board from recycled fibres pulp produced without deinking on site ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.","kg/t",0.4,1.4,"Green","Daily",0,0,"Unspecified","Yearly",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Paper and board from recycled fibres pulp produced without deinking on site ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.","kg/t",0.4,1.4,"Green","Daily",0,0,"Unspecified","Yearly",0]
["Pulp and paper","6. Other activities","Unbleached fraft pulp mill","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions of pollutants into receiving waters from the whole mill, BAT is to use TCF or modern ECF bleaching (see description in Section 1.7.2.1), and a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Modified cooking before bleaching; (ii) Oxygen delignification before bleaching; (iii) Closed brown stock screening and efficient brown stock washing; (iv) Partial process water recycling in the bleach plant; (v) Effective spill monitoring and containment with a suitable recovery system; (vi) Maintaining sufficient black liquor evaporation and recovery boiler capacity to cope with peak loads; (vii) Stripping the contaminated (foul) condensates and reusing the condensates in the process","kg/ADt",2.5,8,"Green","Daily",0,0,"Unspecified","Yearly","The BAT-AEL ranges refer to market pulp production and the pulp production part of integrated mills (emissions from papermaking are not included).",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Unbleached fraft pulp mill","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions of pollutants into receiving waters from the whole mill, BAT is to use TCF or modern ECF bleaching (see description in Section 1.7.2.1), and a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Modified cooking before bleaching; (ii) Oxygen delignification before bleaching; (iii) Closed brown stock screening and efficient brown stock washing; (iv) Partial process water recycling in the bleach plant; (v) Effective spill monitoring and containment with a suitable recovery system; (vi) Maintaining sufficient black liquor evaporation and recovery boiler capacity to cope with peak loads; (vii) Stripping the contaminated (foul) condensates and reusing the condensates in the process","kg/ADt",2.5,8,"Green","Daily",0,0,"Unspecified","Yearly","The BAT-AEL ranges refer to market pulp production and the pulp production part of integrated mills (emissions from papermaking are not included)."]
["Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","CTMP or CMP pulp mill","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce fresh water use, waste water flow, and the pollution load, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Counter-current flow of process water and separation of water systems; (ii) High consistency bleaching.; (iii) Washing stage before the refining of softwood mechanical pulp using chip pre-treatment; (iv) Substitution of NaOH by Ca(OH)2 or Mg(OH)2 as alkali in peroxide bleaching; (v) Fibre and filler recovery and treatment of white water (papermaking); (vi) Optimum design and construction of tanks and chests (papermaking).","kg/ADt",12,20,"Green","Daily",0,0,"Unspecified","Yearly",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","CTMP or CMP pulp mill","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce fresh water use, waste water flow, and the pollution load, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Counter-current flow of process water and separation of water systems; (ii) High consistency bleaching.; (iii) Washing stage before the refining of softwood mechanical pulp using chip pre-treatment; (iv) Substitution of NaOH by Ca(OH)2 or Mg(OH)2 as alkali in peroxide bleaching; (v) Fibre and filler recovery and treatment of white water (papermaking); (vi) Optimum design and construction of tanks and chests (papermaking).","kg/ADt",12,20,"Green","Daily",0,0,"Unspecified","Yearly",0]
["Pulp and paper","6. Other activities","Bleached sulphite paper grade pulp   ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Pulp mill","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce emissions of pollutants into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Extended modified cooking before bleaching.; (ii) Oxygen delignification before bleaching; (iii) Closed brown stock screening and efficient brown stock washing.; (iv) Evaporation of effluents from the hot alkaline extraction stage and incineration of concentrates in a soda boiler; (v) TCF bleaching; (vi) Closed-loop bleaching; (vii) MgO-based pre-bleaching and recirculation of washing liquids from pre- bleaching to brown stock washing; (viii) pH adjustment of weak liquor before/ inside the evaporation plant; (ix) Anaerobic treatment of the condensates from the evaporators; (x) Stripping and recovery of SO2 from the condensates of evaporators; (xi) Effective spill monitoring and containment, also with chemical and energy recovery system","kg/ADt",0.15,3,"Green","Weekly",0,0,"Unspecified","Yearly","The BAT-AEL ranges refer to market pulp production and the pulp production part of integrated mills (emissions from papermaking are not included).\n\nThe BAT-AELs do not apply to natural greaseproof pulp mills).",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Bleached sulphite paper grade pulp   ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Pulp mill","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce emissions of pollutants into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Extended modified cooking before bleaching.; (ii) Oxygen delignification before bleaching; (iii) Closed brown stock screening and efficient brown stock washing.; (iv) Evaporation of effluents from the hot alkaline extraction stage and incineration of concentrates in a soda boiler; (v) TCF bleaching; (vi) Closed-loop bleaching; (vii) MgO-based pre-bleaching and recirculation of washing liquids from pre- bleaching to brown stock washing; (viii) pH adjustment of weak liquor before/ inside the evaporation plant; (ix) Anaerobic treatment of the condensates from the evaporators; (x) Stripping and recovery of SO2 from the condensates of evaporators; (xi) Effective spill monitoring and containment, also with chemical and energy recovery system","kg/ADt",0.15,3,"Green","Weekly",0,0,"Unspecified","Yearly","The BAT-AEL ranges refer to market pulp production and the pulp production part of integrated mills (emissions from papermaking are not included).\n\nThe BAT-AELs do not apply to natural greaseproof pulp mills)."]
["Pulp and paper","6. Other activities","Magnefite paper grade pulp","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Pulp mill","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce emissions of pollutants into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Extended modified cooking before bleaching.; (ii) Oxygen delignification before bleaching; (iii) Closed brown stock screening and efficient brown stock washing.; (iv) Evaporation of effluents from the hot alkaline extraction stage and incineration of concentrates in a soda boiler; (v) TCF bleaching; (vi) Closed-loop bleaching; (vii) MgO-based pre-bleaching and recirculation of washing liquids from pre- bleaching to brown stock washing; (viii) pH adjustment of weak liquor before/ inside the evaporation plant; (ix) Anaerobic treatment of the condensates from the evaporators; (x) Stripping and recovery of SO2 from the condensates of evaporators; (xi) Effective spill monitoring and containment, also with chemical and energy recovery system","kg/ADt",0.1,0.25,"Green","Weekly",0,0,"Unspecified","Yearly","The BAT-AEL ranges refer to market pulp production and the pulp production part of integrated mills (emissions from papermaking are not included).",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Magnefite paper grade pulp","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Pulp mill","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce emissions of pollutants into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Extended modified cooking before bleaching.; (ii) Oxygen delignification before bleaching; (iii) Closed brown stock screening and efficient brown stock washing.; (iv) Evaporation of effluents from the hot alkaline extraction stage and incineration of concentrates in a soda boiler; (v) TCF bleaching; (vi) Closed-loop bleaching; (vii) MgO-based pre-bleaching and recirculation of washing liquids from pre- bleaching to brown stock washing; (viii) pH adjustment of weak liquor before/ inside the evaporation plant; (ix) Anaerobic treatment of the condensates from the evaporators; (x) Stripping and recovery of SO2 from the condensates of evaporators; (xi) Effective spill monitoring and containment, also with chemical and energy recovery system","kg/ADt",0.1,0.25,"Green","Weekly",0,0,"Unspecified","Yearly","The BAT-AEL ranges refer to market pulp production and the pulp production part of integrated mills (emissions from papermaking are not included)."]
["Pulp and paper","6. Other activities","Bleached kraft pulp mill","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions of pollutants into receiving waters from the whole mill, BAT is to use TCF or modern ECF bleaching (see description in Section 1.7.2.1), and a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Modified cooking before bleaching; (ii) Oxygen delignification before bleaching; (iii) Closed brown stock screening and efficient brown stock washing; (iv) Partial process water recycling in the bleach plant; (v) Effective spill monitoring and containment with a suitable recovery system; (vi) Maintaining sufficient black liquor evaporation and recovery boiler capacity to cope with peak loads; (vii) Stripping the contaminated (foul) condensates and reusing the condensates in the process","kg/Adt",0.05,0.25,"Green","Weekly",0,0,"Unspecified","Yearly","The BAT-AEL ranges refer to market pulp production and the pulp production part of integrated mills (emissions from papermaking are not included).\n\nA compact biological waste water treatment plant can result in slightly higher emission levels.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Bleached kraft pulp mill","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions of pollutants into receiving waters from the whole mill, BAT is to use TCF or modern ECF bleaching (see description in Section 1.7.2.1), and a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Modified cooking before bleaching; (ii) Oxygen delignification before bleaching; (iii) Closed brown stock screening and efficient brown stock washing; (iv) Partial process water recycling in the bleach plant; (v) Effective spill monitoring and containment with a suitable recovery system; (vi) Maintaining sufficient black liquor evaporation and recovery boiler capacity to cope with peak loads; (vii) Stripping the contaminated (foul) condensates and reusing the condensates in the process","kg/Adt",0.05,0.25,"Green","Weekly",0,0,"Unspecified","Yearly","The BAT-AEL ranges refer to market pulp production and the pulp production part of integrated mills (emissions from papermaking are not included).\n\nA compact biological waste water treatment plant can result in slightly higher emission levels."]
["Pulp and paper","6. Other activities","Excluding speciality paper ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.","kg/t",0.01,0.1,"Green","Weekly",0,0,"Unspecified","Yearly",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Excluding speciality paper ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.","kg/t",0.01,0.1,"Green","Weekly",0,0,"Unspecified","Yearly",0]
["Pulp and paper","6. Other activities","Excluding speciality paper ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Non-integrated speciality paper mill ","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.","kg/t",1.4999999999999999E-2,0.4,"Green","Weekly",0,0,"Unspecified","Yearly",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Excluding speciality paper ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Non-integrated speciality paper mill ","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.","kg/t",1.4999999999999999E-2,0.4,"Green","Weekly",0,0,"Unspecified","Yearly",0]
["Pulp and paper","6. Other activities","NSSC pulp","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Sulphite pulp mill","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce emissions of pollutants into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Extended modified cooking before bleaching.; (ii) Oxygen delignification before bleaching; (iii) Closed brown stock screening and efficient brown stock washing.; (iv) Evaporation of effluents from the hot alkaline extraction stage and incineration of concentrates in a soda boiler; (v) TCF bleaching; (vi) Closed-loop bleaching; (vii) MgO-based pre-bleaching and recirculation of washing liquids from pre- bleaching to brown stock washing; (viii) pH adjustment of weak liquor before/ inside the evaporation plant; (ix) Anaerobic treatment of the condensates from the evaporators; (x) Stripping and recovery of SO2 from the condensates of evaporators; (xi) Effective spill monitoring and containment, also with chemical and energy recovery system","kg/ADt",0.1,0.2,"Green","Weekly",0,0,"Unspecified","Yearly","The BAT-AEL ranges refer to market pulp production and the pulp production part of integrated mills (emissions from papermaking are not included).\n\nDue to process-specific higher emissions, the BAT-AEL for total nitrogen does not apply to ammonium-based NSSC pulping.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","NSSC pulp","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Sulphite pulp mill","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce emissions of pollutants into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Extended modified cooking before bleaching.; (ii) Oxygen delignification before bleaching; (iii) Closed brown stock screening and efficient brown stock washing.; (iv) Evaporation of effluents from the hot alkaline extraction stage and incineration of concentrates in a soda boiler; (v) TCF bleaching; (vi) Closed-loop bleaching; (vii) MgO-based pre-bleaching and recirculation of washing liquids from pre- bleaching to brown stock washing; (viii) pH adjustment of weak liquor before/ inside the evaporation plant; (ix) Anaerobic treatment of the condensates from the evaporators; (x) Stripping and recovery of SO2 from the condensates of evaporators; (xi) Effective spill monitoring and containment, also with chemical and energy recovery system","kg/ADt",0.1,0.2,"Green","Weekly",0,0,"Unspecified","Yearly","The BAT-AEL ranges refer to market pulp production and the pulp production part of integrated mills (emissions from papermaking are not included).\n\nDue to process-specific higher emissions, the BAT-AEL for total nitrogen does not apply to ammonium-based NSSC pulping."]
["Pulp and paper","6. Other activities","Paper and board","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Mechanical pulps prdouced on site ","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce fresh water use, waste water flow, and the pollution load, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Counter-current flow of process water and separation of water systems; (ii) High consistency bleaching.; (iii) Washing stage before the refining of softwood mechanical pulp using chip pre-treatment; (iv) Substitution of NaOH by Ca(OH)2 or Mg(OH)2 as alkali in peroxide bleaching; (v) Fibre and filler recovery and treatment of white water (papermaking); (vi) Optimum design and construction of tanks and chests (papermaking).","kg/ADt",0.15,0.18,"Green","Weekly",0,0,"Unspecified","Yearly","When biodegradable or eliminable chelating agents cannot be used due to pulp quality requirements (e.g. high brightness), the emissions of total nitrogen might be higher than this BAT-AEL and should be assessed on a case-by-case basis.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Paper and board","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Mechanical pulps prdouced on site ","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce fresh water use, waste water flow, and the pollution load, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Counter-current flow of process water and separation of water systems; (ii) High consistency bleaching.; (iii) Washing stage before the refining of softwood mechanical pulp using chip pre-treatment; (iv) Substitution of NaOH by Ca(OH)2 or Mg(OH)2 as alkali in peroxide bleaching; (v) Fibre and filler recovery and treatment of white water (papermaking); (vi) Optimum design and construction of tanks and chests (papermaking).","kg/ADt",0.15,0.18,"Green","Weekly",0,0,"Unspecified","Yearly","When biodegradable or eliminable chelating agents cannot be used due to pulp quality requirements (e.g. high brightness), the emissions of total nitrogen might be higher than this BAT-AEL and should be assessed on a case-by-case basis."]
["Pulp and paper","6. Other activities","Paper and board from recycled fibres pulp produced with deinking on site ","Tissue Paper","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.","kg/t",0.01,0.15,"Green","Weekly",0,0,"Unspecified","Yearly",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Paper and board from recycled fibres pulp produced with deinking on site ","Tissue Paper","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.","kg/t",0.01,0.15,"Green","Weekly",0,0,"Unspecified","Yearly",0]
["Pulp and paper","6. Other activities","Paper and board from recycled fibres pulp produced with deinking on site ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.","kg/t",0.01,0.1,"Green","Weekly",0,0,"Unspecified","Yearly",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Paper and board from recycled fibres pulp produced with deinking on site ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.","kg/t",0.01,0.1,"Green","Weekly",0,0,"Unspecified","Yearly",0]
["Pulp and paper","6. Other activities","Paper and board from recycled fibres pulp produced without deinking on site ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.","kg/t",8.0000000000000002E-3,0.09,"Green","Weekly",0,0,"Unspecified","Yearly",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Paper and board from recycled fibres pulp produced without deinking on site ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.","kg/t",8.0000000000000002E-3,0.09,"Green","Weekly",0,0,"Unspecified","Yearly",0]
["Pulp and paper","6. Other activities","Tissue paper (excluding speciality paper)","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.",0,0.01,0.15,"Green","Weekly",0,0,"Unspecified","Yearly",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Tissue paper (excluding speciality paper)","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.",0,0.01,0.15,"Green","Weekly",0,0,"Unspecified","Yearly",0]
["Pulp and paper","6. Other activities","Unbleached fraft pulp mill","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions of pollutants into receiving waters from the whole mill, BAT is to use TCF or modern ECF bleaching (see description in Section 1.7.2.1), and a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Modified cooking before bleaching; (ii) Oxygen delignification before bleaching; (iii) Closed brown stock screening and efficient brown stock washing; (iv) Partial process water recycling in the bleach plant; (v) Effective spill monitoring and containment with a suitable recovery system; (vi) Maintaining sufficient black liquor evaporation and recovery boiler capacity to cope with peak loads; (vii) Stripping the contaminated (foul) condensates and reusing the condensates in the process","kg/ADt",0.1,0.2,"Green","Weekly",0,0,"Unspecified","Yearly","The BAT-AEL ranges refer to market pulp production and the pulp production part of integrated mills (emissions from papermaking are not included).\n\nA compact biological waste water treatment plant can result in slightly higher emission levels.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Unbleached fraft pulp mill","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions of pollutants into receiving waters from the whole mill, BAT is to use TCF or modern ECF bleaching (see description in Section 1.7.2.1), and a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Modified cooking before bleaching; (ii) Oxygen delignification before bleaching; (iii) Closed brown stock screening and efficient brown stock washing; (iv) Partial process water recycling in the bleach plant; (v) Effective spill monitoring and containment with a suitable recovery system; (vi) Maintaining sufficient black liquor evaporation and recovery boiler capacity to cope with peak loads; (vii) Stripping the contaminated (foul) condensates and reusing the condensates in the process","kg/ADt",0.1,0.2,"Green","Weekly",0,0,"Unspecified","Yearly","The BAT-AEL ranges refer to market pulp production and the pulp production part of integrated mills (emissions from papermaking are not included).\n\nA compact biological waste water treatment plant can result in slightly higher emission levels."]
["Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","CTMP or CMP pulp mill","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce fresh water use, waste water flow, and the pollution load, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Counter-current flow of process water and separation of water systems; (ii) High consistency bleaching.; (iii) Washing stage before the refining of softwood mechanical pulp using chip pre-treatment; (iv) Substitution of NaOH by Ca(OH)2 or Mg(OH)2 as alkali in peroxide bleaching; (v) Fibre and filler recovery and treatment of white water (papermaking); (vi) Optimum design and construction of tanks and chests (papermaking).","kg/ADt",0.15,0.18,"Green","Weekly",0,0,"Unspecified","Yearly","When biodegradable or eliminable chelating agents cannot be used due to pulp quality requirements (e.g. high brightness), the emissions of total nitrogen might be higher than this BAT- AEL and should be assessed on a case-by-case basis.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","CTMP or CMP pulp mill","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce fresh water use, waste water flow, and the pollution load, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Counter-current flow of process water and separation of water systems; (ii) High consistency bleaching.; (iii) Washing stage before the refining of softwood mechanical pulp using chip pre-treatment; (iv) Substitution of NaOH by Ca(OH)2 or Mg(OH)2 as alkali in peroxide bleaching; (v) Fibre and filler recovery and treatment of white water (papermaking); (vi) Optimum design and construction of tanks and chests (papermaking).","kg/ADt",0.15,0.18,"Green","Weekly",0,0,"Unspecified","Yearly","When biodegradable or eliminable chelating agents cannot be used due to pulp quality requirements (e.g. high brightness), the emissions of total nitrogen might be higher than this BAT- AEL and should be assessed on a case-by-case basis."]
["Pulp and paper","6. Other activities","Bleached kraft pulp mill","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions of pollutants into receiving waters from the whole mill, BAT is to use TCF or modern ECF bleaching (see description in Section 1.7.2.1), and a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Modified cooking before bleaching; (ii) Oxygen delignification before bleaching; (iii) Closed brown stock screening and efficient brown stock washing; (iv) Partial process water recycling in the bleach plant; (v) Effective spill monitoring and containment with a suitable recovery system; (vi) Maintaining sufficient black liquor evaporation and recovery boiler capacity to cope with peak loads; (vii) Stripping the contaminated (foul) condensates and reusing the condensates in the process","kg/Adt","0.01\n","0.03\n","Green","Weekly",0,0,"Unspecified","Yearly","The BAT-AEL ranges refer to market pulp production and the pulp production part of integrated mills (emissions from papermaking are not included).\n\nA compact biological waste water treatment plant can result in slightly higher emission levels.\n\nThe upper end of the range refers to mills using eucalyptus from regions with higher levels of phosphorus (e.g. Iberian eucalyptus).",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Bleached kraft pulp mill","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions of pollutants into receiving waters from the whole mill, BAT is to use TCF or modern ECF bleaching (see description in Section 1.7.2.1), and a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Modified cooking before bleaching; (ii) Oxygen delignification before bleaching; (iii) Closed brown stock screening and efficient brown stock washing; (iv) Partial process water recycling in the bleach plant; (v) Effective spill monitoring and containment with a suitable recovery system; (vi) Maintaining sufficient black liquor evaporation and recovery boiler capacity to cope with peak loads; (vii) Stripping the contaminated (foul) condensates and reusing the condensates in the process","kg/Adt","0.01\n","0.03\n","Green","Weekly",0,0,"Unspecified","Yearly","The BAT-AEL ranges refer to market pulp production and the pulp production part of integrated mills (emissions from papermaking are not included).\n\nA compact biological waste water treatment plant can result in slightly higher emission levels.\n\nThe upper end of the range refers to mills using eucalyptus from regions with higher levels of phosphorus (e.g. Iberian eucalyptus)."]
["Pulp and paper","6. Other activities","Bleached kraft pulp mill","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions of pollutants into receiving waters from the whole mill, BAT is to use TCF or modern ECF bleaching (see description in Section 1.7.2.1), and a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Modified cooking before bleaching; (ii) Oxygen delignification before bleaching; (iii) Closed brown stock screening and efficient brown stock washing; (iv) Partial process water recycling in the bleach plant; (v) Effective spill monitoring and containment with a suitable recovery system; (vi) Maintaining sufficient black liquor evaporation and recovery boiler capacity to cope with peak loads; (vii) Stripping the contaminated (foul) condensates and reusing the condensates in the process","kg/Adt",0.02,0.11,"Green","Weekly",0,0,"Unspecified","Yearly"," The BAT-AEL ranges refer to market pulp production and the pulp production part of integrated mills (emissions from\npapermaking are not included).\n\nThe upper end of the range refers to mills using eucalyptus from regions with higher levels of phosphorus (e.g. Iberian\neucalyptus). ",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Bleached kraft pulp mill","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions of pollutants into receiving waters from the whole mill, BAT is to use TCF or modern ECF bleaching (see description in Section 1.7.2.1), and a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Modified cooking before bleaching; (ii) Oxygen delignification before bleaching; (iii) Closed brown stock screening and efficient brown stock washing; (iv) Partial process water recycling in the bleach plant; (v) Effective spill monitoring and containment with a suitable recovery system; (vi) Maintaining sufficient black liquor evaporation and recovery boiler capacity to cope with peak loads; (vii) Stripping the contaminated (foul) condensates and reusing the condensates in the process","kg/Adt",0.02,0.11,"Green","Weekly",0,0,"Unspecified","Yearly"," The BAT-AEL ranges refer to market pulp production and the pulp production part of integrated mills (emissions from\npapermaking are not included).\n\nThe upper end of the range refers to mills using eucalyptus from regions with higher levels of phosphorus (e.g. Iberian\neucalyptus). "]
["Pulp and paper","6. Other activities","Bleached sulphite paper grade pulp   ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Pulp mill","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce emissions of pollutants into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Extended modified cooking before bleaching.; (ii) Oxygen delignification before bleaching; (iii) Closed brown stock screening and efficient brown stock washing.; (iv) Evaporation of effluents from the hot alkaline extraction stage and incineration of concentrates in a soda boiler; (v) TCF bleaching; (vi) Closed-loop bleaching; (vii) MgO-based pre-bleaching and recirculation of washing liquids from pre- bleaching to brown stock washing; (viii) pH adjustment of weak liquor before/ inside the evaporation plant; (ix) Anaerobic treatment of the condensates from the evaporators; (x) Stripping and recovery of SO2 from the condensates of evaporators; (xi) Effective spill monitoring and containment, also with chemical and energy recovery system","kg/ADt",0.01,0.05,"Green","Weekly",0,0,"Unspecified","Yearly","The BAT-AEL ranges refer to market pulp production and the pulp production part of integrated mills (emissions from papermaking are not included).\n\nThe BAT-AELs do not apply to natural greaseproof pulp mills).\n\nThe BAT-AEL for COD and total phosphorus do not apply to eucalyptus based market pulp",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Bleached sulphite paper grade pulp   ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Pulp mill","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce emissions of pollutants into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Extended modified cooking before bleaching.; (ii) Oxygen delignification before bleaching; (iii) Closed brown stock screening and efficient brown stock washing.; (iv) Evaporation of effluents from the hot alkaline extraction stage and incineration of concentrates in a soda boiler; (v) TCF bleaching; (vi) Closed-loop bleaching; (vii) MgO-based pre-bleaching and recirculation of washing liquids from pre- bleaching to brown stock washing; (viii) pH adjustment of weak liquor before/ inside the evaporation plant; (ix) Anaerobic treatment of the condensates from the evaporators; (x) Stripping and recovery of SO2 from the condensates of evaporators; (xi) Effective spill monitoring and containment, also with chemical and energy recovery system","kg/ADt",0.01,0.05,"Green","Weekly",0,0,"Unspecified","Yearly","The BAT-AEL ranges refer to market pulp production and the pulp production part of integrated mills (emissions from papermaking are not included).\n\nThe BAT-AELs do not apply to natural greaseproof pulp mills).\n\nThe BAT-AEL for COD and total phosphorus do not apply to eucalyptus based market pulp"]
["Pulp and paper","6. Other activities","Excluding speciality paper ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.","kg/t",3.0000000000000001E-3,1.2E-2,"Green","Weekly",0,0,"Unspecified","Yearly",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Excluding speciality paper ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.","kg/t",3.0000000000000001E-3,1.2E-2,"Green","Weekly",0,0,"Unspecified","Yearly",0]
["Pulp and paper","6. Other activities","Excluding speciality paper ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Non-integrated speciality paper mill ","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.","kg/t",2E-3,0.04,"Green","Weekly",0,0,"Unspecified","Yearly",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Excluding speciality paper ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Non-integrated speciality paper mill ","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.","kg/t",2E-3,0.04,"Green","Weekly",0,0,"Unspecified","Yearly",0]
["Pulp and paper","6. Other activities","Magnefite paper grade pulp","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Pulp mill","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce emissions of pollutants into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Extended modified cooking before bleaching.; (ii) Oxygen delignification before bleaching; (iii) Closed brown stock screening and efficient brown stock washing.; (iv) Evaporation of effluents from the hot alkaline extraction stage and incineration of concentrates in a soda boiler; (v) TCF bleaching; (vi) Closed-loop bleaching; (vii) MgO-based pre-bleaching and recirculation of washing liquids from pre- bleaching to brown stock washing; (viii) pH adjustment of weak liquor before/ inside the evaporation plant; (ix) Anaerobic treatment of the condensates from the evaporators; (x) Stripping and recovery of SO2 from the condensates of evaporators; (xi) Effective spill monitoring and containment, also with chemical and energy recovery system","kg/ADt",0.01,7.0000000000000007E-2,"Green","Weekly",0,0,"Unspecified","Yearly","The BAT-AEL ranges refer to market pulp production and the pulp production part of integrated mills (emissions from papermaking are not included).",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Magnefite paper grade pulp","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Pulp mill","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce emissions of pollutants into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Extended modified cooking before bleaching.; (ii) Oxygen delignification before bleaching; (iii) Closed brown stock screening and efficient brown stock washing.; (iv) Evaporation of effluents from the hot alkaline extraction stage and incineration of concentrates in a soda boiler; (v) TCF bleaching; (vi) Closed-loop bleaching; (vii) MgO-based pre-bleaching and recirculation of washing liquids from pre- bleaching to brown stock washing; (viii) pH adjustment of weak liquor before/ inside the evaporation plant; (ix) Anaerobic treatment of the condensates from the evaporators; (x) Stripping and recovery of SO2 from the condensates of evaporators; (xi) Effective spill monitoring and containment, also with chemical and energy recovery system","kg/ADt",0.01,7.0000000000000007E-2,"Green","Weekly",0,0,"Unspecified","Yearly","The BAT-AEL ranges refer to market pulp production and the pulp production part of integrated mills (emissions from papermaking are not included)."]
["Pulp and paper","6. Other activities","NSSC pulp","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Sulphite pulp mill","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce emissions of pollutants into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Extended modified cooking before bleaching.; (ii) Oxygen delignification before bleaching; (iii) Closed brown stock screening and efficient brown stock washing.; (iv) Evaporation of effluents from the hot alkaline extraction stage and incineration of concentrates in a soda boiler; (v) TCF bleaching; (vi) Closed-loop bleaching; (vii) MgO-based pre-bleaching and recirculation of washing liquids from pre- bleaching to brown stock washing; (viii) pH adjustment of weak liquor before/ inside the evaporation plant; (ix) Anaerobic treatment of the condensates from the evaporators; (x) Stripping and recovery of SO2 from the condensates of evaporators; (xi) Effective spill monitoring and containment, also with chemical and energy recovery system","kg/ADt",0.01,0.02,"Green","Weekly",0,0,"Unspecified","Yearly","The BAT-AEL ranges refer to market pulp production and the pulp production part of integrated mills (emissions from papermaking are not included).",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","NSSC pulp","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Sulphite pulp mill","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce emissions of pollutants into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Extended modified cooking before bleaching.; (ii) Oxygen delignification before bleaching; (iii) Closed brown stock screening and efficient brown stock washing.; (iv) Evaporation of effluents from the hot alkaline extraction stage and incineration of concentrates in a soda boiler; (v) TCF bleaching; (vi) Closed-loop bleaching; (vii) MgO-based pre-bleaching and recirculation of washing liquids from pre- bleaching to brown stock washing; (viii) pH adjustment of weak liquor before/ inside the evaporation plant; (ix) Anaerobic treatment of the condensates from the evaporators; (x) Stripping and recovery of SO2 from the condensates of evaporators; (xi) Effective spill monitoring and containment, also with chemical and energy recovery system","kg/ADt",0.01,0.02,"Green","Weekly",0,0,"Unspecified","Yearly","The BAT-AEL ranges refer to market pulp production and the pulp production part of integrated mills (emissions from papermaking are not included)."]
["Pulp and paper","6. Other activities","Paper and board from mechanical pupls produced on site","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce fresh water use, waste water flow, and the pollution load, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Counter-current flow of process water and separation of water systems; (ii) High consistency bleaching.; (iii) Washing stage before the refining of softwood mechanical pulp using chip pre-treatment; (iv) Substitution of NaOH by Ca(OH)2 or Mg(OH)2 as alkali in peroxide bleaching; (v) Fibre and filler recovery and treatment of white water (papermaking); (vi) Optimum design and construction of tanks and chests (papermaking).","kg/ADt",1E-3,0.01,"Green","Weekly",0,0,"Unspecified","Yearly",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Paper and board from mechanical pupls produced on site","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce fresh water use, waste water flow, and the pollution load, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Counter-current flow of process water and separation of water systems; (ii) High consistency bleaching.; (iii) Washing stage before the refining of softwood mechanical pulp using chip pre-treatment; (iv) Substitution of NaOH by Ca(OH)2 or Mg(OH)2 as alkali in peroxide bleaching; (v) Fibre and filler recovery and treatment of white water (papermaking); (vi) Optimum design and construction of tanks and chests (papermaking).","kg/ADt",1E-3,0.01,"Green","Weekly",0,0,"Unspecified","Yearly",0]
["Pulp and paper","6. Other activities","Paper and board from recycled fibres pulp produced with deinking on site ","Tissue Paper","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.","kg/t",2E-3,1.4999999999999999E-2,"Green","Weekly",0,0,"Unspecified","Yearly",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Paper and board from recycled fibres pulp produced with deinking on site ","Tissue Paper","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.","kg/t",2E-3,1.4999999999999999E-2,"Green","Weekly",0,0,"Unspecified","Yearly",0]
["Pulp and paper","6. Other activities","Paper and board from recycled fibres pulp produced with deinking on site ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.","kg/t",2E-3,0.01,"Green","Weekly",0,0,"Unspecified","Yearly",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Paper and board from recycled fibres pulp produced with deinking on site ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.","kg/t",2E-3,0.01,"Green","Weekly",0,0,"Unspecified","Yearly",0]
["Pulp and paper","6. Other activities","Paper and board from recycled fibres pulp produced without deinking on site ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.","kg/t",1E-3,5.0000000000000001E-3,"Green","Weekly",0,0,"Unspecified","Yearly","For mills with a waste water flow between 5 and 10 m3/t, the upper end of the range is 0,008 kg/t.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Paper and board from recycled fibres pulp produced without deinking on site ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.","kg/t",1E-3,5.0000000000000001E-3,"Green","Weekly",0,0,"Unspecified","Yearly","For mills with a waste water flow between 5 and 10 m3/t, the upper end of the range is 0,008 kg/t."]
["Pulp and paper","6. Other activities","Unbleached fraft pulp mill","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions of pollutants into receiving waters from the whole mill, BAT is to use TCF or modern ECF bleaching (see description in Section 1.7.2.1), and a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Modified cooking before bleaching; (ii) Oxygen delignification before bleaching; (iii) Closed brown stock screening and efficient brown stock washing; (iv) Partial process water recycling in the bleach plant; (v) Effective spill monitoring and containment with a suitable recovery system; (vi) Maintaining sufficient black liquor evaporation and recovery boiler capacity to cope with peak loads; (vii) Stripping the contaminated (foul) condensates and reusing the condensates in the process","kg/ADt",0.01,0.02,"Green","Weekly",0,0,"Unspecified","Yearly","The BAT-AEL ranges refer to market pulp production and the pulp production part of integrated mills (emissions from papermaking are not included).\n\nA compact biological waste water treatment plant can result in slightly higher emission levels.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Unbleached fraft pulp mill","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions of pollutants into receiving waters from the whole mill, BAT is to use TCF or modern ECF bleaching (see description in Section 1.7.2.1), and a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Modified cooking before bleaching; (ii) Oxygen delignification before bleaching; (iii) Closed brown stock screening and efficient brown stock washing; (iv) Partial process water recycling in the bleach plant; (v) Effective spill monitoring and containment with a suitable recovery system; (vi) Maintaining sufficient black liquor evaporation and recovery boiler capacity to cope with peak loads; (vii) Stripping the contaminated (foul) condensates and reusing the condensates in the process","kg/ADt",0.01,0.02,"Green","Weekly",0,0,"Unspecified","Yearly","The BAT-AEL ranges refer to market pulp production and the pulp production part of integrated mills (emissions from papermaking are not included).\n\nA compact biological waste water treatment plant can result in slightly higher emission levels."]
["Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","CTMP or CMP pulp mill","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce fresh water use, waste water flow, and the pollution load, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Counter-current flow of process water and separation of water systems; (ii) High consistency bleaching.; (iii) Washing stage before the refining of softwood mechanical pulp using chip pre-treatment; (iv) Substitution of NaOH by Ca(OH)2 or Mg(OH)2 as alkali in peroxide bleaching; (v) Fibre and filler recovery and treatment of white water (papermaking); (vi) Optimum design and construction of tanks and chests (papermaking).","kg/ADt",1E-3,0.01,"Green","Weekly",0,0,"Unspecified","Yearly",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","CTMP or CMP pulp mill","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce fresh water use, waste water flow, and the pollution load, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Counter-current flow of process water and separation of water systems; (ii) High consistency bleaching.; (iii) Washing stage before the refining of softwood mechanical pulp using chip pre-treatment; (iv) Substitution of NaOH by Ca(OH)2 or Mg(OH)2 as alkali in peroxide bleaching; (v) Fibre and filler recovery and treatment of white water (papermaking); (vi) Optimum design and construction of tanks and chests (papermaking).","kg/ADt",1E-3,0.01,"Green","Weekly",0,0,"Unspecified","Yearly",0]
["Pulp and paper","6. Other activities","Bleached kraft pulp mill","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions of pollutants into receiving waters from the whole mill, BAT is to use TCF or modern ECF bleaching (see description in Section 1.7.2.1), and a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Modified cooking before bleaching; (ii) Oxygen delignification before bleaching; (iii) Closed brown stock screening and efficient brown stock washing; (iv) Partial process water recycling in the bleach plant; (v) Effective spill monitoring and containment with a suitable recovery system; (vi) Maintaining sufficient black liquor evaporation and recovery boiler capacity to cope with peak loads; (vii) Stripping the contaminated (foul) condensates and reusing the condensates in the process","kg/Adt",0.3,1.5,"Green","Daily",0,0,"Unspecified","Yearly","The BAT-AEL ranges refer to market pulp production and the pulp production part of integrated mills (emissions from papermaking are not included).",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Bleached kraft pulp mill","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions of pollutants into receiving waters from the whole mill, BAT is to use TCF or modern ECF bleaching (see description in Section 1.7.2.1), and a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Modified cooking before bleaching; (ii) Oxygen delignification before bleaching; (iii) Closed brown stock screening and efficient brown stock washing; (iv) Partial process water recycling in the bleach plant; (v) Effective spill monitoring and containment with a suitable recovery system; (vi) Maintaining sufficient black liquor evaporation and recovery boiler capacity to cope with peak loads; (vii) Stripping the contaminated (foul) condensates and reusing the condensates in the process","kg/Adt",0.3,1.5,"Green","Daily",0,0,"Unspecified","Yearly","The BAT-AEL ranges refer to market pulp production and the pulp production part of integrated mills (emissions from papermaking are not included)."]
["Pulp and paper","6. Other activities","Bleached sulphite paper grade pulp   ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Pulp mill","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce emissions of pollutants into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Extended modified cooking before bleaching.; (ii) Oxygen delignification before bleaching; (iii) Closed brown stock screening and efficient brown stock washing.; (iv) Evaporation of effluents from the hot alkaline extraction stage and incineration of concentrates in a soda boiler; (v) TCF bleaching; (vi) Closed-loop bleaching; (vii) MgO-based pre-bleaching and recirculation of washing liquids from pre- bleaching to brown stock washing; (viii) pH adjustment of weak liquor before/ inside the evaporation plant; (ix) Anaerobic treatment of the condensates from the evaporators; (x) Stripping and recovery of SO2 from the condensates of evaporators; (xi) Effective spill monitoring and containment, also with chemical and energy recovery system","kg/ADt",0.4,1.5,"Green","Daily",0,0,"Unspecified","Yearly","The BAT-AEL ranges refer to market pulp production and the pulp production part of integrated mills (emissions from papermaking are not included).\n\nThe BAT-AELs do not apply to natural greaseproof pulp mills).",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Bleached sulphite paper grade pulp   ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Pulp mill","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce emissions of pollutants into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Extended modified cooking before bleaching.; (ii) Oxygen delignification before bleaching; (iii) Closed brown stock screening and efficient brown stock washing.; (iv) Evaporation of effluents from the hot alkaline extraction stage and incineration of concentrates in a soda boiler; (v) TCF bleaching; (vi) Closed-loop bleaching; (vii) MgO-based pre-bleaching and recirculation of washing liquids from pre- bleaching to brown stock washing; (viii) pH adjustment of weak liquor before/ inside the evaporation plant; (ix) Anaerobic treatment of the condensates from the evaporators; (x) Stripping and recovery of SO2 from the condensates of evaporators; (xi) Effective spill monitoring and containment, also with chemical and energy recovery system","kg/ADt",0.4,1.5,"Green","Daily",0,0,"Unspecified","Yearly","The BAT-AEL ranges refer to market pulp production and the pulp production part of integrated mills (emissions from papermaking are not included).\n\nThe BAT-AELs do not apply to natural greaseproof pulp mills)."]
["Pulp and paper","6. Other activities","Excluding speciality paper ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.","kg/t",0.02,0.35,"Green","Daily",0,0,"Unspecified","Yearly",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Excluding speciality paper ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.","kg/t",0.02,0.35,"Green","Daily",0,0,"Unspecified","Yearly",0]
["Pulp and paper","6. Other activities","Excluding speciality paper ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Non-integrated speciality paper mill ","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.","kg/t",0.1,1,"Green","Daily",0,0,"Unspecified","Yearly",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Excluding speciality paper ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Non-integrated speciality paper mill ","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.","kg/t",0.1,1,"Green","Daily",0,0,"Unspecified","Yearly",0]
["Pulp and paper","6. Other activities","Magnefite paper grade pulp","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Pulp mill","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce emissions of pollutants into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Extended modified cooking before bleaching.; (ii) Oxygen delignification before bleaching; (iii) Closed brown stock screening and efficient brown stock washing.; (iv) Evaporation of effluents from the hot alkaline extraction stage and incineration of concentrates in a soda boiler; (v) TCF bleaching; (vi) Closed-loop bleaching; (vii) MgO-based pre-bleaching and recirculation of washing liquids from pre- bleaching to brown stock washing; (viii) pH adjustment of weak liquor before/ inside the evaporation plant; (ix) Anaerobic treatment of the condensates from the evaporators; (x) Stripping and recovery of SO2 from the condensates of evaporators; (xi) Effective spill monitoring and containment, also with chemical and energy recovery system","kg/ADt",0.5,2,"Green","Daily",0,0,"Unspecified","Yearly","The BAT-AEL ranges refer to market pulp production and the pulp production part of integrated mills (emissions from papermaking are not included).",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Magnefite paper grade pulp","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Pulp mill","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce emissions of pollutants into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Extended modified cooking before bleaching.; (ii) Oxygen delignification before bleaching; (iii) Closed brown stock screening and efficient brown stock washing.; (iv) Evaporation of effluents from the hot alkaline extraction stage and incineration of concentrates in a soda boiler; (v) TCF bleaching; (vi) Closed-loop bleaching; (vii) MgO-based pre-bleaching and recirculation of washing liquids from pre- bleaching to brown stock washing; (viii) pH adjustment of weak liquor before/ inside the evaporation plant; (ix) Anaerobic treatment of the condensates from the evaporators; (x) Stripping and recovery of SO2 from the condensates of evaporators; (xi) Effective spill monitoring and containment, also with chemical and energy recovery system","kg/ADt",0.5,2,"Green","Daily",0,0,"Unspecified","Yearly","The BAT-AEL ranges refer to market pulp production and the pulp production part of integrated mills (emissions from papermaking are not included)."]
["Pulp and paper","6. Other activities","NSSC pulp","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Sulphite pulp mill","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce emissions of pollutants into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Extended modified cooking before bleaching.; (ii) Oxygen delignification before bleaching; (iii) Closed brown stock screening and efficient brown stock washing.; (iv) Evaporation of effluents from the hot alkaline extraction stage and incineration of concentrates in a soda boiler; (v) TCF bleaching; (vi) Closed-loop bleaching; (vii) MgO-based pre-bleaching and recirculation of washing liquids from pre- bleaching to brown stock washing; (viii) pH adjustment of weak liquor before/ inside the evaporation plant; (ix) Anaerobic treatment of the condensates from the evaporators; (x) Stripping and recovery of SO2 from the condensates of evaporators; (xi) Effective spill monitoring and containment, also with chemical and energy recovery system","kg/ADt",0.5,1.3,"Green","Daily",0,0,"Unspecified","Yearly","The BAT-AEL ranges refer to market pulp production and the pulp production part of integrated mills (emissions from papermaking are not included).",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","NSSC pulp","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Sulphite pulp mill","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce emissions of pollutants into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Extended modified cooking before bleaching.; (ii) Oxygen delignification before bleaching; (iii) Closed brown stock screening and efficient brown stock washing.; (iv) Evaporation of effluents from the hot alkaline extraction stage and incineration of concentrates in a soda boiler; (v) TCF bleaching; (vi) Closed-loop bleaching; (vii) MgO-based pre-bleaching and recirculation of washing liquids from pre- bleaching to brown stock washing; (viii) pH adjustment of weak liquor before/ inside the evaporation plant; (ix) Anaerobic treatment of the condensates from the evaporators; (x) Stripping and recovery of SO2 from the condensates of evaporators; (xi) Effective spill monitoring and containment, also with chemical and energy recovery system","kg/ADt",0.5,1.3,"Green","Daily",0,0,"Unspecified","Yearly","The BAT-AEL ranges refer to market pulp production and the pulp production part of integrated mills (emissions from papermaking are not included)."]
["Pulp and paper","6. Other activities","Paper and board","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Mechanical pulps prdouced on site ","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce fresh water use, waste water flow, and the pollution load, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Counter-current flow of process water and separation of water systems; (ii) High consistency bleaching.; (iii) Washing stage before the refining of softwood mechanical pulp using chip pre-treatment; (iv) Substitution of NaOH by Ca(OH)2 or Mg(OH)2 as alkali in peroxide bleaching; (v) Fibre and filler recovery and treatment of white water (papermaking); (vi) Optimum design and construction of tanks and chests (papermaking).","kg/ADt",0.5,0.9,"Green","Daily",0,0,"Unspecified","Yearly",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Paper and board","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Mechanical pulps prdouced on site ","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce fresh water use, waste water flow, and the pollution load, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Counter-current flow of process water and separation of water systems; (ii) High consistency bleaching.; (iii) Washing stage before the refining of softwood mechanical pulp using chip pre-treatment; (iv) Substitution of NaOH by Ca(OH)2 or Mg(OH)2 as alkali in peroxide bleaching; (v) Fibre and filler recovery and treatment of white water (papermaking); (vi) Optimum design and construction of tanks and chests (papermaking).","kg/ADt",0.5,0.9,"Green","Daily",0,0,"Unspecified","Yearly",0]
["Pulp and paper","6. Other activities","Paper and board from recycled fibres pulp produced with deinking on site ","Tissue Paper","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.","kg/t",0.1,0.4,"Green","Daily",0,0,"Unspecified","Yearly",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Paper and board from recycled fibres pulp produced with deinking on site ","Tissue Paper","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.","kg/t",0.1,0.4,"Green","Daily",0,0,"Unspecified","Yearly",0]
["Pulp and paper","6. Other activities","Paper and board from recycled fibres pulp produced with deinking on site ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.","kg/t",0.08,0.3,"Green","Daily",0,0,"Unspecified","Yearly",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Paper and board from recycled fibres pulp produced with deinking on site ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.","kg/t",0.08,0.3,"Green","Daily",0,0,"Unspecified","Yearly",0]
["Pulp and paper","6. Other activities","Paper and board from recycled fibres pulp produced without deinking on site ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.","kg/t",0.02,0.2,"Green","Daily",0,0,"Unspecified","Yearly","For existing plants, levels up to 0,45 kg/t may occur, due to the continuous decline in the quality of paper for recycling and the difficulty of continuously upgrading the effluent plant.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Paper and board from recycled fibres pulp produced without deinking on site ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce the pollution load of waste water into receiving waters from the whole mill, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15, BAT 16, BAT 43 and BAT 44. For integrated RCF paper mills, the BAT-AELs include emissions from papermaking, since the white water circuits of the paper machine are closely connected with those of the stock preparation.","kg/t",0.02,0.2,"Green","Daily",0,0,"Unspecified","Yearly","For existing plants, levels up to 0,45 kg/t may occur, due to the continuous decline in the quality of paper for recycling and the difficulty of continuously upgrading the effluent plant."]
["Pulp and paper","6. Other activities","Unbleached fraft pulp mill","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions of pollutants into receiving waters from the whole mill, BAT is to use TCF or modern ECF bleaching (see description in Section 1.7.2.1), and a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Modified cooking before bleaching; (ii) Oxygen delignification before bleaching; (iii) Closed brown stock screening and efficient brown stock washing; (iv) Partial process water recycling in the bleach plant; (v) Effective spill monitoring and containment with a suitable recovery system; (vi) Maintaining sufficient black liquor evaporation and recovery boiler capacity to cope with peak loads; (vii) Stripping the contaminated (foul) condensates and reusing the condensates in the process","kg/ADt",0.3,1,"Green","Daily",0,0,"Unspecified","Yearly","The BAT-AEL ranges refer to market pulp production and the pulp production part of integrated mills (emissions from papermaking are not included).",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Unbleached fraft pulp mill","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Direct waste water discharge","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce emissions of pollutants into receiving waters from the whole mill, BAT is to use TCF or modern ECF bleaching (see description in Section 1.7.2.1), and a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Modified cooking before bleaching; (ii) Oxygen delignification before bleaching; (iii) Closed brown stock screening and efficient brown stock washing; (iv) Partial process water recycling in the bleach plant; (v) Effective spill monitoring and containment with a suitable recovery system; (vi) Maintaining sufficient black liquor evaporation and recovery boiler capacity to cope with peak loads; (vii) Stripping the contaminated (foul) condensates and reusing the condensates in the process","kg/ADt",0.3,1,"Green","Daily",0,0,"Unspecified","Yearly","The BAT-AEL ranges refer to market pulp production and the pulp production part of integrated mills (emissions from papermaking are not included)."]
["Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","CTMP or CMP pulp mill","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce fresh water use, waste water flow, and the pollution load, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Counter-current flow of process water and separation of water systems; (ii) High consistency bleaching.; (iii) Washing stage before the refining of softwood mechanical pulp using chip pre-treatment; (iv) Substitution of NaOH by Ca(OH)2 or Mg(OH)2 as alkali in peroxide bleaching; (v) Fibre and filler recovery and treatment of white water (papermaking); (vi) Optimum design and construction of tanks and chests (papermaking).","kg/ADt",0.5,0.9,"Green","Daily",0,0,"Unspecified","Yearly",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","CTMP or CMP pulp mill","Water","Ammonia (ecological receptor - Sensitive Lichens)","In order to reduce fresh water use, waste water flow, and the pollution load, BAT is to use a suitable combination of the techniques specified in BAT 13, BAT 14, BAT 15 and BAT 16 and of the techniques given below: (i) Counter-current flow of process water and separation of water systems; (ii) High consistency bleaching.; (iii) Washing stage before the refining of softwood mechanical pulp using chip pre-treatment; (iv) Substitution of NaOH by Ca(OH)2 or Mg(OH)2 as alkali in peroxide bleaching; (v) Fibre and filler recovery and treatment of white water (papermaking); (vi) Optimum design and construction of tanks and chests (papermaking).","kg/ADt",0.5,0.9,"Green","Daily",0,0,"Unspecified","Yearly",0]
["Refineries","1. Energy industries","Unspecified","Unspecified","All","Unspecified","All","Unspecified","All units equipped with SCR or SNCR","Air","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce ammonia (NH3) emissions to air when applying selective catalytic reduction (SCR) or selective non-catalytic reduction (SNCR) techniques, BAT is to maintain suitable operating conditions of the SCR or SNCR waste gas treatment systems, with the aim of limiting emissions of unreacted NH3.","mg/Nm3",5,15,"Green","Continuous",0,0,0.03,"Monthly average","The higher end of the range is associated with higher inlet NOX concentrations, higher NOX reduction rates and the ageing\nof the catalyst. \n\nThe lower end of the range is associated with the use of the SCR technique. ",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Refineries","1. Energy industries","Unspecified","Unspecified","All","Unspecified","All","Unspecified","All units equipped with SCR or SNCR","Air","Ammonia (ecological receptor - Sensitive Lichens)","In order to prevent and reduce ammonia (NH3) emissions to air when applying selective catalytic reduction (SCR) or selective non-catalytic reduction (SNCR) techniques, BAT is to maintain suitable operating conditions of the SCR or SNCR waste gas treatment systems, with the aim of limiting emissions of unreacted NH3.","mg/Nm3",5,15,"Green","Continuous",0,0,0.03,"Monthly average","The higher end of the range is associated with higher inlet NOX concentrations, higher NOX reduction rates and the ageing\nof the catalyst. \n\nThe lower end of the range is associated with the use of the SCR technique. "]
["Refineries","1. Energy industries","Unspecified","Unspecified","All","Unspecified","All","Unspecified","Loading and unloading operations of volatile liquid hydrocarbon compounds","Air","Benzene","In order to prevent or reduce VOC emissions to air from loading and unloading operations of volatile liquid hydrocarbon compounds, BAT is to use one or a combination of the techniques given below to achieve a recovery rate of at least 95 %:\n\nVapour recovery by:\n(i) Condensation\n(ii) Absorption\n(iii) Adsorption\n(iv) Membrane separation\n(v) Hybrid systems ","mg/Nm3","N/A",1,"Amber",0,0,0,0,"Hourly","Hourly values in continuous operation expressed and measured according to European Parliament and Council Directive 94/63/EC (OJ L 365, 31.12.1994, p. 24).",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Refineries","1. Energy industries","Unspecified","Unspecified","All","Unspecified","All","Unspecified","Loading and unloading operations of volatile liquid hydrocarbon compounds","Air","Benzene","In order to prevent or reduce VOC emissions to air from loading and unloading operations of volatile liquid hydrocarbon compounds, BAT is to use one or a combination of the techniques given below to achieve a recovery rate of at least 95 %:\n\nVapour recovery by:\n(i) Condensation\n(ii) Absorption\n(iii) Adsorption\n(iv) Membrane separation\n(v) Hybrid systems ","mg/Nm3","N/A",1,"Amber",0,0,0,0,"Hourly","Hourly values in continuous operation expressed and measured according to European Parliament and Council Directive 94/63/EC (OJ L 365, 31.12.1994, p. 24)."]
["Refineries","1. Energy industries","Unspecified","Unspecified","All","Unspecified","All","Unspecified","Combustion unit","Air","Carbon monoxide","In order to reduce carbon monoxide (CO) emissions to air from the combustion units, BAT is to use a combustion operation control.","mg/Nm3","N/A",100,"Amber",0,0,0,0.03,"Monthly ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Refineries","1. Energy industries","Unspecified","Unspecified","All","Unspecified","All","Unspecified","Combustion unit","Air","Carbon monoxide","In order to reduce carbon monoxide (CO) emissions to air from the combustion units, BAT is to use a combustion operation control.","mg/Nm3","N/A",100,"Amber",0,0,0,0.03,"Monthly ",0]
["Refineries","1. Energy industries","Unspecified","Unspecified","All","Unspecified","All","Unspecified","Regenerator in the catalytic cracking process- Partical combustion","Air","Carbon monoxide","In order to reduce carbon monoxide (CO) emissions to air from the catalytic cracking process (regenerator), BAT is to use one or a combination of the techniques given below.\n(i) Combustion operation control; (ii) Catalysts with carbon monoxide (CO) oxidation promoters; (iii) Carbon monoxide (CO) boiler ","mg/Nm3","N/A",100,"Green","Continuous",0,0,0.03,"Monthly ","May not be achievable when not operating the CO boiler at full load.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Refineries","1. Energy industries","Unspecified","Unspecified","All","Unspecified","All","Unspecified","Regenerator in the catalytic cracking process- Partical combustion","Air","Carbon monoxide","In order to reduce carbon monoxide (CO) emissions to air from the catalytic cracking process (regenerator), BAT is to use one or a combination of the techniques given below.\n(i) Combustion operation control; (ii) Catalysts with carbon monoxide (CO) oxidation promoters; (iii) Carbon monoxide (CO) boiler ","mg/Nm3","N/A",100,"Green","Continuous",0,0,0.03,"Monthly ","May not be achievable when not operating the CO boiler at full load."]
["Refineries","1. Energy industries","Unspecified","Unspecified","All","Unspecified","All","Unspecified","Unit for calcining of green coke","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust emissions to air from the calcining of green coke process, BAT is to use a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Multistage cyclone\nseparators ","mg/Nm3",10,50,"Amber","Continuous",0,0,0,"Monthly ","The lower end of the range can be achieved with a 4-field ESP\n\nWhen an ESP is not applicable, values of up to 150 mg/Nm3 may occur. ",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Refineries","1. Energy industries","Unspecified","Unspecified","All","Unspecified","All","Unspecified","Unit for calcining of green coke","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust emissions to air from the calcining of green coke process, BAT is to use a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Multistage cyclone\nseparators ","mg/Nm3",10,50,"Amber","Continuous",0,0,0,"Monthly ","The lower end of the range can be achieved with a 4-field ESP\n\nWhen an ESP is not applicable, values of up to 150 mg/Nm3 may occur. "]
["Refineries","1. Energy industries","Unspecified","Unspecified","All","Existing","All","Unspecified","Regenerator in the catalytic cracking process","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metals emissions to air from the catalytic cracking process (regenerator), BAT is to use one or a combination of the techniques given below:\n\nPrimary techniques:\n(i) Use of an attrition-resistant catalyst; (ii) Use of low sulphur feedstock (e.g. by feedstock selection or by hydrotreatment of feed) \n\nSecondary techniqyes:\n(i) Electrostatic precipitator (ESP); (ii) Multistage cyclone separators; (iii) Third stage blowback\nfilter; (iv) Wet scrubbing ","mg/Nm3",10,50,"Green","Continuous",0,0,0.03,"Monthly ","Soot blowing in CO boiler and through the gas cooler is excluded.\n\nThe lower end of the range can be achieved with a 4-field ESP.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Refineries","1. Energy industries","Unspecified","Unspecified","All","Existing","All","Unspecified","Regenerator in the catalytic cracking process","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metals emissions to air from the catalytic cracking process (regenerator), BAT is to use one or a combination of the techniques given below:\n\nPrimary techniques:\n(i) Use of an attrition-resistant catalyst; (ii) Use of low sulphur feedstock (e.g. by feedstock selection or by hydrotreatment of feed) \n\nSecondary techniqyes:\n(i) Electrostatic precipitator (ESP); (ii) Multistage cyclone separators; (iii) Third stage blowback\nfilter; (iv) Wet scrubbing ","mg/Nm3",10,50,"Green","Continuous",0,0,0.03,"Monthly ","Soot blowing in CO boiler and through the gas cooler is excluded.\n\nThe lower end of the range can be achieved with a 4-field ESP."]
["Refineries","1. Energy industries","Unspecified","Unspecified","All","New","All","Unspecified","Regenerator in the catalytic cracking process","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metals emissions to air from the catalytic cracking process (regenerator), BAT is to use one or a combination of the techniques given below:\n\nPrimary techniques:\n(i) Use of an attrition-resistant catalyst; (ii) Use of low sulphur feedstock (e.g. by feedstock selection or by hydrotreatment of feed) \n\nSecondary techniqyes:\n(i) Electrostatic precipitator (ESP); (ii) Multistage cyclone separators; (iii) Third stage blowback\nfilter; (iv) Wet scrubbing ","mg/Nm3",10,25,"Green","Continuous",0,0,0.03,"Monthly ","Soot blowing in CO boiler and through the gas cooler is excluded.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Refineries","1. Energy industries","Unspecified","Unspecified","All","New","All","Unspecified","Regenerator in the catalytic cracking process","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust and metals emissions to air from the catalytic cracking process (regenerator), BAT is to use one or a combination of the techniques given below:\n\nPrimary techniques:\n(i) Use of an attrition-resistant catalyst; (ii) Use of low sulphur feedstock (e.g. by feedstock selection or by hydrotreatment of feed) \n\nSecondary techniqyes:\n(i) Electrostatic precipitator (ESP); (ii) Multistage cyclone separators; (iii) Third stage blowback\nfilter; (iv) Wet scrubbing ","mg/Nm3",10,25,"Green","Continuous",0,0,0.03,"Monthly ","Soot blowing in CO boiler and through the gas cooler is excluded."]
["Refineries","1. Energy industries","Unspecified","Unspecified","All","Existing","All","Unspecified","Multi-fuel fired combustion unit  with the exception\nof gas turbines","Air","Particulates (PM10) (24 hr Mean)","In order to prevent or reduce dust and metal emissions to air from the combustion units, BAT is to use one or a combination of the techniques given below: \n\nPrimary techniques:\n(i) Selection or treatment of fuel; (ii) Combustion modifications\n\nSecondary techniques:\n(i) Electrostatic precipitator (ESP); (ii) Third stage blowback filter; (iii) Wet scrubbing; (iv) Centrifugal washers ","mg/Nm3",5,50,"Amber",0,0,0,0.03,"Monthly ","The lower end of the range is achievable for units with the use of end-of-pipe techniques. \n\nThe upper end of the range refers to the use of a high percentage of oil burning and where only primary techniques are\napplicable.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Refineries","1. Energy industries","Unspecified","Unspecified","All","Existing","All","Unspecified","Multi-fuel fired combustion unit  with the exception\nof gas turbines","Air","Particulates (PM10) (24 hr Mean)","In order to prevent or reduce dust and metal emissions to air from the combustion units, BAT is to use one or a combination of the techniques given below: \n\nPrimary techniques:\n(i) Selection or treatment of fuel; (ii) Combustion modifications\n\nSecondary techniques:\n(i) Electrostatic precipitator (ESP); (ii) Third stage blowback filter; (iii) Wet scrubbing; (iv) Centrifugal washers ","mg/Nm3",5,50,"Amber",0,0,0,0.03,"Monthly ","The lower end of the range is achievable for units with the use of end-of-pipe techniques. \n\nThe upper end of the range refers to the use of a high percentage of oil burning and where only primary techniques are\napplicable."]
["Refineries","1. Energy industries","Unspecified","Unspecified","All","New","All","<50 MW","Multi-fuel fired combustion unit  with the exception\nof gas turbines","Air","Particulates (PM10) (24 hr Mean)","In order to prevent or reduce dust and metal emissions to air from the combustion units, BAT is to use one or a combination of the techniques given below: \n\nPrimary techniques:\n(i) Selection or treatment of fuel; (ii) Combustion modifications\n\nSecondary techniques:\n(i) Electrostatic precipitator (ESP); (ii) Third stage blowback filter; (iii) Wet scrubbing; (iv) Centrifugal washers ","mg/Nm3",5,25,"Green","Once a year and after significant fuel changes",0,0,0.03,"Monthly ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Refineries","1. Energy industries","Unspecified","Unspecified","All","New","All","<50 MW","Multi-fuel fired combustion unit  with the exception\nof gas turbines","Air","Particulates (PM10) (24 hr Mean)","In order to prevent or reduce dust and metal emissions to air from the combustion units, BAT is to use one or a combination of the techniques given below: \n\nPrimary techniques:\n(i) Selection or treatment of fuel; (ii) Combustion modifications\n\nSecondary techniques:\n(i) Electrostatic precipitator (ESP); (ii) Third stage blowback filter; (iii) Wet scrubbing; (iv) Centrifugal washers ","mg/Nm3",5,25,"Green","Once a year and after significant fuel changes",0,0,0.03,"Monthly ",0]
["Refineries","1. Energy industries","Unspecified","Unspecified","All","Unspecified","All","Unspecified","Loading and unloading operations of volatile liquid hydrocarbon compounds","Air","NMVOC","In order to prevent or reduce VOC emissions to air from loading and unloading operations of volatile liquid hydrocarbon compounds, BAT is to use one or a combination of the techniques given below to achieve a recovery rate of at least 95 %:\n\nVapour recovery by:\n(i) Condensation\n(ii) Absorption\n(iii) Adsorption\n(iv) Membrane separation\n(v) Hybrid systems ","g/Nm3",0.15,10,"Amber",0,0,0,0,"Hourly","Hourly values in continuousx operation expressed and measured according to European Parliament and Council Directive 94/63/EC (OJ L 365, 31.12.1994, p. 24).\n\nLower value achievable with two-stage hybrid systems. Upper value achievable with single-stage adsorption or membrane\nsystem. \n\nBenzene monitoring may not be necessary where emissions of NMVOC are at the lower end of the range",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Refineries","1. Energy industries","Unspecified","Unspecified","All","Unspecified","All","Unspecified","Loading and unloading operations of volatile liquid hydrocarbon compounds","Air","NMVOC","In order to prevent or reduce VOC emissions to air from loading and unloading operations of volatile liquid hydrocarbon compounds, BAT is to use one or a combination of the techniques given below to achieve a recovery rate of at least 95 %:\n\nVapour recovery by:\n(i) Condensation\n(ii) Absorption\n(iii) Adsorption\n(iv) Membrane separation\n(v) Hybrid systems ","g/Nm3",0.15,10,"Amber",0,0,0,0,"Hourly","Hourly values in continuousx operation expressed and measured according to European Parliament and Council Directive 94/63/EC (OJ L 365, 31.12.1994, p. 24).\n\nLower value achievable with two-stage hybrid systems. Upper value achievable with single-stage adsorption or membrane\nsystem. \n\nBenzene monitoring may not be necessary where emissions of NMVOC are at the lower end of the range"]
["Refineries","1. Energy industries","Unspecified","Unspecified","All","Existing","All","Unspecified","Gas-fired combustion unit, with the exception of gas turbines","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion units, BAT is to use one or a combination of the techniques given below: \n\nPrimary techniques:\n(i) Selection or treatment of fuel; (ii) Combustion modifications\n\nSeconary techniques:\n(i) Selective catalytic reduction (SCR) ; (ii) Selective non-catalytic reduction (SNCR), (iii) Low temperature oxidation; (iv) SNOX combined technique\n\n\n","mg/Nm3",30,150,"Amber",0,0,0,0.03,"Monthly ","For an existing unit using high air pre-heat (i.e. > 200 °C) or with H2 content in the fuel gas higher than 50 %, the upper end of the BAT-AEL range is 200 mg/Nm3.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Refineries","1. Energy industries","Unspecified","Unspecified","All","Existing","All","Unspecified","Gas-fired combustion unit, with the exception of gas turbines","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion units, BAT is to use one or a combination of the techniques given below: \n\nPrimary techniques:\n(i) Selection or treatment of fuel; (ii) Combustion modifications\n\nSeconary techniques:\n(i) Selective catalytic reduction (SCR) ; (ii) Selective non-catalytic reduction (SNCR), (iii) Low temperature oxidation; (iv) SNOX combined technique\n\n\n","mg/Nm3",30,150,"Amber",0,0,0,0.03,"Monthly ","For an existing unit using high air pre-heat (i.e. > 200 °C) or with H2 content in the fuel gas higher than 50 %, the upper end of the BAT-AEL range is 200 mg/Nm3."]
["Refineries","1. Energy industries","Unspecified","Unspecified","All","Existing","All","Unspecified","Multi-fuel fired combustion unit  with the exception\nof gas turbines","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion units, BAT is to use one or a combination of the techniques given below: \n\nPrimary techniques:\n(i) Selection or treatment of fuel; (ii) Combustion modifications\n\nSeconary techniques:\n(i) Selective catalytic reduction (SCR) ; (ii) Selective non-catalytic reduction (SNCR), (iii) Low temperature oxidation; (iv) SNOX combined technique\n\n\n","mg/Nm3",30,300,"Green","Continuous",0,0,0.03,"Monthly ","For existing units < 100 MW firing fuel oil with a nitrogen content higher than 0,5 % (w/w) or with liquid firing > 50 % or using air preheating, values up to 450 mg/Nm3 may occur\n\nThe lower end of the range can be achieved by using the SCR technique",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Refineries","1. Energy industries","Unspecified","Unspecified","All","Existing","All","Unspecified","Multi-fuel fired combustion unit  with the exception\nof gas turbines","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion units, BAT is to use one or a combination of the techniques given below: \n\nPrimary techniques:\n(i) Selection or treatment of fuel; (ii) Combustion modifications\n\nSeconary techniques:\n(i) Selective catalytic reduction (SCR) ; (ii) Selective non-catalytic reduction (SNCR), (iii) Low temperature oxidation; (iv) SNOX combined technique\n\n\n","mg/Nm3",30,300,"Green","Continuous",0,0,0.03,"Monthly ","For existing units < 100 MW firing fuel oil with a nitrogen content higher than 0,5 % (w/w) or with liquid firing > 50 % or using air preheating, values up to 450 mg/Nm3 may occur\n\nThe lower end of the range can be achieved by using the SCR technique"]
["Refineries","1. Energy industries","Unspecified","Unspecified","All","New","All","Unspecified","Gas turbine","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion units, BAT is to use one or a combination of the techniques given below: \n\nPrimary techniques:\n(i) Selection or treatment of fuel; (ii) Combustion modifications\n\nSeconary techniques:\n(i) Selective catalytic reduction (SCR) ; (ii) Selective non-catalytic reduction (SNCR), (iii) Low temperature oxidation; (iv) SNOX combined technique\n\n\n","mg/Nm3",20,50,"Amber",0,0,0,0.15,"Monthly "," BAT-AEL refers to combined emissions from the gas turbine and the supplementary firing recovery boiler, where present.\n\nFor fuel with high H2 content (i.e. above 10 %), the upper end of the range is 75 mg/Nm3. \n\nGas turbine (including combined cycle gas\nturbine — CCGT) and integrated gasification\ncombined cycle turbine (IGCC)) ",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Refineries","1. Energy industries","Unspecified","Unspecified","All","New","All","Unspecified","Gas turbine","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion units, BAT is to use one or a combination of the techniques given below: \n\nPrimary techniques:\n(i) Selection or treatment of fuel; (ii) Combustion modifications\n\nSeconary techniques:\n(i) Selective catalytic reduction (SCR) ; (ii) Selective non-catalytic reduction (SNCR), (iii) Low temperature oxidation; (iv) SNOX combined technique\n\n\n","mg/Nm3",20,50,"Amber",0,0,0,0.15,"Monthly "," BAT-AEL refers to combined emissions from the gas turbine and the supplementary firing recovery boiler, where present.\n\nFor fuel with high H2 content (i.e. above 10 %), the upper end of the range is 75 mg/Nm3. \n\nGas turbine (including combined cycle gas\nturbine — CCGT) and integrated gasification\ncombined cycle turbine (IGCC)) "]
["Refineries","1. Energy industries","Unspecified","Unspecified","All","New","All","Unspecified","Gas-fired combustion unit, with the exception of gas turbines","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion units, BAT is to use one or a combination of the techniques given below: \n\nPrimary techniques:\n(i) Selection or treatment of fuel; (ii) Combustion modifications\n\nSeconary techniques:\n(i) Selective catalytic reduction (SCR) ; (ii) Selective non-catalytic reduction (SNCR), (iii) Low temperature oxidation; (iv) SNOX combined technique\n\n\n","mg/Nm3",30,100,"Amber",0,0,0,0.03,"Monthly ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Refineries","1. Energy industries","Unspecified","Unspecified","All","New","All","Unspecified","Gas-fired combustion unit, with the exception of gas turbines","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion units, BAT is to use one or a combination of the techniques given below: \n\nPrimary techniques:\n(i) Selection or treatment of fuel; (ii) Combustion modifications\n\nSeconary techniques:\n(i) Selective catalytic reduction (SCR) ; (ii) Selective non-catalytic reduction (SNCR), (iii) Low temperature oxidation; (iv) SNOX combined technique\n\n\n","mg/Nm3",30,100,"Amber",0,0,0,0.03,"Monthly ",0]
["Refineries","1. Energy industries","Unspecified","Unspecified","All","Unspecified","All","Unspecified","Gas turbine- Existing","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion units, BAT is to use one or a combination of the techniques given below: \n\nPrimary techniques:\n(i) Selection or treatment of fuel; (ii) Combustion modifications\n\nSeconary techniques:\n(i) Selective catalytic reduction (SCR) ; (ii) Selective non-catalytic reduction (SNCR), (iii) Low temperature oxidation; (iv) SNOX combined technique\n\n\n","mg/Nm3",40,120,"Amber",0,0,0,0.15,"Monthly ","\n\n BAT-AEL refers to combined emissions from the gas turbine and the supplementary firing recovery boiler, where present.\n\nGas turbine (including combined cycle gas\nturbine — CCGT) and integrated gasification\ncombined cycle turbine (IGCC)) ",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Refineries","1. Energy industries","Unspecified","Unspecified","All","Unspecified","All","Unspecified","Gas turbine- Existing","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from the combustion units, BAT is to use one or a combination of the techniques given below: \n\nPrimary techniques:\n(i) Selection or treatment of fuel; (ii) Combustion modifications\n\nSeconary techniques:\n(i) Selective catalytic reduction (SCR) ; (ii) Selective non-catalytic reduction (SNCR), (iii) Low temperature oxidation; (iv) SNOX combined technique\n\n\n","mg/Nm3",40,120,"Amber",0,0,0,0.15,"Monthly ","\n\n BAT-AEL refers to combined emissions from the gas turbine and the supplementary firing recovery boiler, where present.\n\nGas turbine (including combined cycle gas\nturbine — CCGT) and integrated gasification\ncombined cycle turbine (IGCC)) "]
["Refineries","1. Energy industries","Unspecified","Unspecified","All","New","All","Unspecified","Regenerator in the catalytic cracking process-all combustion mode ","Air","NOX, expressed as NO2","In order to prevent or reduce NOX emissions to air from the catalytic cracking process (regenerator),\nBAT is to use one or a combination of the techniques given below: \n\nPrimary techniques\n(i) Process optimisation ; (ii) Low-NOX CO oxidation promoters; (iii) Specific additives for NOX reduction \n\nSecondary techniques\n(i) Selective catalytic reduction (SCR); (ii) Selective non-catalytic reduction (SNCR) ; (iii) Low temperature oxidation\n","mg/Nm3",30,100,"Green","Continuous",0,0,0.03,"Monthly ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Refineries","1. Energy industries","Unspecified","Unspecified","All","New","All","Unspecified","Regenerator in the catalytic cracking process-all combustion mode ","Air","NOX, expressed as NO2","In order to prevent or reduce NOX emissions to air from the catalytic cracking process (regenerator),\nBAT is to use one or a combination of the techniques given below: \n\nPrimary techniques\n(i) Process optimisation ; (ii) Low-NOX CO oxidation promoters; (iii) Specific additives for NOX reduction \n\nSecondary techniques\n(i) Selective catalytic reduction (SCR); (ii) Selective non-catalytic reduction (SNCR) ; (iii) Low temperature oxidation\n","mg/Nm3",30,100,"Green","Continuous",0,0,0.03,"Monthly ",0]
["Refineries","1. Energy industries","Unspecified","Unspecified","All","Existing","All","Unspecified","Regenerator in the catalytic cracking process- full combustion mode","Air","NOX, expressed as NO3","In order to prevent or reduce NOX emissions to air from the catalytic cracking process (regenerator),\nBAT is to use one or a combination of the techniques given below: \n\nPrimary techniques\n(i) Process optimisation ; (ii) Low-NOX CO oxidation promoters; (iii) Specific additives for NOX reduction \n\nSecondary techniques\n(i) Selective catalytic reduction (SCR); (ii) Selective non-catalytic reduction (SNCR) ; (iii) Low temperature oxidation\n","mg/Nm3",100,300,"Green","Continuous",0,0,0.03,"Monthly ","When antimony (Sb) injection is used for metal passivation, NOX levels up to 700 mg/Nm3 may occur. The lower end of the range can be achieved by using the SCR technique.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Refineries","1. Energy industries","Unspecified","Unspecified","All","Existing","All","Unspecified","Regenerator in the catalytic cracking process- full combustion mode","Air","NOX, expressed as NO3","In order to prevent or reduce NOX emissions to air from the catalytic cracking process (regenerator),\nBAT is to use one or a combination of the techniques given below: \n\nPrimary techniques\n(i) Process optimisation ; (ii) Low-NOX CO oxidation promoters; (iii) Specific additives for NOX reduction \n\nSecondary techniques\n(i) Selective catalytic reduction (SCR); (ii) Selective non-catalytic reduction (SNCR) ; (iii) Low temperature oxidation\n","mg/Nm3",100,300,"Green","Continuous",0,0,0.03,"Monthly ","When antimony (Sb) injection is used for metal passivation, NOX levels up to 700 mg/Nm3 may occur. The lower end of the range can be achieved by using the SCR technique."]
["Refineries","1. Energy industries","Unspecified","Unspecified","All","Existing","All","Unspecified","Regenerator in the catalytic cracking process- partial combustion mode ","Air","NOX, expressed as NO4","In order to prevent or reduce NOX emissions to air from the catalytic cracking process (regenerator),\nBAT is to use one or a combination of the techniques given below: \n\nPrimary techniques\n(i) Process optimisation ; (ii) Low-NOX CO oxidation promoters; (iii) Specific additives for NOX reduction \n\nSecondary techniques\n(i) Selective catalytic reduction (SCR); (ii) Selective non-catalytic reduction (SNCR) ; (iii) Low temperature oxidation\n","mg/Nm3",100,400,"Green","Continuous",0,0,0.03,"Monthly ","When antimony (Sb) injection is used for metal passivation, NOX levels up to 700 mg/Nm3 may occur. The lower end of the range can be achieved by using the SCR technique.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Refineries","1. Energy industries","Unspecified","Unspecified","All","Existing","All","Unspecified","Regenerator in the catalytic cracking process- partial combustion mode ","Air","NOX, expressed as NO4","In order to prevent or reduce NOX emissions to air from the catalytic cracking process (regenerator),\nBAT is to use one or a combination of the techniques given below: \n\nPrimary techniques\n(i) Process optimisation ; (ii) Low-NOX CO oxidation promoters; (iii) Specific additives for NOX reduction \n\nSecondary techniques\n(i) Selective catalytic reduction (SCR); (ii) Selective non-catalytic reduction (SNCR) ; (iii) Low temperature oxidation\n","mg/Nm3",100,400,"Green","Continuous",0,0,0.03,"Monthly ","When antimony (Sb) injection is used for metal passivation, NOX levels up to 700 mg/Nm3 may occur. The lower end of the range can be achieved by using the SCR technique."]
["Refineries","1. Energy industries","Unspecified","Unspecified","All","Existing","All","Unspecified","Regenerator in the catalytic cracking process- full combustion","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX emissions to air from the catalytic cracking process (regenerator), BAT is to use one or a combination of the techniques given below:\n\nPrimary techniques:\n(i) Use of SOX reducing catalyst additives, (ii) Use of low sulphur feedstock (e.g. by feedstock selection or by hydrotreatment of the feed) \n\nSecondary techniques:\n(i) i) Non-regenerative scrubbing; (ii) Regenerative scrubbing","mg/Nm3",100,800,"Green","Continuous",0,0,0.03,"Monthly ","Where selection of low sulphur (e.g. < 0,5 % w/w) feed (or hydrotreatment) and/or scrubbing is applicable, for all combustion modes: the upper end of the BAT-AEL range is ≤ 600 mg/Nm3.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Refineries","1. Energy industries","Unspecified","Unspecified","All","Existing","All","Unspecified","Regenerator in the catalytic cracking process- full combustion","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX emissions to air from the catalytic cracking process (regenerator), BAT is to use one or a combination of the techniques given below:\n\nPrimary techniques:\n(i) Use of SOX reducing catalyst additives, (ii) Use of low sulphur feedstock (e.g. by feedstock selection or by hydrotreatment of the feed) \n\nSecondary techniques:\n(i) i) Non-regenerative scrubbing; (ii) Regenerative scrubbing","mg/Nm3",100,800,"Green","Continuous",0,0,0.03,"Monthly ","Where selection of low sulphur (e.g. < 0,5 % w/w) feed (or hydrotreatment) and/or scrubbing is applicable, for all combustion modes: the upper end of the BAT-AEL range is ≤ 600 mg/Nm3."]
["Refineries","1. Energy industries","Unspecified","Unspecified","All","Existing","All","Unspecified","Regenerator in the catalytic cracking process- partial combustion","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX emissions to air from the catalytic cracking process (regenerator), BAT is to use one or a combination of the techniques given below:\n\nPrimary techniques:\n(i) Use of SOX reducing catalyst additives, (ii) Use of low sulphur feedstock (e.g. by feedstock selection or by hydrotreatment of the feed) \n\nSecondary techniques:\n(i) i) Non-regenerative scrubbing; (ii) Regenerative scrubbing","mg/Nm3",100,1200,"Green","Continuous",0,0,0.03,"Monthly ","Where selection of low sulphur (e.g. < 0,5 % w/w) feed (or hydrotreatment) and/or scrubbing is applicable, for all combustion modes: the upper end of the BAT-AEL range is ≤ 600 mg/Nm3.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Refineries","1. Energy industries","Unspecified","Unspecified","All","Existing","All","Unspecified","Regenerator in the catalytic cracking process- partial combustion","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX emissions to air from the catalytic cracking process (regenerator), BAT is to use one or a combination of the techniques given below:\n\nPrimary techniques:\n(i) Use of SOX reducing catalyst additives, (ii) Use of low sulphur feedstock (e.g. by feedstock selection or by hydrotreatment of the feed) \n\nSecondary techniques:\n(i) i) Non-regenerative scrubbing; (ii) Regenerative scrubbing","mg/Nm3",100,1200,"Green","Continuous",0,0,0.03,"Monthly ","Where selection of low sulphur (e.g. < 0,5 % w/w) feed (or hydrotreatment) and/or scrubbing is applicable, for all combustion modes: the upper end of the BAT-AEL range is ≤ 600 mg/Nm3."]
["Refineries","1. Energy industries","Unspecified","Unspecified","All","New","All","Unspecified","Regenerator in the catalytic cracking process","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX emissions to air from the catalytic cracking process (regenerator), BAT is to use one or a combination of the techniques given below:\n\nPrimary techniques:\n(i) Use of SOX reducing catalyst additives, (ii) Use of low sulphur feedstock (e.g. by feedstock selection or by hydrotreatment of the feed) \n\nSecondary techniques:\n(i) i) Non-regenerative scrubbing; (ii) Regenerative scrubbing","mg/Nm3","N/A",300,"Green","Continuous",0,0,0.03,"Monthly ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Refineries","1. Energy industries","Unspecified","Unspecified","All","New","All","Unspecified","Regenerator in the catalytic cracking process","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX emissions to air from the catalytic cracking process (regenerator), BAT is to use one or a combination of the techniques given below:\n\nPrimary techniques:\n(i) Use of SOX reducing catalyst additives, (ii) Use of low sulphur feedstock (e.g. by feedstock selection or by hydrotreatment of the feed) \n\nSecondary techniques:\n(i) i) Non-regenerative scrubbing; (ii) Regenerative scrubbing","mg/Nm3","N/A",300,"Green","Continuous",0,0,0.03,"Monthly ",0]
["Refineries","1. Energy industries","Unspecified","Unspecified","All","Unspecified","All","Unspecified","Multi-fuel fired combustion units, with the exception of gas turbines and stationary gas engines","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX emissions to air from the combustion units, BAT is to use one or a combination of the techniques given below.\n\nPrimary techniques:\n(i) Use of gas to replace liquid fuel; (ii) Treatment of refinery fuel gas (RFG); (iii) Use of low sulphur\nrefinery fuel oil (RFO) e.g. by RFO selection or by hydrotreatment of RFO \n\nSecondary techniques:\n(i) Use of low sulphur refinery fuel oil (RFO) e. g. by RFO selection or by hydrotreatment of RFO; (ii) Regenerative scrubbing; (iii) SNOX combined technique","mg/Nm3",35,600,"Amber",0,0,0,0.03,"Monthly ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Refineries","1. Energy industries","Unspecified","Unspecified","All","Unspecified","All","Unspecified","Multi-fuel fired combustion units, with the exception of gas turbines and stationary gas engines","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX emissions to air from the combustion units, BAT is to use one or a combination of the techniques given below.\n\nPrimary techniques:\n(i) Use of gas to replace liquid fuel; (ii) Treatment of refinery fuel gas (RFG); (iii) Use of low sulphur\nrefinery fuel oil (RFO) e.g. by RFO selection or by hydrotreatment of RFO \n\nSecondary techniques:\n(i) Use of low sulphur refinery fuel oil (RFO) e. g. by RFO selection or by hydrotreatment of RFO; (ii) Regenerative scrubbing; (iii) SNOX combined technique","mg/Nm3",35,600,"Amber",0,0,0,0.03,"Monthly ",0]
["Refineries","1. Energy industries","Unspecified","Unspecified","All","Unspecified","Refinery fuel gas (RFG)","Unspecified","Combustion unit","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX emissions to air from the combustion units, BAT is to use one or a combination of the techniques given below.\n\nPrimary techniques:\n(i) Use of gas to replace liquid fuel; (ii) Treatment of refinery fuel gas (RFG); (iii) Use of low sulphur\nrefinery fuel oil (RFO) e.g. by RFO selection or by hydrotreatment of RFO \n\nSecondary techniques:\n(i) Use of low sulphur refinery fuel oil (RFO) e. g. by RFO selection or by hydrotreatment of RFO; (ii) Regenerative scrubbing; (iii) SNOX combined technique","mg/Nm3",5,35,"Amber",0,0,0,0.03,"Monthly ","In the specific configuration of RFG treatment with a low scrubber operative pressure and with a refinery fuel gas with an H/C molar ratio above 5, the upper end of the BAT-AEL range can be as high as 45 mg/Nm3.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Refineries","1. Energy industries","Unspecified","Unspecified","All","Unspecified","Refinery fuel gas (RFG)","Unspecified","Combustion unit","Air","Sulphur Dioxide (24 Hour Mean)","In order to prevent or reduce SOX emissions to air from the combustion units, BAT is to use one or a combination of the techniques given below.\n\nPrimary techniques:\n(i) Use of gas to replace liquid fuel; (ii) Treatment of refinery fuel gas (RFG); (iii) Use of low sulphur\nrefinery fuel oil (RFO) e.g. by RFO selection or by hydrotreatment of RFO \n\nSecondary techniques:\n(i) Use of low sulphur refinery fuel oil (RFO) e. g. by RFO selection or by hydrotreatment of RFO; (ii) Regenerative scrubbing; (iii) SNOX combined technique","mg/Nm3",5,35,"Amber",0,0,0,0.03,"Monthly ","In the specific configuration of RFG treatment with a low scrubber operative pressure and with a refinery fuel gas with an H/C molar ratio above 5, the upper end of the BAT-AEL range can be as high as 45 mg/Nm3."]
["Refineries","1. Energy industries","Unspecified","Unspecified","All","Unspecified","All","Unspecified","Whole refinery ","Water","Benzene","Removal of insoluble substances by recovering oil: \n— API Separators (APIs)\n— Corrugated Plate Interceptors (CPIs)\n— Parallel Plate Interceptors (PPIs)\n— Tilted Plate Interceptors (TPIs)\n— Buffer and/or equalisation tanks \n\nRemoval of insoluble substances by recovering suspended solid and dispersed oil:\nThese techniques generally include:\n— Dissolved Gas Flotation (DGF)\n— Induced Gas Flotation (IGF)\n— Sand Filtration \n\nRemoval of soluble substances including biological treatment and clarification:\nBiological treatment techniques may include:\n— Fixed bed systems\n— Suspended bed systems.\nOne of the most commonly used suspended bed system in refineries WWTP is\nthe activated sludge process. Fixed bed systems may include a biofilter or trickling\nfilter\n\nAdditional treatment step:\nA specific waste water treatment intended to complement the previous treatment\nsteps e.g. for further reducing nitrogen or carbon compounds. Generally used\nwhere specific local requirements for water preservation exist\n","mg/l",1E-3,0.05,"Green","Monthly",0,0,"N/A","Yearly ","Refers to a flow-proportional composite sample taken over a period of 24 hours or, provided that sufficient flow stability is demonstrated, a time-proportional sample.\n\nNot all parameters and sampling frequencies are applicable to effluent from gas refining sites",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Refineries","1. Energy industries","Unspecified","Unspecified","All","Unspecified","All","Unspecified","Whole refinery ","Water","Benzene","Removal of insoluble substances by recovering oil: \n— API Separators (APIs)\n— Corrugated Plate Interceptors (CPIs)\n— Parallel Plate Interceptors (PPIs)\n— Tilted Plate Interceptors (TPIs)\n— Buffer and/or equalisation tanks \n\nRemoval of insoluble substances by recovering suspended solid and dispersed oil:\nThese techniques generally include:\n— Dissolved Gas Flotation (DGF)\n— Induced Gas Flotation (IGF)\n— Sand Filtration \n\nRemoval of soluble substances including biological treatment and clarification:\nBiological treatment techniques may include:\n— Fixed bed systems\n— Suspended bed systems.\nOne of the most commonly used suspended bed system in refineries WWTP is\nthe activated sludge process. Fixed bed systems may include a biofilter or trickling\nfilter\n\nAdditional treatment step:\nA specific waste water treatment intended to complement the previous treatment\nsteps e.g. for further reducing nitrogen or carbon compounds. Generally used\nwhere specific local requirements for water preservation exist\n","mg/l",1E-3,0.05,"Green","Monthly",0,0,"N/A","Yearly ","Refers to a flow-proportional composite sample taken over a period of 24 hours or, provided that sufficient flow stability is demonstrated, a time-proportional sample.\n\nNot all parameters and sampling frequencies are applicable to effluent from gas refining sites"]
["Refineries","1. Energy industries","Unspecified","Unspecified","All","Unspecified","All","Unspecified","Whole refinery ","Water","BOD5","Removal of insoluble substances by recovering oil: \n— API Separators (APIs)\n— Corrugated Plate Interceptors (CPIs)\n— Parallel Plate Interceptors (PPIs)\n— Tilted Plate Interceptors (TPIs)\n— Buffer and/or equalisation tanks \n\nRemoval of insoluble substances by recovering suspended solid and dispersed oil:\nThese techniques generally include:\n— Dissolved Gas Flotation (DGF)\n— Induced Gas Flotation (IGF)\n— Sand Filtration \n\nRemoval of soluble substances including biological treatment and clarification:\nBiological treatment techniques may include:\n— Fixed bed systems\n— Suspended bed systems.\nOne of the most commonly used suspended bed system in refineries WWTP is\nthe activated sludge process. Fixed bed systems may include a biofilter or trickling\nfilter\n\nAdditional treatment step:\nA specific waste water treatment intended to complement the previous treatment\nsteps e.g. for further reducing nitrogen or carbon compounds. Generally used\nwhere specific local requirements for water preservation exist\n","mg/l","N/A","N/A","Green","Weekly",0,0,"N/A","Yearly ","Refers to a flow-proportional composite sample taken over a period of 24 hours or, provided that sufficient flow stability is demonstrated, a time-proportional sample.\n\nNot all parameters and sampling frequencies are applicable to effluent from gas refining sites",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Refineries","1. Energy industries","Unspecified","Unspecified","All","Unspecified","All","Unspecified","Whole refinery ","Water","BOD5","Removal of insoluble substances by recovering oil: \n— API Separators (APIs)\n— Corrugated Plate Interceptors (CPIs)\n— Parallel Plate Interceptors (PPIs)\n— Tilted Plate Interceptors (TPIs)\n— Buffer and/or equalisation tanks \n\nRemoval of insoluble substances by recovering suspended solid and dispersed oil:\nThese techniques generally include:\n— Dissolved Gas Flotation (DGF)\n— Induced Gas Flotation (IGF)\n— Sand Filtration \n\nRemoval of soluble substances including biological treatment and clarification:\nBiological treatment techniques may include:\n— Fixed bed systems\n— Suspended bed systems.\nOne of the most commonly used suspended bed system in refineries WWTP is\nthe activated sludge process. Fixed bed systems may include a biofilter or trickling\nfilter\n\nAdditional treatment step:\nA specific waste water treatment intended to complement the previous treatment\nsteps e.g. for further reducing nitrogen or carbon compounds. Generally used\nwhere specific local requirements for water preservation exist\n","mg/l","N/A","N/A","Green","Weekly",0,0,"N/A","Yearly ","Refers to a flow-proportional composite sample taken over a period of 24 hours or, provided that sufficient flow stability is demonstrated, a time-proportional sample.\n\nNot all parameters and sampling frequencies are applicable to effluent from gas refining sites"]
["Refineries","1. Energy industries","Unspecified","Unspecified","All","Unspecified","All","Unspecified","Whole refinery ","Water","Cadmium and its compounds (< 40 mg/l Ca CO3)","Removal of insoluble substances by recovering oil: \n— API Separators (APIs)\n— Corrugated Plate Interceptors (CPIs)\n— Parallel Plate Interceptors (PPIs)\n— Tilted Plate Interceptors (TPIs)\n— Buffer and/or equalisation tanks \n\nRemoval of insoluble substances by recovering suspended solid and dispersed oil:\nThese techniques generally include:\n— Dissolved Gas Flotation (DGF)\n— Induced Gas Flotation (IGF)\n— Sand Filtration \n\nRemoval of soluble substances including biological treatment and clarification:\nBiological treatment techniques may include:\n— Fixed bed systems\n— Suspended bed systems.\nOne of the most commonly used suspended bed system in refineries WWTP is\nthe activated sludge process. Fixed bed systems may include a biofilter or trickling\nfilter\n\nAdditional treatment step:\nA specific waste water treatment intended to complement the previous treatment\nsteps e.g. for further reducing nitrogen or carbon compounds. Generally used\nwhere specific local requirements for water preservation exist\n","mg/l",2E-3,8.0000000000000002E-3,"Green","Quarterly",0,0,"N/A","Yearly ","Refers to a flow-proportional composite sample taken over a period of 24 hours or, provided that sufficient flow stability is demonstrated, a time-proportional sample.\n\nNot all parameters and sampling frequencies are applicable to effluent from gas refining sites",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Refineries","1. Energy industries","Unspecified","Unspecified","All","Unspecified","All","Unspecified","Whole refinery ","Water","Cadmium and its compounds (< 40 mg/l Ca CO3)","Removal of insoluble substances by recovering oil: \n— API Separators (APIs)\n— Corrugated Plate Interceptors (CPIs)\n— Parallel Plate Interceptors (PPIs)\n— Tilted Plate Interceptors (TPIs)\n— Buffer and/or equalisation tanks \n\nRemoval of insoluble substances by recovering suspended solid and dispersed oil:\nThese techniques generally include:\n— Dissolved Gas Flotation (DGF)\n— Induced Gas Flotation (IGF)\n— Sand Filtration \n\nRemoval of soluble substances including biological treatment and clarification:\nBiological treatment techniques may include:\n— Fixed bed systems\n— Suspended bed systems.\nOne of the most commonly used suspended bed system in refineries WWTP is\nthe activated sludge process. Fixed bed systems may include a biofilter or trickling\nfilter\n\nAdditional treatment step:\nA specific waste water treatment intended to complement the previous treatment\nsteps e.g. for further reducing nitrogen or carbon compounds. Generally used\nwhere specific local requirements for water preservation exist\n","mg/l",2E-3,8.0000000000000002E-3,"Green","Quarterly",0,0,"N/A","Yearly ","Refers to a flow-proportional composite sample taken over a period of 24 hours or, provided that sufficient flow stability is demonstrated, a time-proportional sample.\n\nNot all parameters and sampling frequencies are applicable to effluent from gas refining sites"]
["Refineries","1. Energy industries","Unspecified","Unspecified","All","Unspecified","All","Unspecified","Whole refinery ","Water","COD","Removal of insoluble substances by recovering oil: \n— API Separators (APIs)\n— Corrugated Plate Interceptors (CPIs)\n— Parallel Plate Interceptors (PPIs)\n— Tilted Plate Interceptors (TPIs)\n— Buffer and/or equalisation tanks \n\nRemoval of insoluble substances by recovering suspended solid and dispersed oil:\nThese techniques generally include:\n— Dissolved Gas Flotation (DGF)\n— Induced Gas Flotation (IGF)\n— Sand Filtration \n\nRemoval of soluble substances including biological treatment and clarification:\nBiological treatment techniques may include:\n— Fixed bed systems\n— Suspended bed systems.\nOne of the most commonly used suspended bed system in refineries WWTP is\nthe activated sludge process. Fixed bed systems may include a biofilter or trickling\nfilter\n\nAdditional treatment step:\nA specific waste water treatment intended to complement the previous treatment\nsteps e.g. for further reducing nitrogen or carbon compounds. Generally used\nwhere specific local requirements for water preservation exist\n","mg/l",30,125,"Green","Daily",0,0,"N/A","Yearly ","Refers to a flow-proportional composite sample taken over a period of 24 hours or, provided that sufficient flow stability is demonstrated, a time-proportional sample.\n\nWhere on-site correlation is available, COD may be replaced by TOC. The correlation between COD and TOC should be\nelaborated on a case-by-case basis. TOC monitoring would be the preferred option because it does not rely on the use of\nvery toxic compounds. \n\nNot all parameters and sampling frequencies are applicable to effluent from gas refining sites",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Refineries","1. Energy industries","Unspecified","Unspecified","All","Unspecified","All","Unspecified","Whole refinery ","Water","COD","Removal of insoluble substances by recovering oil: \n— API Separators (APIs)\n— Corrugated Plate Interceptors (CPIs)\n— Parallel Plate Interceptors (PPIs)\n— Tilted Plate Interceptors (TPIs)\n— Buffer and/or equalisation tanks \n\nRemoval of insoluble substances by recovering suspended solid and dispersed oil:\nThese techniques generally include:\n— Dissolved Gas Flotation (DGF)\n— Induced Gas Flotation (IGF)\n— Sand Filtration \n\nRemoval of soluble substances including biological treatment and clarification:\nBiological treatment techniques may include:\n— Fixed bed systems\n— Suspended bed systems.\nOne of the most commonly used suspended bed system in refineries WWTP is\nthe activated sludge process. Fixed bed systems may include a biofilter or trickling\nfilter\n\nAdditional treatment step:\nA specific waste water treatment intended to complement the previous treatment\nsteps e.g. for further reducing nitrogen or carbon compounds. Generally used\nwhere specific local requirements for water preservation exist\n","mg/l",30,125,"Green","Daily",0,0,"N/A","Yearly ","Refers to a flow-proportional composite sample taken over a period of 24 hours or, provided that sufficient flow stability is demonstrated, a time-proportional sample.\n\nWhere on-site correlation is available, COD may be replaced by TOC. The correlation between COD and TOC should be\nelaborated on a case-by-case basis. TOC monitoring would be the preferred option because it does not rely on the use of\nvery toxic compounds. \n\nNot all parameters and sampling frequencies are applicable to effluent from gas refining sites"]
["Refineries","1. Energy industries","Unspecified","Unspecified","All","Unspecified","All","Unspecified","Whole refinery ","Water","Hydrocarbon oil index (HOI)","Removal of insoluble substances by recovering oil: \n— API Separators (APIs)\n— Corrugated Plate Interceptors (CPIs)\n— Parallel Plate Interceptors (PPIs)\n— Tilted Plate Interceptors (TPIs)\n— Buffer and/or equalisation tanks \n\nRemoval of insoluble substances by recovering suspended solid and dispersed oil:\nThese techniques generally include:\n— Dissolved Gas Flotation (DGF)\n— Induced Gas Flotation (IGF)\n— Sand Filtration \n\nRemoval of soluble substances including biological treatment and clarification:\nBiological treatment techniques may include:\n— Fixed bed systems\n— Suspended bed systems.\nOne of the most commonly used suspended bed system in refineries WWTP is\nthe activated sludge process. Fixed bed systems may include a biofilter or trickling\nfilter\n\nAdditional treatment step:\nA specific waste water treatment intended to complement the previous treatment\nsteps e.g. for further reducing nitrogen or carbon compounds. Generally used\nwhere specific local requirements for water preservation exist\n","mg/l",0.1,2.5,"Green","Daily",0,0,"N/A","Yearly ","Refers to a flow-proportional composite sample taken over a period of 24 hours or, provided that sufficient flow stability is demonstrated, a time-proportional sample.\n\nMoving from the current method to EN 9377-2 may require an adaptation period.\n\nNot all parameters and sampling frequencies are applicable to effluent from gas refining sites",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Refineries","1. Energy industries","Unspecified","Unspecified","All","Unspecified","All","Unspecified","Whole refinery ","Water","Hydrocarbon oil index (HOI)","Removal of insoluble substances by recovering oil: \n— API Separators (APIs)\n— Corrugated Plate Interceptors (CPIs)\n— Parallel Plate Interceptors (PPIs)\n— Tilted Plate Interceptors (TPIs)\n— Buffer and/or equalisation tanks \n\nRemoval of insoluble substances by recovering suspended solid and dispersed oil:\nThese techniques generally include:\n— Dissolved Gas Flotation (DGF)\n— Induced Gas Flotation (IGF)\n— Sand Filtration \n\nRemoval of soluble substances including biological treatment and clarification:\nBiological treatment techniques may include:\n— Fixed bed systems\n— Suspended bed systems.\nOne of the most commonly used suspended bed system in refineries WWTP is\nthe activated sludge process. Fixed bed systems may include a biofilter or trickling\nfilter\n\nAdditional treatment step:\nA specific waste water treatment intended to complement the previous treatment\nsteps e.g. for further reducing nitrogen or carbon compounds. Generally used\nwhere specific local requirements for water preservation exist\n","mg/l",0.1,2.5,"Green","Daily",0,0,"N/A","Yearly ","Refers to a flow-proportional composite sample taken over a period of 24 hours or, provided that sufficient flow stability is demonstrated, a time-proportional sample.\n\nMoving from the current method to EN 9377-2 may require an adaptation period.\n\nNot all parameters and sampling frequencies are applicable to effluent from gas refining sites"]
["Refineries","1. Energy industries","Unspecified","Unspecified","All","Unspecified","All","Unspecified","Whole refinery ","Water","Lead and its compounds","Removal of insoluble substances by recovering oil: \n— API Separators (APIs)\n— Corrugated Plate Interceptors (CPIs)\n— Parallel Plate Interceptors (PPIs)\n— Tilted Plate Interceptors (TPIs)\n— Buffer and/or equalisation tanks \n\nRemoval of insoluble substances by recovering suspended solid and dispersed oil:\nThese techniques generally include:\n— Dissolved Gas Flotation (DGF)\n— Induced Gas Flotation (IGF)\n— Sand Filtration \n\nRemoval of soluble substances including biological treatment and clarification:\nBiological treatment techniques may include:\n— Fixed bed systems\n— Suspended bed systems.\nOne of the most commonly used suspended bed system in refineries WWTP is\nthe activated sludge process. Fixed bed systems may include a biofilter or trickling\nfilter\n\nAdditional treatment step:\nA specific waste water treatment intended to complement the previous treatment\nsteps e.g. for further reducing nitrogen or carbon compounds. Generally used\nwhere specific local requirements for water preservation exist\n","mg/l",5.0000000000000001E-3,0.03,"Green","Quarterly",0,0,"N/A","Yearly ","Refers to a flow-proportional composite sample taken over a period of 24 hours or, provided that sufficient flow stability is demonstrated, a time-proportional sample. \n\nNot all parameters and sampling frequencies are applicable to effluent from gas refining sites",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Refineries","1. Energy industries","Unspecified","Unspecified","All","Unspecified","All","Unspecified","Whole refinery ","Water","Lead and its compounds","Removal of insoluble substances by recovering oil: \n— API Separators (APIs)\n— Corrugated Plate Interceptors (CPIs)\n— Parallel Plate Interceptors (PPIs)\n— Tilted Plate Interceptors (TPIs)\n— Buffer and/or equalisation tanks \n\nRemoval of insoluble substances by recovering suspended solid and dispersed oil:\nThese techniques generally include:\n— Dissolved Gas Flotation (DGF)\n— Induced Gas Flotation (IGF)\n— Sand Filtration \n\nRemoval of soluble substances including biological treatment and clarification:\nBiological treatment techniques may include:\n— Fixed bed systems\n— Suspended bed systems.\nOne of the most commonly used suspended bed system in refineries WWTP is\nthe activated sludge process. Fixed bed systems may include a biofilter or trickling\nfilter\n\nAdditional treatment step:\nA specific waste water treatment intended to complement the previous treatment\nsteps e.g. for further reducing nitrogen or carbon compounds. Generally used\nwhere specific local requirements for water preservation exist\n","mg/l",5.0000000000000001E-3,0.03,"Green","Quarterly",0,0,"N/A","Yearly ","Refers to a flow-proportional composite sample taken over a period of 24 hours or, provided that sufficient flow stability is demonstrated, a time-proportional sample. \n\nNot all parameters and sampling frequencies are applicable to effluent from gas refining sites"]
["Refineries","1. Energy industries","Unspecified","Unspecified","All","Unspecified","All","Unspecified","Whole refinery ","Water","Mercury and its compounds","Removal of insoluble substances by recovering oil: \n— API Separators (APIs)\n— Corrugated Plate Interceptors (CPIs)\n— Parallel Plate Interceptors (PPIs)\n— Tilted Plate Interceptors (TPIs)\n— Buffer and/or equalisation tanks \n\nRemoval of insoluble substances by recovering suspended solid and dispersed oil:\nThese techniques generally include:\n— Dissolved Gas Flotation (DGF)\n— Induced Gas Flotation (IGF)\n— Sand Filtration \n\nRemoval of soluble substances including biological treatment and clarification:\nBiological treatment techniques may include:\n— Fixed bed systems\n— Suspended bed systems.\nOne of the most commonly used suspended bed system in refineries WWTP is\nthe activated sludge process. Fixed bed systems may include a biofilter or trickling\nfilter\n\nAdditional treatment step:\nA specific waste water treatment intended to complement the previous treatment\nsteps e.g. for further reducing nitrogen or carbon compounds. Generally used\nwhere specific local requirements for water preservation exist\n","mg/l",1E-4,1E-3,"Green","Quarterly",0,0,"N/A","Yearly ","Refers to a flow-proportional composite sample taken over a period of 24 hours or, provided that sufficient flow stability is demonstrated, a time-proportional sample.\n\nNot all parameters and sampling frequencies are applicable to effluent from gas refining sites",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Refineries","1. Energy industries","Unspecified","Unspecified","All","Unspecified","All","Unspecified","Whole refinery ","Water","Mercury and its compounds","Removal of insoluble substances by recovering oil: \n— API Separators (APIs)\n— Corrugated Plate Interceptors (CPIs)\n— Parallel Plate Interceptors (PPIs)\n— Tilted Plate Interceptors (TPIs)\n— Buffer and/or equalisation tanks \n\nRemoval of insoluble substances by recovering suspended solid and dispersed oil:\nThese techniques generally include:\n— Dissolved Gas Flotation (DGF)\n— Induced Gas Flotation (IGF)\n— Sand Filtration \n\nRemoval of soluble substances including biological treatment and clarification:\nBiological treatment techniques may include:\n— Fixed bed systems\n— Suspended bed systems.\nOne of the most commonly used suspended bed system in refineries WWTP is\nthe activated sludge process. Fixed bed systems may include a biofilter or trickling\nfilter\n\nAdditional treatment step:\nA specific waste water treatment intended to complement the previous treatment\nsteps e.g. for further reducing nitrogen or carbon compounds. Generally used\nwhere specific local requirements for water preservation exist\n","mg/l",1E-4,1E-3,"Green","Quarterly",0,0,"N/A","Yearly ","Refers to a flow-proportional composite sample taken over a period of 24 hours or, provided that sufficient flow stability is demonstrated, a time-proportional sample.\n\nNot all parameters and sampling frequencies are applicable to effluent from gas refining sites"]
["Refineries","1. Energy industries","Unspecified","Unspecified","All","Unspecified","All","Unspecified","Whole refinery ","Water","Nickel and its compounds","Removal of insoluble substances by recovering oil: \n— API Separators (APIs)\n— Corrugated Plate Interceptors (CPIs)\n— Parallel Plate Interceptors (PPIs)\n— Tilted Plate Interceptors (TPIs)\n— Buffer and/or equalisation tanks \n\nRemoval of insoluble substances by recovering suspended solid and dispersed oil:\nThese techniques generally include:\n— Dissolved Gas Flotation (DGF)\n— Induced Gas Flotation (IGF)\n— Sand Filtration \n\nRemoval of soluble substances including biological treatment and clarification:\nBiological treatment techniques may include:\n— Fixed bed systems\n— Suspended bed systems.\nOne of the most commonly used suspended bed system in refineries WWTP is\nthe activated sludge process. Fixed bed systems may include a biofilter or trickling\nfilter\n\nAdditional treatment step:\nA specific waste water treatment intended to complement the previous treatment\nsteps e.g. for further reducing nitrogen or carbon compounds. Generally used\nwhere specific local requirements for water preservation exist\n","mg/l",5.0000000000000001E-3,0.1,"Green","Quarterly",0,0,"N/A","Yearly ","Refers to a flow-proportional composite sample taken over a period of 24 hours or, provided that sufficient flow stability is demonstrated, a time-proportional sample.\n\nNot all parameters and sampling frequencies are applicable to effluent from gas refining sites",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Refineries","1. Energy industries","Unspecified","Unspecified","All","Unspecified","All","Unspecified","Whole refinery ","Water","Nickel and its compounds","Removal of insoluble substances by recovering oil: \n— API Separators (APIs)\n— Corrugated Plate Interceptors (CPIs)\n— Parallel Plate Interceptors (PPIs)\n— Tilted Plate Interceptors (TPIs)\n— Buffer and/or equalisation tanks \n\nRemoval of insoluble substances by recovering suspended solid and dispersed oil:\nThese techniques generally include:\n— Dissolved Gas Flotation (DGF)\n— Induced Gas Flotation (IGF)\n— Sand Filtration \n\nRemoval of soluble substances including biological treatment and clarification:\nBiological treatment techniques may include:\n— Fixed bed systems\n— Suspended bed systems.\nOne of the most commonly used suspended bed system in refineries WWTP is\nthe activated sludge process. Fixed bed systems may include a biofilter or trickling\nfilter\n\nAdditional treatment step:\nA specific waste water treatment intended to complement the previous treatment\nsteps e.g. for further reducing nitrogen or carbon compounds. Generally used\nwhere specific local requirements for water preservation exist\n","mg/l",5.0000000000000001E-3,0.1,"Green","Quarterly",0,0,"N/A","Yearly ","Refers to a flow-proportional composite sample taken over a period of 24 hours or, provided that sufficient flow stability is demonstrated, a time-proportional sample.\n\nNot all parameters and sampling frequencies are applicable to effluent from gas refining sites"]
["Refineries","1. Energy industries","Unspecified","Unspecified","All","Unspecified","All","Unspecified","Whole refinery ","Water","Phenol Index","Removal of insoluble substances by recovering oil: \n— API Separators (APIs)\n— Corrugated Plate Interceptors (CPIs)\n— Parallel Plate Interceptors (PPIs)\n— Tilted Plate Interceptors (TPIs)\n— Buffer and/or equalisation tanks \n\nRemoval of insoluble substances by recovering suspended solid and dispersed oil:\nThese techniques generally include:\n— Dissolved Gas Flotation (DGF)\n— Induced Gas Flotation (IGF)\n— Sand Filtration \n\nRemoval of soluble substances including biological treatment and clarification:\nBiological treatment techniques may include:\n— Fixed bed systems\n— Suspended bed systems.\nOne of the most commonly used suspended bed system in refineries WWTP is\nthe activated sludge process. Fixed bed systems may include a biofilter or trickling\nfilter\n\nAdditional treatment step:\nA specific waste water treatment intended to complement the previous treatment\nsteps e.g. for further reducing nitrogen or carbon compounds. Generally used\nwhere specific local requirements for water preservation exist\n","mg/l","N/A","N/A","Green","Monthly",0,0,"N/A","Yearly ","Refers to a flow-proportional composite sample taken over a period of 24 hours or, provided that sufficient flow stability is demonstrated, a time-proportional sample.\n\nNot all parameters and sampling frequencies are applicable to effluent from gas refining sites",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Refineries","1. Energy industries","Unspecified","Unspecified","All","Unspecified","All","Unspecified","Whole refinery ","Water","Phenol Index","Removal of insoluble substances by recovering oil: \n— API Separators (APIs)\n— Corrugated Plate Interceptors (CPIs)\n— Parallel Plate Interceptors (PPIs)\n— Tilted Plate Interceptors (TPIs)\n— Buffer and/or equalisation tanks \n\nRemoval of insoluble substances by recovering suspended solid and dispersed oil:\nThese techniques generally include:\n— Dissolved Gas Flotation (DGF)\n— Induced Gas Flotation (IGF)\n— Sand Filtration \n\nRemoval of soluble substances including biological treatment and clarification:\nBiological treatment techniques may include:\n— Fixed bed systems\n— Suspended bed systems.\nOne of the most commonly used suspended bed system in refineries WWTP is\nthe activated sludge process. Fixed bed systems may include a biofilter or trickling\nfilter\n\nAdditional treatment step:\nA specific waste water treatment intended to complement the previous treatment\nsteps e.g. for further reducing nitrogen or carbon compounds. Generally used\nwhere specific local requirements for water preservation exist\n","mg/l","N/A","N/A","Green","Monthly",0,0,"N/A","Yearly ","Refers to a flow-proportional composite sample taken over a period of 24 hours or, provided that sufficient flow stability is demonstrated, a time-proportional sample.\n\nNot all parameters and sampling frequencies are applicable to effluent from gas refining sites"]
["Refineries","1. Energy industries","Unspecified","Unspecified","All","Unspecified","All","Unspecified","Whole refinery ","Water","Total Nitrogen (TN)","Removal of insoluble substances by recovering oil: \n— API Separators (APIs)\n— Corrugated Plate Interceptors (CPIs)\n— Parallel Plate Interceptors (PPIs)\n— Tilted Plate Interceptors (TPIs)\n— Buffer and/or equalisation tanks \n\nRemoval of insoluble substances by recovering suspended solid and dispersed oil:\nThese techniques generally include:\n— Dissolved Gas Flotation (DGF)\n— Induced Gas Flotation (IGF)\n— Sand Filtration \n\nRemoval of soluble substances including biological treatment and clarification:\nBiological treatment techniques may include:\n— Fixed bed systems\n— Suspended bed systems.\nOne of the most commonly used suspended bed system in refineries WWTP is\nthe activated sludge process. Fixed bed systems may include a biofilter or trickling\nfilter\n\nAdditional treatment step:\nA specific waste water treatment intended to complement the previous treatment\nsteps e.g. for further reducing nitrogen or carbon compounds. Generally used\nwhere specific local requirements for water preservation exist\n","mg/l",1,25,"Green","Daily",0,0,"N/A","Yearly ","Refers to a flow-proportional composite sample taken over a period of 24 hours or, provided that sufficient flow stability is demonstrated, a time-proportional sample.\n\nWhen nitrification/denitrification is used, levels below 15 mg/l can be achieved. \n\nWhere total-nitrogen is the sum of total Kjeldahl nitrogen (TKN), nitrates and nitrites\n\nNot all parameters and sampling frequencies are applicable to effluent from gas refining sites",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Refineries","1. Energy industries","Unspecified","Unspecified","All","Unspecified","All","Unspecified","Whole refinery ","Water","Total Nitrogen (TN)","Removal of insoluble substances by recovering oil: \n— API Separators (APIs)\n— Corrugated Plate Interceptors (CPIs)\n— Parallel Plate Interceptors (PPIs)\n— Tilted Plate Interceptors (TPIs)\n— Buffer and/or equalisation tanks \n\nRemoval of insoluble substances by recovering suspended solid and dispersed oil:\nThese techniques generally include:\n— Dissolved Gas Flotation (DGF)\n— Induced Gas Flotation (IGF)\n— Sand Filtration \n\nRemoval of soluble substances including biological treatment and clarification:\nBiological treatment techniques may include:\n— Fixed bed systems\n— Suspended bed systems.\nOne of the most commonly used suspended bed system in refineries WWTP is\nthe activated sludge process. Fixed bed systems may include a biofilter or trickling\nfilter\n\nAdditional treatment step:\nA specific waste water treatment intended to complement the previous treatment\nsteps e.g. for further reducing nitrogen or carbon compounds. Generally used\nwhere specific local requirements for water preservation exist\n","mg/l",1,25,"Green","Daily",0,0,"N/A","Yearly ","Refers to a flow-proportional composite sample taken over a period of 24 hours or, provided that sufficient flow stability is demonstrated, a time-proportional sample.\n\nWhen nitrification/denitrification is used, levels below 15 mg/l can be achieved. \n\nWhere total-nitrogen is the sum of total Kjeldahl nitrogen (TKN), nitrates and nitrites\n\nNot all parameters and sampling frequencies are applicable to effluent from gas refining sites"]
["Refineries","1. Energy industries","Unspecified","Unspecified","All","Unspecified","All","Unspecified","Whole refinery ","Water","Total Suspended Solids (TSS) ","Removal of insoluble substances by recovering oil: \n— API Separators (APIs)\n— Corrugated Plate Interceptors (CPIs)\n— Parallel Plate Interceptors (PPIs)\n— Tilted Plate Interceptors (TPIs)\n— Buffer and/or equalisation tanks \n\nRemoval of insoluble substances by recovering suspended solid and dispersed oil:\nThese techniques generally include:\n— Dissolved Gas Flotation (DGF)\n— Induced Gas Flotation (IGF)\n— Sand Filtration \n\nRemoval of soluble substances including biological treatment and clarification:\nBiological treatment techniques may include:\n— Fixed bed systems\n— Suspended bed systems.\nOne of the most commonly used suspended bed system in refineries WWTP is\nthe activated sludge process. Fixed bed systems may include a biofilter or trickling\nfilter\n\nAdditional treatment step:\nA specific waste water treatment intended to complement the previous treatment\nsteps e.g. for further reducing nitrogen or carbon compounds. Generally used\nwhere specific local requirements for water preservation exist\n","mg/l",5,25,"Green","Daily",0,0,"N/A","Yearly ","Refers to a flow-proportional composite sample taken over a period of 24 hours or, provided that sufficient flow stability is demonstrated, a time-proportional sample.\n\nNot all parameters and sampling frequencies are applicable to effluent from gas refining sites",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Refineries","1. Energy industries","Unspecified","Unspecified","All","Unspecified","All","Unspecified","Whole refinery ","Water","Total Suspended Solids (TSS) ","Removal of insoluble substances by recovering oil: \n— API Separators (APIs)\n— Corrugated Plate Interceptors (CPIs)\n— Parallel Plate Interceptors (PPIs)\n— Tilted Plate Interceptors (TPIs)\n— Buffer and/or equalisation tanks \n\nRemoval of insoluble substances by recovering suspended solid and dispersed oil:\nThese techniques generally include:\n— Dissolved Gas Flotation (DGF)\n— Induced Gas Flotation (IGF)\n— Sand Filtration \n\nRemoval of soluble substances including biological treatment and clarification:\nBiological treatment techniques may include:\n— Fixed bed systems\n— Suspended bed systems.\nOne of the most commonly used suspended bed system in refineries WWTP is\nthe activated sludge process. Fixed bed systems may include a biofilter or trickling\nfilter\n\nAdditional treatment step:\nA specific waste water treatment intended to complement the previous treatment\nsteps e.g. for further reducing nitrogen or carbon compounds. Generally used\nwhere specific local requirements for water preservation exist\n","mg/l",5,25,"Green","Daily",0,0,"N/A","Yearly ","Refers to a flow-proportional composite sample taken over a period of 24 hours or, provided that sufficient flow stability is demonstrated, a time-proportional sample.\n\nNot all parameters and sampling frequencies are applicable to effluent from gas refining sites"]
["Refineries","1. Energy industries","Unspecified","Unspecified","All","Unspecified","All","Unspecified","Whole refinery ","Water","Vanadium (> 200 mg/l CaCO3)","Removal of insoluble substances by recovering oil: \n— API Separators (APIs)\n— Corrugated Plate Interceptors (CPIs)\n— Parallel Plate Interceptors (PPIs)\n— Tilted Plate Interceptors (TPIs)\n— Buffer and/or equalisation tanks \n\nRemoval of insoluble substances by recovering suspended solid and dispersed oil:\nThese techniques generally include:\n— Dissolved Gas Flotation (DGF)\n— Induced Gas Flotation (IGF)\n— Sand Filtration \n\nRemoval of soluble substances including biological treatment and clarification:\nBiological treatment techniques may include:\n— Fixed bed systems\n— Suspended bed systems.\nOne of the most commonly used suspended bed system in refineries WWTP is\nthe activated sludge process. Fixed bed systems may include a biofilter or trickling\nfilter\n\nAdditional treatment step:\nA specific waste water treatment intended to complement the previous treatment\nsteps e.g. for further reducing nitrogen or carbon compounds. Generally used\nwhere specific local requirements for water preservation exist\n","mg/l","N/A","N/A","Green","Quarterly",0,0,"N/A","Yearly ","Refers to a flow-proportional composite sample taken over a period of 24 hours or, provided that sufficient flow stability is demonstrated, a time-proportional sample.\n\nNot all parameters and sampling frequencies are applicable to effluent from gas refining sites",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Refineries","1. Energy industries","Unspecified","Unspecified","All","Unspecified","All","Unspecified","Whole refinery ","Water","Vanadium (> 200 mg/l CaCO3)","Removal of insoluble substances by recovering oil: \n— API Separators (APIs)\n— Corrugated Plate Interceptors (CPIs)\n— Parallel Plate Interceptors (PPIs)\n— Tilted Plate Interceptors (TPIs)\n— Buffer and/or equalisation tanks \n\nRemoval of insoluble substances by recovering suspended solid and dispersed oil:\nThese techniques generally include:\n— Dissolved Gas Flotation (DGF)\n— Induced Gas Flotation (IGF)\n— Sand Filtration \n\nRemoval of soluble substances including biological treatment and clarification:\nBiological treatment techniques may include:\n— Fixed bed systems\n— Suspended bed systems.\nOne of the most commonly used suspended bed system in refineries WWTP is\nthe activated sludge process. Fixed bed systems may include a biofilter or trickling\nfilter\n\nAdditional treatment step:\nA specific waste water treatment intended to complement the previous treatment\nsteps e.g. for further reducing nitrogen or carbon compounds. Generally used\nwhere specific local requirements for water preservation exist\n","mg/l","N/A","N/A","Green","Quarterly",0,0,"N/A","Yearly ","Refers to a flow-proportional composite sample taken over a period of 24 hours or, provided that sufficient flow stability is demonstrated, a time-proportional sample.\n\nNot all parameters and sampling frequencies are applicable to effluent from gas refining sites"]
["Tanning of Hides and Skins","6. Other activities ","Extraction ventilation and abatement system is used as an alternative to the use of waterborne finishing materials","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Air","VOC","In order to reduce the airborne emissions of halogenated volatile organic compounds, BAT is to replace halogenated volatile organic compounds used in the process with substances that are not halogenated.","g/m3",9,23,"Green","Monitoring of volatile organic compound emissions at the outlet of abatement equipment, and recording of production continuously or periodcally. Applicable to plants carrying out finishing using solvents and employing abatement.",0,0,"Unspecified ","annual average values per unit of finished leather","BAT-AEL range expressed as total carbon.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Tanning of Hides and Skins","6. Other activities ","Extraction ventilation and abatement system is used as an alternative to the use of waterborne finishing materials","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Air","VOC","In order to reduce the airborne emissions of halogenated volatile organic compounds, BAT is to replace halogenated volatile organic compounds used in the process with substances that are not halogenated.","g/m3",9,23,"Green","Monitoring of volatile organic compound emissions at the outlet of abatement equipment, and recording of production continuously or periodcally. Applicable to plants carrying out finishing using solvents and employing abatement.",0,0,"Unspecified ","annual average values per unit of finished leather","BAT-AEL range expressed as total carbon."]
["Tanning of Hides and Skins","6. Other activities ","Bovine salted hides- Raw to wet blue/white","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Consumption","Water","In order to minimise water consumption, BAT is to use one or both of the techniques given below: (i) The optimisation of water use in all wet process steps, including the use of batch washing instead of running water washes; (ii) The use of short floats","m3/t",13,18,"Green","Measurement of water consumption in the two process stages: up to tanning and post-tanning, and recording of production in the same period.",0,0,"Unspecified ","Monthly ","Monthly average values. Processing of calfskins and vegetable tanning may require a higher water",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Tanning of Hides and Skins","6. Other activities ","Bovine salted hides- Raw to wet blue/white","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Consumption","Water","In order to minimise water consumption, BAT is to use one or both of the techniques given below: (i) The optimisation of water use in all wet process steps, including the use of batch washing instead of running water washes; (ii) The use of short floats","m3/t",13,18,"Green","Measurement of water consumption in the two process stages: up to tanning and post-tanning, and recording of production in the same period.",0,0,"Unspecified ","Monthly ","Monthly average values. Processing of calfskins and vegetable tanning may require a higher water"]
["Tanning of Hides and Skins","6. Other activities ","Bovine salted hides- Total consumption ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Consumption","Water","In order to minimise water consumption, BAT is to use one or both of the techniques given below: (i) The optimisation of water use in all wet process steps, including the use of batch washing instead of running water washes; (ii) The use of short floats","m3/t",19,28,"Green","Measurement of water consumption in the two process stages: up to tanning and post-tanning, and recording of production in the same period.",0,0,"Unspecified ","Monthly ","Monthly average values. Processing of calfskins and vegetable tanning may require a higher water",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Tanning of Hides and Skins","6. Other activities ","Bovine salted hides- Total consumption ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Consumption","Water","In order to minimise water consumption, BAT is to use one or both of the techniques given below: (i) The optimisation of water use in all wet process steps, including the use of batch washing instead of running water washes; (ii) The use of short floats","m3/t",19,28,"Green","Measurement of water consumption in the two process stages: up to tanning and post-tanning, and recording of production in the same period.",0,0,"Unspecified ","Monthly ","Monthly average values. Processing of calfskins and vegetable tanning may require a higher water"]
["Tanning of Hides and Skins","6. Other activities ","Bovine unsalted hides- Raw to wet blue/white","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Consumption","Water","In order to minimise water consumption, BAT is to use one or both of the techniques given below: (i) The optimisation of water use in all wet process steps, including the use of batch washing instead of running water washes; (ii) The use of short floats","m3/t",10,15,"Green","Measurement of water consumption in the two process stages: up to tanning and post-tanning, and recording of production in the same period.",0,0,"Unspecified ","Monthly ","Monthly average values. Processing of calfskins and vegetable tanning may require a higher water",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Tanning of Hides and Skins","6. Other activities ","Bovine unsalted hides- Raw to wet blue/white","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Consumption","Water","In order to minimise water consumption, BAT is to use one or both of the techniques given below: (i) The optimisation of water use in all wet process steps, including the use of batch washing instead of running water washes; (ii) The use of short floats","m3/t",10,15,"Green","Measurement of water consumption in the two process stages: up to tanning and post-tanning, and recording of production in the same period.",0,0,"Unspecified ","Monthly ","Monthly average values. Processing of calfskins and vegetable tanning may require a higher water"]
["Tanning of Hides and Skins","6. Other activities ","Bovine unsalted hides- Total consumption","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Consumption","Water","In order to minimise water consumption, BAT is to use one or both of the techniques given below: (i) The optimisation of water use in all wet process steps, including the use of batch washing instead of running water washes; (ii) The use of short floats","m3/t",16,25,"Green","Measurement of water consumption in the two process stages: up to tanning and post-tanning, and recording of production in the same period.",0,0,"Unspecified ","Monthly ","Monthly average values. Processing of calfskins and vegetable tanning may require a higher water",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Tanning of Hides and Skins","6. Other activities ","Bovine unsalted hides- Total consumption","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Consumption","Water","In order to minimise water consumption, BAT is to use one or both of the techniques given below: (i) The optimisation of water use in all wet process steps, including the use of batch washing instead of running water washes; (ii) The use of short floats","m3/t",16,25,"Green","Measurement of water consumption in the two process stages: up to tanning and post-tanning, and recording of production in the same period.",0,0,"Unspecified ","Monthly ","Monthly average values. Processing of calfskins and vegetable tanning may require a higher water"]
["Tanning of Hides and Skins","6. Other activities ","Bovine-unsalted hides- Post tanning processes and finishing","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Consumption","Water","In order to minimise water consumption, BAT is to use one or both of the techniques given below: (i) The optimisation of water use in all wet process steps, including the use of batch washing instead of running water washes; (ii) The use of short floats","m3/t",6,10,"Green","Measurement of water consumption in the two process stages: up to tanning and post-tanning, and recording of production in the same period.",0,0,"Unspecified ","Monthly ","Monthly average values. Processing of calfskins and vegetable tanning may require a higher water",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Tanning of Hides and Skins","6. Other activities ","Bovine-unsalted hides- Post tanning processes and finishing","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Consumption","Water","In order to minimise water consumption, BAT is to use one or both of the techniques given below: (i) The optimisation of water use in all wet process steps, including the use of batch washing instead of running water washes; (ii) The use of short floats","m3/t",6,10,"Green","Measurement of water consumption in the two process stages: up to tanning and post-tanning, and recording of production in the same period.",0,0,"Unspecified ","Monthly ","Monthly average values. Processing of calfskins and vegetable tanning may require a higher water"]
["Tanning of Hides and Skins","6. Other activities ","Bovine-unsalted hides- Post tanning processes and finishing","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Consumption","Water","In order to minimise water consumption, BAT is to use one or both of the techniques given below: (i) The optimisation of water use in all wet process steps, including the use of batch washing instead of running water washes; (ii) The use of short floats","m3/t",6,10,"Green","Measurement of water consumption in the two process stages: up to tanning and post-tanning, and recording of production in the same period.",0,0,"Unspecified ","Monthly ","Monthly average values. Processing of calfskins and vegetable tanning may require a higher water",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Tanning of Hides and Skins","6. Other activities ","Bovine-unsalted hides- Post tanning processes and finishing","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Consumption","Water","In order to minimise water consumption, BAT is to use one or both of the techniques given below: (i) The optimisation of water use in all wet process steps, including the use of batch washing instead of running water washes; (ii) The use of short floats","m3/t",6,10,"Green","Measurement of water consumption in the two process stages: up to tanning and post-tanning, and recording of production in the same period.",0,0,"Unspecified ","Monthly ","Monthly average values. Processing of calfskins and vegetable tanning may require a higher water"]
["Tanning of Hides and Skins","6. Other activities ","Sheepskins- Pickle to wet blue","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Consumption","Water","In order to minimise water consumption, BAT is to use one or both of the techniques given below: (i) The optimisation of water use in all wet process steps, including the use of batch washing instead of running water washes; (ii) The use of short floats","m3/t",30,55,"Green","Measurement of water consumption in the two process stages: up to tanning and post-tanning, and recording of production in the same period.",0,0,"Unspecified ","Monthly ","Monthly average values. Processing of calfskins and vegetable tanning may require a higher water",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Tanning of Hides and Skins","6. Other activities ","Sheepskins- Pickle to wet blue","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Consumption","Water","In order to minimise water consumption, BAT is to use one or both of the techniques given below: (i) The optimisation of water use in all wet process steps, including the use of batch washing instead of running water washes; (ii) The use of short floats","m3/t",30,55,"Green","Measurement of water consumption in the two process stages: up to tanning and post-tanning, and recording of production in the same period.",0,0,"Unspecified ","Monthly ","Monthly average values. Processing of calfskins and vegetable tanning may require a higher water"]
["Tanning of Hides and Skins","6. Other activities ","Sheepskins- Post tanning processes and finishing","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Consumption","Water","In order to minimise water consumption, BAT is to use one or both of the techniques given below: (i) The optimisation of water use in all wet process steps, including the use of batch washing instead of running water washes; (ii) The use of short floats","m3/t",15,45,"Green","Measurement of water consumption in the two process stages: up to tanning and post-tanning, and recording of production in the same period.",0,0,"Unspecified ","Monthly ","Monthly average values. Processing of calfskins and vegetable tanning may require a higher water",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Tanning of Hides and Skins","6. Other activities ","Sheepskins- Post tanning processes and finishing","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Consumption","Water","In order to minimise water consumption, BAT is to use one or both of the techniques given below: (i) The optimisation of water use in all wet process steps, including the use of batch washing instead of running water washes; (ii) The use of short floats","m3/t",15,45,"Green","Measurement of water consumption in the two process stages: up to tanning and post-tanning, and recording of production in the same period.",0,0,"Unspecified ","Monthly ","Monthly average values. Processing of calfskins and vegetable tanning may require a higher water"]
["Tanning of Hides and Skins","6. Other activities ","Sheepskins- Raw to picle","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Consumption","Water","In order to minimise water consumption, BAT is to use one or both of the techniques given below: (i) The optimisation of water use in all wet process steps, including the use of batch washing instead of running water washes; (ii) The use of short floats","m3/t",65,80,"Green","Measurement of water consumption in the two process stages: up to tanning and post-tanning, and recording of production in the same period.",0,0,"Unspecified ","Monthly ","Monthly average values. Processing of calfskins and vegetable tanning may require a higher water",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Tanning of Hides and Skins","6. Other activities ","Sheepskins- Raw to picle","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Consumption","Water","In order to minimise water consumption, BAT is to use one or both of the techniques given below: (i) The optimisation of water use in all wet process steps, including the use of batch washing instead of running water washes; (ii) The use of short floats","m3/t",65,80,"Green","Measurement of water consumption in the two process stages: up to tanning and post-tanning, and recording of production in the same period.",0,0,"Unspecified ","Monthly ","Monthly average values. Processing of calfskins and vegetable tanning may require a higher water"]
["Tanning of Hides and Skins","6. Other activities ","Sheepskins- Total","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Consumption","Water","In order to minimise water consumption, BAT is to use one or both of the techniques given below: (i) The optimisation of water use in all wet process steps, including the use of batch washing instead of running water washes; (ii) The use of short floats","m3/t",110,180,"Green","Measurement of water consumption in the two process stages: up to tanning and post-tanning, and recording of production in the same period.",0,0,"Unspecified ","Monthly ","Monthly average values. Processing of calfskins and vegetable tanning may require a higher water",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Tanning of Hides and Skins","6. Other activities ","Sheepskins- Total","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Consumption","Water","In order to minimise water consumption, BAT is to use one or both of the techniques given below: (i) The optimisation of water use in all wet process steps, including the use of batch washing instead of running water washes; (ii) The use of short floats","m3/t",110,180,"Green","Measurement of water consumption in the two process stages: up to tanning and post-tanning, and recording of production in the same period.",0,0,"Unspecified ","Monthly ","Monthly average values. Processing of calfskins and vegetable tanning may require a higher water"]
["Tanning of Hides and Skins","6. Other activities ","Coated leathers (thickness > 0.15mm): Water-borne coatings used in combination with an efficient application system ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Consumption","Solvent use levels","N/A","g/m2",115,150,"Green","N/A",0,0,"Unspecified ","annual average values per unit of finished leather",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Tanning of Hides and Skins","6. Other activities ","Coated leathers (thickness > 0.15mm): Water-borne coatings used in combination with an efficient application system ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Consumption","Solvent use levels","N/A","g/m2",115,150,"Green","N/A",0,0,"Unspecified ","annual average values per unit of finished leather",0]
["Tanning of Hides and Skins","6. Other activities ","Footwear, garment, and leathergoods leathers: Water-borne coatings used in combination with an efficient application system ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Consumption","Solvent use levels","N/A","g/m2",40,85,"Green","N/A",0,0,"Unspecified ","annual average values per unit of finished leather",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Tanning of Hides and Skins","6. Other activities ","Footwear, garment, and leathergoods leathers: Water-borne coatings used in combination with an efficient application system ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Consumption","Solvent use levels","N/A","g/m2",40,85,"Green","N/A",0,0,"Unspecified ","annual average values per unit of finished leather",0]
["Tanning of Hides and Skins","6. Other activities ","Upholstery and automative leather: Water-borne coatings used in combination with an efficient application system ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Consumption","Solvent use levels","N/A","g/m2",10,25,"Green","N/A",0,0,"Unspecified ","annual average values per unit of finished leather",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Tanning of Hides and Skins","6. Other activities ","Upholstery and automative leather: Water-borne coatings used in combination with an efficient application system ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Consumption","Solvent use levels","N/A","g/m2",10,25,"Green","N/A",0,0,"Unspecified ","annual average values per unit of finished leather",0]
["Tanning of Hides and Skins","6. Other activities ","Post treatment","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Water","Un-ionised ammonia as nitrogen","In order to reduce emissions to receiving waters, BAT is to apply waste water treatment comprising an appropriate on-site and/or off-site combination of the following techniques:\n(i) mechanical treatment;\n(ii) physico-chemical treatment;\n(iii) biological treatment;\n(iv) biological nitrogen elimination.","mg/l","N/A",10,"Green","Monitoring of chemical oxygen demand (COD), biochemical oxygen demand (BOD) and ammoniacal nitrogen after on-site or off-site effluent treatment for direct discharges to receiving water, by using flow-proportional 24-hour composite samples. Monitoring of total suspended solids after on-site or off-site effluent treatment for direct discharges to receiving water.",0,0,"Unspecified ","monthly average values based on the average of the 24-hour representative composite samples taken over a month)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Tanning of Hides and Skins","6. Other activities ","Post treatment","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Water","Un-ionised ammonia as nitrogen","In order to reduce emissions to receiving waters, BAT is to apply waste water treatment comprising an appropriate on-site and/or off-site combination of the following techniques:\n(i) mechanical treatment;\n(ii) physico-chemical treatment;\n(iii) biological treatment;\n(iv) biological nitrogen elimination.","mg/l","N/A",10,"Green","Monitoring of chemical oxygen demand (COD), biochemical oxygen demand (BOD) and ammoniacal nitrogen after on-site or off-site effluent treatment for direct discharges to receiving water, by using flow-proportional 24-hour composite samples. Monitoring of total suspended solids after on-site or off-site effluent treatment for direct discharges to receiving water.",0,0,"Unspecified ","monthly average values based on the average of the 24-hour representative composite samples taken over a month)",0]
["Tanning of Hides and Skins","6. Other activities ","Post treatment","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Water","BOD5","In order to reduce emissions to receiving waters, BAT is to apply waste water treatment comprising an appropriate on-site and/or off-site combination of the following techniques:\n(i) mechanical treatment;\n(ii) physico-chemical treatment;\n(iii) biological treatment;\n(iv) biological nitrogen elimination.","mg/l",15,25,"Green","Monitoring of chemical oxygen demand (COD), biochemical oxygen demand (BOD) and ammoniacal nitrogen after on-site or off-site effluent treatment for direct discharges to receiving water, by using flow-proportional 24-hour composite samples. Monitoring of total suspended solids after on-site or off-site effluent treatment for direct discharges to receiving water.",0,0,"Unspecified ","monthly average values based on the average of the 24-hour representative composite samples taken over a month)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Tanning of Hides and Skins","6. Other activities ","Post treatment","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Water","BOD5","In order to reduce emissions to receiving waters, BAT is to apply waste water treatment comprising an appropriate on-site and/or off-site combination of the following techniques:\n(i) mechanical treatment;\n(ii) physico-chemical treatment;\n(iii) biological treatment;\n(iv) biological nitrogen elimination.","mg/l",15,25,"Green","Monitoring of chemical oxygen demand (COD), biochemical oxygen demand (BOD) and ammoniacal nitrogen after on-site or off-site effluent treatment for direct discharges to receiving water, by using flow-proportional 24-hour composite samples. Monitoring of total suspended solids after on-site or off-site effluent treatment for direct discharges to receiving water.",0,0,"Unspecified ","monthly average values based on the average of the 24-hour representative composite samples taken over a month)",0]
["Tanning of Hides and Skins","6. Other activities ","Post treatment","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Water","COD","In order to reduce emissions to receiving waters, BAT is to apply waste water treatment comprising an appropriate on-site and/or off-site combination of the following techniques:\n(i) mechanical treatment;\n(ii) physico-chemical treatment;\n(iii) biological treatment;\n(iv) biological nitrogen elimination.","mg/l",200,500,"Green","Monitoring of chemical oxygen demand (COD), biochemical oxygen demand (BOD) and ammoniacal nitrogen after on-site or off-site effluent treatment for direct discharges to receiving water, by using flow-proportional 24-hour composite samples. Monitoring of total suspended solids after on-site or off-site effluent treatment for direct discharges to receiving water.",0,0,"Unspecified ","monthly average values based on the average of the 24-hour representative composite samples taken over a month)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Tanning of Hides and Skins","6. Other activities ","Post treatment","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Water","COD","In order to reduce emissions to receiving waters, BAT is to apply waste water treatment comprising an appropriate on-site and/or off-site combination of the following techniques:\n(i) mechanical treatment;\n(ii) physico-chemical treatment;\n(iii) biological treatment;\n(iv) biological nitrogen elimination.","mg/l",200,500,"Green","Monitoring of chemical oxygen demand (COD), biochemical oxygen demand (BOD) and ammoniacal nitrogen after on-site or off-site effluent treatment for direct discharges to receiving water, by using flow-proportional 24-hour composite samples. Monitoring of total suspended solids after on-site or off-site effluent treatment for direct discharges to receiving water.",0,0,"Unspecified ","monthly average values based on the average of the 24-hour representative composite samples taken over a month)",0]
["Tanning of Hides and Skins","6. Other activities ","Post treatment","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Water","Sulphide (as S)","In order to reduce emissions to receiving waters, BAT is to apply waste water treatment comprising an appropriate on-site and/or off-site combination of the following techniques:\n(i) mechanical treatment;\n(ii) physico-chemical treatment;\n(iii) biological treatment;\n(iv) biological nitrogen elimination.","mg/l","N/A",1,"Green","Monitoring of the sulphide concentration and total chromium concentration in the final effluent after treatment for direct discharge to receiving water, by using flow proportional 24-hour composite samples. Monitoring of the sulphide concentration and total chromium concentration after chromium precipitation for indirect discharge, by using flow proportional 24-hour composite samples.",0,0,"Unspecified ","monthly average values based on the average of the 24-hour representative composite samples taken over a month)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Tanning of Hides and Skins","6. Other activities ","Post treatment","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Water","Sulphide (as S)","In order to reduce emissions to receiving waters, BAT is to apply waste water treatment comprising an appropriate on-site and/or off-site combination of the following techniques:\n(i) mechanical treatment;\n(ii) physico-chemical treatment;\n(iii) biological treatment;\n(iv) biological nitrogen elimination.","mg/l","N/A",1,"Green","Monitoring of the sulphide concentration and total chromium concentration in the final effluent after treatment for direct discharge to receiving water, by using flow proportional 24-hour composite samples. Monitoring of the sulphide concentration and total chromium concentration after chromium precipitation for indirect discharge, by using flow proportional 24-hour composite samples.",0,0,"Unspecified ","monthly average values based on the average of the 24-hour representative composite samples taken over a month)",0]
["Tanning of Hides and Skins","6. Other activities ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Indirect discharges of waste water from tanneries into urban waste water treatment plants ","Water","Sulphide (as S)","In order to reduce total chromium and sulphide emissions through indirect discharges of waste water from tanneries into urban waste water treatment plants, BAT is to apply chromium precipitation and sulphide oxidation.","mg/l","N/A",1,"Green","Monitoring of the sulphide concentration and total chromium concentration in the final effluent after treatment for direct discharge to receiving water, by using flow proportional 24-hour composite samples. Monitoring of the sulphide concentration and total chromium concentration after chromium precipitation for indirect discharge, by using flow proportional 24-hour composite samples.",0,0,"Unspecified ","monthly average values based on the average of the 24-hour representative composite samples taken over a month","BAT-AELs for total chromium and sulphide emissions through indirect discharges of waste water from tanneries into urban waste water treatment plants",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Tanning of Hides and Skins","6. Other activities ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Indirect discharges of waste water from tanneries into urban waste water treatment plants ","Water","Sulphide (as S)","In order to reduce total chromium and sulphide emissions through indirect discharges of waste water from tanneries into urban waste water treatment plants, BAT is to apply chromium precipitation and sulphide oxidation.","mg/l","N/A",1,"Green","Monitoring of the sulphide concentration and total chromium concentration in the final effluent after treatment for direct discharge to receiving water, by using flow proportional 24-hour composite samples. Monitoring of the sulphide concentration and total chromium concentration after chromium precipitation for indirect discharge, by using flow proportional 24-hour composite samples.",0,0,"Unspecified ","monthly average values based on the average of the 24-hour representative composite samples taken over a month","BAT-AELs for total chromium and sulphide emissions through indirect discharges of waste water from tanneries into urban waste water treatment plants"]
["Tanning of Hides and Skins","6. Other activities ","Post treatment","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Water","Total Suspended Solids (TSS) ","In order to reduce emissions to receiving waters, BAT is to apply waste water treatment comprising an appropriate on-site and/or off-site combination of the following techniques:\n(i) mechanical treatment;\n(ii) physico-chemical treatment;\n(iii) biological treatment;\n(iv) biological nitrogen elimination.","mg/l","N/A",35,"Green","Monitoring of chemical oxygen demand (COD), biochemical oxygen demand (BOD) and ammoniacal nitrogen after on-site or off-site effluent treatment for direct discharges to receiving water, by using flow-proportional 24-hour composite samples. Monitoring of total suspended solids after on-site or off-site effluent treatment for direct discharges to receiving water.",0,0,"Unspecified ",0,0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Tanning of Hides and Skins","6. Other activities ","Post treatment","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Water","Total Suspended Solids (TSS) ","In order to reduce emissions to receiving waters, BAT is to apply waste water treatment comprising an appropriate on-site and/or off-site combination of the following techniques:\n(i) mechanical treatment;\n(ii) physico-chemical treatment;\n(iii) biological treatment;\n(iv) biological nitrogen elimination.","mg/l","N/A",35,"Green","Monitoring of chemical oxygen demand (COD), biochemical oxygen demand (BOD) and ammoniacal nitrogen after on-site or off-site effluent treatment for direct discharges to receiving water, by using flow-proportional 24-hour composite samples. Monitoring of total suspended solids after on-site or off-site effluent treatment for direct discharges to receiving water.",0,0,"Unspecified ",0,0]
["Tanning of Hides and Skins","6. Other activities ","Post treatment","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Water","Total chromium (as Cr)","In order to reduce emissions to receiving waters, BAT is to apply waste water treatment comprising an appropriate on-site and/or off-site combination of the following techniques:\n(i) mechanical treatment;\n(ii) physico-chemical treatment;\n(iii) biological treatment;\n(iv) biological nitrogen elimination.","mg/l",0.3,1,"Green","Monitoring of the sulphide concentration and total chromium concentration in the final effluent after treatment for direct discharge to receiving water, by using flow proportional 24-hour composite samples. Monitoring of the sulphide concentration and total chromium concentration after chromium precipitation for indirect discharge, by using flow proportional 24-hour composite samples.",0,0,"Unspecified ","monthly average values based on the average of the 24-hour representative composite samples taken over a month)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Tanning of Hides and Skins","6. Other activities ","Post treatment","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Water","Total chromium (as Cr)","In order to reduce emissions to receiving waters, BAT is to apply waste water treatment comprising an appropriate on-site and/or off-site combination of the following techniques:\n(i) mechanical treatment;\n(ii) physico-chemical treatment;\n(iii) biological treatment;\n(iv) biological nitrogen elimination.","mg/l",0.3,1,"Green","Monitoring of the sulphide concentration and total chromium concentration in the final effluent after treatment for direct discharge to receiving water, by using flow proportional 24-hour composite samples. Monitoring of the sulphide concentration and total chromium concentration after chromium precipitation for indirect discharge, by using flow proportional 24-hour composite samples.",0,0,"Unspecified ","monthly average values based on the average of the 24-hour representative composite samples taken over a month)",0]
["Tanning of Hides and Skins","6. Other activities ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Indirect discharges of waste water from tanneries into urban waste water treatment plants ","Water","Total chromium (as Cr)","In order to reduce total chromium and sulphide emissions through indirect discharges of waste water from tanneries into urban waste water treatment plants, BAT is to apply chromium precipitation and sulphide oxidation.","mg/l",0.3,1,"Green","Monitoring of the sulphide concentration and total chromium concentration in the final effluent after treatment for direct discharge to receiving water, by using flow proportional 24-hour composite samples. Monitoring of the sulphide concentration and total chromium concentration after chromium precipitation for indirect discharge, by using flow proportional 24-hour composite samples.",0,0,"Unspecified ","monthly average values based on the average of the 24-hour representative composite samples taken over a month","BAT-AELs for total chromium and sulphide emissions through indirect discharges of waste water from tanneries into urban waste water treatment plants",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Tanning of Hides and Skins","6. Other activities ","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Indirect discharges of waste water from tanneries into urban waste water treatment plants ","Water","Total chromium (as Cr)","In order to reduce total chromium and sulphide emissions through indirect discharges of waste water from tanneries into urban waste water treatment plants, BAT is to apply chromium precipitation and sulphide oxidation.","mg/l",0.3,1,"Green","Monitoring of the sulphide concentration and total chromium concentration in the final effluent after treatment for direct discharge to receiving water, by using flow proportional 24-hour composite samples. Monitoring of the sulphide concentration and total chromium concentration after chromium precipitation for indirect discharge, by using flow proportional 24-hour composite samples.",0,0,"Unspecified ","monthly average values based on the average of the 24-hour representative composite samples taken over a month","BAT-AELs for total chromium and sulphide emissions through indirect discharges of waste water from tanneries into urban waste water treatment plants"]
["Woodbased Panels Production","6.   Other activities","Unspecified","Fibre","Unspecified","Unspecified","Unspecified","Unspecified","Dryer- all types ","Air","Particulates (PM10) (24 hr Mean)","In order to prevent or reduce emissions to air from the dryer, BAT is to achieve and manage a balanced operation of the\ndrying process and to use one or a combination of the techniques given below: (i) Dust abatement of inlet hot gas to a\ndirectly heated dryer in combination with one or a combination of the other techniques listed below; (ii) Bag filter; (iii) Cyclone; (iv) UTWS dryer and combustion with heat exchanger and thermal treatment of discharged dryer waste gasl (v) Wet electrostatic precipitator; (vi) Wet scrubber; (vii) Bioscrubber; (viii) Chemical degradation or capture of formaldehyde with chemicals in combination with a wet scrubbing system \n\n","mg/Nm3",3,20,"Green","Periodic (at least once every 6 months)",0,0,"N/A","Average over sampling period ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Woodbased Panels Production","6.   Other activities","Unspecified","Fibre","Unspecified","Unspecified","Unspecified","Unspecified","Dryer- all types ","Air","Particulates (PM10) (24 hr Mean)","In order to prevent or reduce emissions to air from the dryer, BAT is to achieve and manage a balanced operation of the\ndrying process and to use one or a combination of the techniques given below: (i) Dust abatement of inlet hot gas to a\ndirectly heated dryer in combination with one or a combination of the other techniques listed below; (ii) Bag filter; (iii) Cyclone; (iv) UTWS dryer and combustion with heat exchanger and thermal treatment of discharged dryer waste gasl (v) Wet electrostatic precipitator; (vi) Wet scrubber; (vii) Bioscrubber; (viii) Chemical degradation or capture of formaldehyde with chemicals in combination with a wet scrubbing system \n\n","mg/Nm3",3,20,"Green","Periodic (at least once every 6 months)",0,0,"N/A","Average over sampling period ",0]
["Woodbased Panels Production","6.   Other activities","Unspecified","PB or OSB","Unspecified","Unspecified","Unspecified","Unspecified","Dryer- Directly heated","Air","Particulates (PM10) (24 hr Mean)","In order to prevent or reduce emissions to air from the dryer, BAT is to achieve and manage a balanced operation of the\ndrying process and to use one or a combination of the techniques given below: (i) Dust abatement of inlet hot gas to a\ndirectly heated dryer in combination with one or a combination of the other techniques listed below; (ii) Bag filter; (iii) Cyclone; (iv) UTWS dryer and combustion with heat exchanger and thermal treatment of discharged dryer waste gasl (v) Wet electrostatic precipitator; (vi) Wet scrubber; (vii) Bioscrubber; (viii) Chemical degradation or capture of formaldehyde with chemicals in combination with a wet scrubbing system \n\n","mg/Nm3",3,30,"Green","Periodic (at least once every 6 months)",0,0,0.15,"Average over sampling period ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Woodbased Panels Production","6.   Other activities","Unspecified","PB or OSB","Unspecified","Unspecified","Unspecified","Unspecified","Dryer- Directly heated","Air","Particulates (PM10) (24 hr Mean)","In order to prevent or reduce emissions to air from the dryer, BAT is to achieve and manage a balanced operation of the\ndrying process and to use one or a combination of the techniques given below: (i) Dust abatement of inlet hot gas to a\ndirectly heated dryer in combination with one or a combination of the other techniques listed below; (ii) Bag filter; (iii) Cyclone; (iv) UTWS dryer and combustion with heat exchanger and thermal treatment of discharged dryer waste gasl (v) Wet electrostatic precipitator; (vi) Wet scrubber; (vii) Bioscrubber; (viii) Chemical degradation or capture of formaldehyde with chemicals in combination with a wet scrubbing system \n\n","mg/Nm3",3,30,"Green","Periodic (at least once every 6 months)",0,0,0.15,"Average over sampling period ",0]
["Woodbased Panels Production","6.   Other activities","Unspecified","PB or OSB","Unspecified","Unspecified","Unspecified","Unspecified","Dryer-Indirectly heated ","Air","Particulates (PM10) (24 hr Mean)","In order to prevent or reduce emissions to air from the dryer, BAT is to achieve and manage a balanced operation of the\ndrying process and to use one or a combination of the techniques given below: (i) Dust abatement of inlet hot gas to a\ndirectly heated dryer in combination with one or a combination of the other techniques listed below; (ii) Bag filter; (iii) Cyclone; (iv) UTWS dryer and combustion with heat exchanger and thermal treatment of discharged dryer waste gasl (v) Wet electrostatic precipitator; (vi) Wet scrubber; (vii) Bioscrubber; (viii) Chemical degradation or capture of formaldehyde with chemicals in combination with a wet scrubbing system \n\n","mg/Nm3",3,10,"Green","Periodic (at least once every 6 months)",0,0,0.15,"Average over sampling period ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Woodbased Panels Production","6.   Other activities","Unspecified","PB or OSB","Unspecified","Unspecified","Unspecified","Unspecified","Dryer-Indirectly heated ","Air","Particulates (PM10) (24 hr Mean)","In order to prevent or reduce emissions to air from the dryer, BAT is to achieve and manage a balanced operation of the\ndrying process and to use one or a combination of the techniques given below: (i) Dust abatement of inlet hot gas to a\ndirectly heated dryer in combination with one or a combination of the other techniques listed below; (ii) Bag filter; (iii) Cyclone; (iv) UTWS dryer and combustion with heat exchanger and thermal treatment of discharged dryer waste gasl (v) Wet electrostatic precipitator; (vi) Wet scrubber; (vii) Bioscrubber; (viii) Chemical degradation or capture of formaldehyde with chemicals in combination with a wet scrubbing system \n\n","mg/Nm3",3,10,"Green","Periodic (at least once every 6 months)",0,0,0.15,"Average over sampling period ",0]
["Woodbased Panels Production","6.   Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Press","Air","Particulates (PM10) (24 hr Mean)","In order to prevent or reduce emissions to air from the press, BAT is to use in-duct quenching of collected press waste gas and an appropriate combination of the techniques given below.: (i) Select resins with a low formaldehyde content; (ii) Controlled operation of the press with balanced press temperature, applied pressure and press speed; (iii) Wet scrubbing of collected press\nwaste gases using Venturi scrubbers or hydrocyclones, etc.; (iv) Wet electrostatic precipitator; (v) Bioscrubber; (vi) Post-combustion as the last treatment step after application of a wet scrubber ","mg/Nm3",3,15,"Green","Periodic (at least once every 6 months)",0,0,"N/A","Average over sampling period ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Woodbased Panels Production","6.   Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Press","Air","Particulates (PM10) (24 hr Mean)","In order to prevent or reduce emissions to air from the press, BAT is to use in-duct quenching of collected press waste gas and an appropriate combination of the techniques given below.: (i) Select resins with a low formaldehyde content; (ii) Controlled operation of the press with balanced press temperature, applied pressure and press speed; (iii) Wet scrubbing of collected press\nwaste gases using Venturi scrubbers or hydrocyclones, etc.; (iv) Wet electrostatic precipitator; (v) Bioscrubber; (vi) Post-combustion as the last treatment step after application of a wet scrubber ","mg/Nm3",3,15,"Green","Periodic (at least once every 6 months)",0,0,"N/A","Average over sampling period ",0]
["Woodbased Panels Production","6.   Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Upstream and downstream wood processing, conveying of wood materials and mat forming ","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust emissions to air from upstream and downstream wood processing, conveying of wood materials and mat forming, BAT is to use either a bag filter or a cyclofilter.","mg/Nm3",3,5,"Green","Periodic (at least once a year)",0,0,"N/A","Average over sampling period ","When a bag filter or a cyclofilter is not applicable, the upper end of the range can be up to 10 mg/Nm3",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Woodbased Panels Production","6.   Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Upstream and downstream wood processing, conveying of wood materials and mat forming ","Air","Particulates (PM10) (24 hr Mean)","In order to reduce dust emissions to air from upstream and downstream wood processing, conveying of wood materials and mat forming, BAT is to use either a bag filter or a cyclofilter.","mg/Nm3",3,5,"Green","Periodic (at least once a year)",0,0,"N/A","Average over sampling period ","When a bag filter or a cyclofilter is not applicable, the upper end of the range can be up to 10 mg/Nm3"]
["Woodbased Panels Production","6.   Other activities","Unspecified","Fibre","Unspecified","Unspecified","Unspecified","Unspecified","Dryer- all types ","Air","Formaldehyde","In order to prevent or reduce emissions to air from the dryer, BAT is to achieve and manage a balanced operation of the\ndrying process and to use one or a combination of the techniques given below: (i) Dust abatement of inlet hot gas to a\ndirectly heated dryer in combination with one or a combination of the other techniques listed below; (ii) Bag filter; (iii) Cyclone; (iv) UTWS dryer and combustion with heat exchanger and thermal treatment of discharged dryer waste gasl (v) Wet electrostatic precipitator; (vi) Wet scrubber; (vii) Bioscrubber; (viii) Chemical degradation or capture of formaldehyde with chemicals in combination with a wet scrubbing system \n\n","mg/Nm3",5,15,"Green","Periodic (at least once every 6 months)",0,0,"N/A","Average over sampling period ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Woodbased Panels Production","6.   Other activities","Unspecified","Fibre","Unspecified","Unspecified","Unspecified","Unspecified","Dryer- all types ","Air","Formaldehyde","In order to prevent or reduce emissions to air from the dryer, BAT is to achieve and manage a balanced operation of the\ndrying process and to use one or a combination of the techniques given below: (i) Dust abatement of inlet hot gas to a\ndirectly heated dryer in combination with one or a combination of the other techniques listed below; (ii) Bag filter; (iii) Cyclone; (iv) UTWS dryer and combustion with heat exchanger and thermal treatment of discharged dryer waste gasl (v) Wet electrostatic precipitator; (vi) Wet scrubber; (vii) Bioscrubber; (viii) Chemical degradation or capture of formaldehyde with chemicals in combination with a wet scrubbing system \n\n","mg/Nm3",5,15,"Green","Periodic (at least once every 6 months)",0,0,"N/A","Average over sampling period ",0]
["Woodbased Panels Production","6.   Other activities","Unspecified","OSB","Unspecified","Unspecified","Unspecified","Unspecified","Dryer- all types ","Air","Formaldehyde","In order to prevent or reduce emissions to air from the dryer, BAT is to achieve and manage a balanced operation of the\ndrying process and to use one or a combination of the techniques given below: (i) Dust abatement of inlet hot gas to a\ndirectly heated dryer in combination with one or a combination of the other techniques listed below; (ii) Bag filter; (iii) Cyclone; (iv) UTWS dryer and combustion with heat exchanger and thermal treatment of discharged dryer waste gasl (v) Wet electrostatic precipitator; (vi) Wet scrubber; (vii) Bioscrubber; (viii) Chemical degradation or capture of formaldehyde with chemicals in combination with a wet scrubbing system \n\n","mg/Nm3",5,20,"Green","Periodic (at least once every 6 months)",0,0,0.15,"Average over sampling period ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Woodbased Panels Production","6.   Other activities","Unspecified","OSB","Unspecified","Unspecified","Unspecified","Unspecified","Dryer- all types ","Air","Formaldehyde","In order to prevent or reduce emissions to air from the dryer, BAT is to achieve and manage a balanced operation of the\ndrying process and to use one or a combination of the techniques given below: (i) Dust abatement of inlet hot gas to a\ndirectly heated dryer in combination with one or a combination of the other techniques listed below; (ii) Bag filter; (iii) Cyclone; (iv) UTWS dryer and combustion with heat exchanger and thermal treatment of discharged dryer waste gasl (v) Wet electrostatic precipitator; (vi) Wet scrubber; (vii) Bioscrubber; (viii) Chemical degradation or capture of formaldehyde with chemicals in combination with a wet scrubbing system \n\n","mg/Nm3",5,20,"Green","Periodic (at least once every 6 months)",0,0,0.15,"Average over sampling period ",0]
["Woodbased Panels Production","6.   Other activities","Unspecified","PB","Unspecified","Unspecified","Unspecified","Unspecified","Dryer- all types ","Air","Formaldehyde","In order to prevent or reduce emissions to air from the dryer, BAT is to achieve and manage a balanced operation of the\ndrying process and to use one or a combination of the techniques given below: (i) Dust abatement of inlet hot gas to a\ndirectly heated dryer in combination with one or a combination of the other techniques listed below; (ii) Bag filter; (iii) Cyclone; (iv) UTWS dryer and combustion with heat exchanger and thermal treatment of discharged dryer waste gasl (v) Wet electrostatic precipitator; (vi) Wet scrubber; (vii) Bioscrubber; (viii) Chemical degradation or capture of formaldehyde with chemicals in combination with a wet scrubbing system \n\n","mg/Nm3",5,10,"Green","Periodic (at least once every 6 months)",0,0,0.15,"Average over sampling period ","When using almost exclusively recovered wood, the upper end of the range may be up to 15 mg/Nm3",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Woodbased Panels Production","6.   Other activities","Unspecified","PB","Unspecified","Unspecified","Unspecified","Unspecified","Dryer- all types ","Air","Formaldehyde","In order to prevent or reduce emissions to air from the dryer, BAT is to achieve and manage a balanced operation of the\ndrying process and to use one or a combination of the techniques given below: (i) Dust abatement of inlet hot gas to a\ndirectly heated dryer in combination with one or a combination of the other techniques listed below; (ii) Bag filter; (iii) Cyclone; (iv) UTWS dryer and combustion with heat exchanger and thermal treatment of discharged dryer waste gasl (v) Wet electrostatic precipitator; (vi) Wet scrubber; (vii) Bioscrubber; (viii) Chemical degradation or capture of formaldehyde with chemicals in combination with a wet scrubbing system \n\n","mg/Nm3",5,10,"Green","Periodic (at least once every 6 months)",0,0,0.15,"Average over sampling period ","When using almost exclusively recovered wood, the upper end of the range may be up to 15 mg/Nm3"]
["Woodbased Panels Production","6.   Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Press","Air","Formaldehyde","In order to prevent or reduce emissions to air from the press, BAT is to use in-duct quenching of collected press waste gas and an appropriate combination of the techniques given below.: (i) Select resins with a low formaldehyde content; (ii) Controlled operation of the press with balanced press temperature, applied pressure and press speed; (iii) Wet scrubbing of collected press\nwaste gases using Venturi scrubbers or hydrocyclones, etc.; (iv) Wet electrostatic precipitator; (v) Bioscrubber; (vi) Post-combustion as the last treatment step after application of a wet scrubber ","mg/Nm3",2,15,"Green","Periodic (at least once every 6 months)",0,0,"N/A","Average over sampling period ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Woodbased Panels Production","6.   Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Press","Air","Formaldehyde","In order to prevent or reduce emissions to air from the press, BAT is to use in-duct quenching of collected press waste gas and an appropriate combination of the techniques given below.: (i) Select resins with a low formaldehyde content; (ii) Controlled operation of the press with balanced press temperature, applied pressure and press speed; (iii) Wet scrubbing of collected press\nwaste gases using Venturi scrubbers or hydrocyclones, etc.; (iv) Wet electrostatic precipitator; (v) Bioscrubber; (vi) Post-combustion as the last treatment step after application of a wet scrubber ","mg/Nm3",2,15,"Green","Periodic (at least once every 6 months)",0,0,"N/A","Average over sampling period ",0]
["Woodbased Panels Production","6.   Other activities","Unspecified","Impregnation of paper ","Unspecified","Unspecified","Unspecified","Unspecified","Drying oven","Air","Formaldehyde","In order to reduce emissions of volatile organic compounds to air from the drying ovens for the impregnation of paper, BAT is to use one or a combination of the techniques given below: (i) Select and use resins with a low formaldehyde content; (ii) Controlled operation of ovens with balanced temperature\nand speed; (iii) Thermal oxidation of waste gas in a regenerative thermal\noxidiser or a catalytic thermal oxidiser; (iv) Post-combustion or incineration of waste gas in a\ncombustion plant ; (v) Wet scrubbing of waste gas followed by treatment in a\nbiofilter","mg/Nm3",5,10,"Green","Periodic (at least once a year)",0,0,"N/A","Average over sampling period ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Woodbased Panels Production","6.   Other activities","Unspecified","Impregnation of paper ","Unspecified","Unspecified","Unspecified","Unspecified","Drying oven","Air","Formaldehyde","In order to reduce emissions of volatile organic compounds to air from the drying ovens for the impregnation of paper, BAT is to use one or a combination of the techniques given below: (i) Select and use resins with a low formaldehyde content; (ii) Controlled operation of ovens with balanced temperature\nand speed; (iii) Thermal oxidation of waste gas in a regenerative thermal\noxidiser or a catalytic thermal oxidiser; (iv) Post-combustion or incineration of waste gas in a\ncombustion plant ; (v) Wet scrubbing of waste gas followed by treatment in a\nbiofilter","mg/Nm3",5,10,"Green","Periodic (at least once a year)",0,0,"N/A","Average over sampling period ",0]
["Woodbased Panels Production","6.   Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Dryer- Directly heated","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from directly heated dryers, BAT is to use technique (i) or technique (i) in combination with technique (ii): (i) Efficient operation of the combustion process using\nair- and fuel-staged combustion, while applying pulverised\ncombustion, fluidised bed boilers or moving\ngrate firing; (ii) Selective non-catalytic reduction (SNCR) by injection\nand reaction with urea or liquid ammonia","mg/Nm3",30,250,"Green","Periodic (at least once every 6 months)",0,0,"Unspecified ","Average over sampling period ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Woodbased Panels Production","6.   Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Dryer- Directly heated","Air","Nitrogen dioxide","In order to prevent or reduce NOX emissions to air from directly heated dryers, BAT is to use technique (i) or technique (i) in combination with technique (ii): (i) Efficient operation of the combustion process using\nair- and fuel-staged combustion, while applying pulverised\ncombustion, fluidised bed boilers or moving\ngrate firing; (ii) Selective non-catalytic reduction (SNCR) by injection\nand reaction with urea or liquid ammonia","mg/Nm3",30,250,"Green","Periodic (at least once every 6 months)",0,0,"Unspecified ","Average over sampling period ",0]
["Woodbased Panels Production","6.   Other activities","Unspecified","Fibre","Unspecified","Unspecified","Unspecified","Unspecified","Dryer- all types ","Air","VOC","In order to prevent or reduce emissions to air from the dryer, BAT is to achieve and manage a balanced operation of the\ndrying process and to use one or a combination of the techniques given below: (i) Dust abatement of inlet hot gas to a\ndirectly heated dryer in combination with one or a combination of the other techniques listed below; (ii) Bag filter; (iii) Cyclone; (iv) UTWS dryer and combustion with heat exchanger and thermal treatment of discharged dryer waste gasl (v) Wet electrostatic precipitator; (vi) Wet scrubber; (vii) Bioscrubber; (viii) Chemical degradation or capture of formaldehyde with chemicals in combination with a wet scrubbing system \n\n","mg/Nm3",20,120,"Green","Periodic (at least once every 6 months)",0,0,"N/A","Average over sampling period ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Woodbased Panels Production","6.   Other activities","Unspecified","Fibre","Unspecified","Unspecified","Unspecified","Unspecified","Dryer- all types ","Air","VOC","In order to prevent or reduce emissions to air from the dryer, BAT is to achieve and manage a balanced operation of the\ndrying process and to use one or a combination of the techniques given below: (i) Dust abatement of inlet hot gas to a\ndirectly heated dryer in combination with one or a combination of the other techniques listed below; (ii) Bag filter; (iii) Cyclone; (iv) UTWS dryer and combustion with heat exchanger and thermal treatment of discharged dryer waste gasl (v) Wet electrostatic precipitator; (vi) Wet scrubber; (vii) Bioscrubber; (viii) Chemical degradation or capture of formaldehyde with chemicals in combination with a wet scrubbing system \n\n","mg/Nm3",20,120,"Green","Periodic (at least once every 6 months)",0,0,"N/A","Average over sampling period ",0]
["Woodbased Panels Production","6.   Other activities","Unspecified","Impregnation of paper ","Unspecified","Unspecified","Unspecified","Unspecified","Drying oven","Air","VOC","In order to reduce emissions of volatile organic compounds to air from the drying ovens for the impregnation of paper, BAT is to use one or a combination of the techniques given below: (i) Select and use resins with a low formaldehyde content; (ii) Controlled operation of ovens with balanced temperature\nand speed; (iii) Thermal oxidation of waste gas in a regenerative thermal\noxidiser or a catalytic thermal oxidiser; (iv) Post-combustion or incineration of waste gas in a\ncombustion plant ; (v) Wet scrubbing of waste gas followed by treatment in a\nbiofilter","mg/Nm3",5,30,"Green","Periodic (at least once a year)",0,0,"N/A","Average over sampling period ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Woodbased Panels Production","6.   Other activities","Unspecified","Impregnation of paper ","Unspecified","Unspecified","Unspecified","Unspecified","Drying oven","Air","VOC","In order to reduce emissions of volatile organic compounds to air from the drying ovens for the impregnation of paper, BAT is to use one or a combination of the techniques given below: (i) Select and use resins with a low formaldehyde content; (ii) Controlled operation of ovens with balanced temperature\nand speed; (iii) Thermal oxidation of waste gas in a regenerative thermal\noxidiser or a catalytic thermal oxidiser; (iv) Post-combustion or incineration of waste gas in a\ncombustion plant ; (v) Wet scrubbing of waste gas followed by treatment in a\nbiofilter","mg/Nm3",5,30,"Green","Periodic (at least once a year)",0,0,"N/A","Average over sampling period ",0]
["Woodbased Panels Production","6.   Other activities","Unspecified","OSB","Unspecified","Unspecified","Unspecified","Unspecified","Dryer- all types ","Air","VOC","In order to prevent or reduce emissions to air from the dryer, BAT is to achieve and manage a balanced operation of the\ndrying process and to use one or a combination of the techniques given below: (i) Dust abatement of inlet hot gas to a\ndirectly heated dryer in combination with one or a combination of the other techniques listed below; (ii) Bag filter; (iii) Cyclone; (iv) UTWS dryer and combustion with heat exchanger and thermal treatment of discharged dryer waste gasl (v) Wet electrostatic precipitator; (vi) Wet scrubber; (vii) Bioscrubber; (viii) Chemical degradation or capture of formaldehyde with chemicals in combination with a wet scrubbing system \n\n","mg/Nm3",10,400,"Green","Periodic (at least once every 6 months)",0,0,0.15,"Average over sampling period ","Emissions below 30 mg/Nm3 can be achieved using UTWS dryer.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Woodbased Panels Production","6.   Other activities","Unspecified","OSB","Unspecified","Unspecified","Unspecified","Unspecified","Dryer- all types ","Air","VOC","In order to prevent or reduce emissions to air from the dryer, BAT is to achieve and manage a balanced operation of the\ndrying process and to use one or a combination of the techniques given below: (i) Dust abatement of inlet hot gas to a\ndirectly heated dryer in combination with one or a combination of the other techniques listed below; (ii) Bag filter; (iii) Cyclone; (iv) UTWS dryer and combustion with heat exchanger and thermal treatment of discharged dryer waste gasl (v) Wet electrostatic precipitator; (vi) Wet scrubber; (vii) Bioscrubber; (viii) Chemical degradation or capture of formaldehyde with chemicals in combination with a wet scrubbing system \n\n","mg/Nm3",10,400,"Green","Periodic (at least once every 6 months)",0,0,0.15,"Average over sampling period ","Emissions below 30 mg/Nm3 can be achieved using UTWS dryer."]
["Woodbased Panels Production","6.   Other activities","Unspecified","PB","Unspecified","Unspecified","Unspecified","Unspecified","Dryer- all types ","Air","VOC","In order to prevent or reduce emissions to air from the dryer, BAT is to achieve and manage a balanced operation of the\ndrying process and to use one or a combination of the techniques given below: (i) Dust abatement of inlet hot gas to a\ndirectly heated dryer in combination with one or a combination of the other techniques listed below; (ii) Bag filter; (iii) Cyclone; (iv) UTWS dryer and combustion with heat exchanger and thermal treatment of discharged dryer waste gasl (v) Wet electrostatic precipitator; (vi) Wet scrubber; (vii) Bioscrubber; (viii) Chemical degradation or capture of formaldehyde with chemicals in combination with a wet scrubbing system \n\n","mg/Nm3",20,200,"Green","Periodic (at least once every 6 months)",0,0,0.15,"Average over sampling period ","This BAT-AEL does not apply when using pine as the predominant raw material. \n\nEmissions below 30 mg/Nm3 can be achieved using UTWS dryer. \n",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Woodbased Panels Production","6.   Other activities","Unspecified","PB","Unspecified","Unspecified","Unspecified","Unspecified","Dryer- all types ","Air","VOC","In order to prevent or reduce emissions to air from the dryer, BAT is to achieve and manage a balanced operation of the\ndrying process and to use one or a combination of the techniques given below: (i) Dust abatement of inlet hot gas to a\ndirectly heated dryer in combination with one or a combination of the other techniques listed below; (ii) Bag filter; (iii) Cyclone; (iv) UTWS dryer and combustion with heat exchanger and thermal treatment of discharged dryer waste gasl (v) Wet electrostatic precipitator; (vi) Wet scrubber; (vii) Bioscrubber; (viii) Chemical degradation or capture of formaldehyde with chemicals in combination with a wet scrubbing system \n\n","mg/Nm3",20,200,"Green","Periodic (at least once every 6 months)",0,0,0.15,"Average over sampling period ","This BAT-AEL does not apply when using pine as the predominant raw material. \n\nEmissions below 30 mg/Nm3 can be achieved using UTWS dryer. \n"]
["Woodbased Panels Production","6.   Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Press","Air","VOC","In order to prevent or reduce emissions to air from the press, BAT is to use in-duct quenching of collected press waste gas and an appropriate combination of the techniques given below.: (i) Select resins with a low formaldehyde content; (ii) Controlled operation of the press with balanced press temperature, applied pressure and press speed; (iii) Wet scrubbing of collected press\nwaste gases using Venturi scrubbers or hydrocyclones, etc.; (iv) Wet electrostatic precipitator; (v) Bioscrubber; (vi) Post-combustion as the last treatment step after application of a wet scrubber ","mg/Nm3",10,100,"Green","Periodic (at least once every 6 months)",0,0,"N/A","Average over sampling period ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Woodbased Panels Production","6.   Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Press","Air","VOC","In order to prevent or reduce emissions to air from the press, BAT is to use in-duct quenching of collected press waste gas and an appropriate combination of the techniques given below.: (i) Select resins with a low formaldehyde content; (ii) Controlled operation of the press with balanced press temperature, applied pressure and press speed; (iii) Wet scrubbing of collected press\nwaste gases using Venturi scrubbers or hydrocyclones, etc.; (iv) Wet electrostatic precipitator; (v) Bioscrubber; (vi) Post-combustion as the last treatment step after application of a wet scrubber ","mg/Nm3",10,100,"Green","Periodic (at least once every 6 months)",0,0,"N/A","Average over sampling period ",0]
["Woodbased Panels Production","6.   Other activities","Unspecified","Wood fibre","Unspecified","Unspecified","Unspecified","Unspecified","All plant","Water","COD","In order to reduce emissions to water from wood fibre production, BAT is to use a combination of the techniques given below: (i) Mechanical separation of coarse materials by screens\nand sieves; (ii) Physico-chemical separation, e.g. using sand filters,\ndissolved air flotation, coagulation and flocculation; (iii) Biological treatment","mg/l",20,200,"Green","Periodic (at least once a week) ",0,0,"N/A","Average of samples obtained during one year ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Woodbased Panels Production","6.   Other activities","Unspecified","Wood fibre","Unspecified","Unspecified","Unspecified","Unspecified","All plant","Water","COD","In order to reduce emissions to water from wood fibre production, BAT is to use a combination of the techniques given below: (i) Mechanical separation of coarse materials by screens\nand sieves; (ii) Physico-chemical separation, e.g. using sand filters,\ndissolved air flotation, coagulation and flocculation; (iii) Biological treatment","mg/l",20,200,"Green","Periodic (at least once a week) ",0,0,"N/A","Average of samples obtained during one year ",0]
["Woodbased Panels Production","6.   Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Surface run-off ","Water","Total Suspended Solids (TSS) ","In order to reduce emissions to water from surface run-off water, BAT is to use a combination of the techniques given below: (i) Mechanical separation of coarse materials by screens\nand sieves as preliminary treatment; (ii) Oil-water separation; (iii) Removal of solids by sedimentation in retention basins\nor settlement tanks","mg/l",10,40,"Green","Periodic (at least once every 3 months) ",0,0,"N/A","Average of samples obtained during one year ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Woodbased Panels Production","6.   Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Surface run-off ","Water","Total Suspended Solids (TSS) ","In order to reduce emissions to water from surface run-off water, BAT is to use a combination of the techniques given below: (i) Mechanical separation of coarse materials by screens\nand sieves as preliminary treatment; (ii) Oil-water separation; (iii) Removal of solids by sedimentation in retention basins\nor settlement tanks","mg/l",10,40,"Green","Periodic (at least once every 3 months) ",0,0,"N/A","Average of samples obtained during one year ",0]
["Woodbased Panels Production","6.   Other activities","Unspecified","Wood fibre","Unspecified","Unspecified","Unspecified","Unspecified","All plant","Water","Total Suspended Solids (TSS) ","In order to reduce emissions to water from wood fibre production, BAT is to use a combination of the techniques given below: (i) Mechanical separation of coarse materials by screens\nand sieves; (ii) Physico-chemical separation, e.g. using sand filters,\ndissolved air flotation, coagulation and flocculation; (iii) Biological treatment","mg/l",5,35,"Green","Periodic (at least once a week) ",0,0,"N/A","Average of samples obtained during one year ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Woodbased Panels Production","6.   Other activities","Unspecified","Wood fibre","Unspecified","Unspecified","Unspecified","Unspecified","All plant","Water","Total Suspended Solids (TSS) ","In order to reduce emissions to water from wood fibre production, BAT is to use a combination of the techniques given below: (i) Mechanical separation of coarse materials by screens\nand sieves; (ii) Physico-chemical separation, e.g. using sand filters,\ndissolved air flotation, coagulation and flocculation; (iii) Biological treatment","mg/l",5,35,"Green","Periodic (at least once a week) ",0,0,"N/A","Average of samples obtained during one year ",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Copper","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Cadmium and its compounds (≥ 200 mg/l CaCO3)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l",0.02,0.1,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Copper","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Cadmium and its compounds (≥ 200 mg/l CaCO3)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l",0.02,0.1,"Green","Once per month",0,0,0,"Daily average",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Ferro alloys Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Cadmium and its compounds (≥ 200 mg/l CaCO3)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.05,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Ferro alloys Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Cadmium and its compounds (≥ 200 mg/l CaCO3)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.05,"Green","Once per month",0,0,0,"Daily average",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Lead and Tin Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Cadmium and its compounds (≥ 200 mg/l CaCO3)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.1,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Lead and Tin Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Cadmium and its compounds (≥ 200 mg/l CaCO3)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.1,"Green","Once per month",0,0,0,"Daily average",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Nickel and Cobalt Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Cadmium and its compounds (≥ 200 mg/l CaCO3)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.1,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Nickel and Cobalt Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Cadmium and its compounds (≥ 200 mg/l CaCO3)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.1,"Green","Once per month",0,0,0,"Daily average",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Precious metals","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Cadmium and its compounds (≥ 200 mg/l CaCO3)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.05,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Precious metals","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Cadmium and its compounds (≥ 200 mg/l CaCO3)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.05,"Green","Once per month",0,0,0,"Daily average",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Zinc and Cadmium Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Cadmium and its compounds (≥ 200 mg/l CaCO3)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.1,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Zinc and Cadmium Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Cadmium and its compounds (≥ 200 mg/l CaCO3)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.1,"Green","Once per month",0,0,0,"Daily average",0]
["Refineries","1. Energy industries","Unspecified","Unspecified","All","Unspecified","All","Unspecified","Whole refinery ","Water","Cadmium and its compounds (≥ 200 mg/l CaCO3)","Removal of insoluble substances by recovering oil: \n— API Separators (APIs)\n— Corrugated Plate Interceptors (CPIs)\n— Parallel Plate Interceptors (PPIs)\n— Tilted Plate Interceptors (TPIs)\n— Buffer and/or equalisation tanks \n\nRemoval of insoluble substances by recovering suspended solid and dispersed oil:\nThese techniques generally include:\n— Dissolved Gas Flotation (DGF)\n— Induced Gas Flotation (IGF)\n— Sand Filtration \n\nRemoval of soluble substances including biological treatment and clarification:\nBiological treatment techniques may include:\n— Fixed bed systems\n— Suspended bed systems.\nOne of the most commonly used suspended bed system in refineries WWTP is\nthe activated sludge process. Fixed bed systems may include a biofilter or trickling\nfilter\n\nAdditional treatment step:\nA specific waste water treatment intended to complement the previous treatment\nsteps e.g. for further reducing nitrogen or carbon compounds. Generally used\nwhere specific local requirements for water preservation exist\n","mg/l",2E-3,8.0000000000000002E-3,"Green","Quarterly",0,0,"N/A","Yearly ","Refers to a flow-proportional composite sample taken over a period of 24 hours or, provided that sufficient flow stability is demonstrated, a time-proportional sample.\n\nNot all parameters and sampling frequencies are applicable to effluent from gas refining sites",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Refineries","1. Energy industries","Unspecified","Unspecified","All","Unspecified","All","Unspecified","Whole refinery ","Water","Cadmium and its compounds (≥ 200 mg/l CaCO3)","Removal of insoluble substances by recovering oil: \n— API Separators (APIs)\n— Corrugated Plate Interceptors (CPIs)\n— Parallel Plate Interceptors (PPIs)\n— Tilted Plate Interceptors (TPIs)\n— Buffer and/or equalisation tanks \n\nRemoval of insoluble substances by recovering suspended solid and dispersed oil:\nThese techniques generally include:\n— Dissolved Gas Flotation (DGF)\n— Induced Gas Flotation (IGF)\n— Sand Filtration \n\nRemoval of soluble substances including biological treatment and clarification:\nBiological treatment techniques may include:\n— Fixed bed systems\n— Suspended bed systems.\nOne of the most commonly used suspended bed system in refineries WWTP is\nthe activated sludge process. Fixed bed systems may include a biofilter or trickling\nfilter\n\nAdditional treatment step:\nA specific waste water treatment intended to complement the previous treatment\nsteps e.g. for further reducing nitrogen or carbon compounds. Generally used\nwhere specific local requirements for water preservation exist\n","mg/l",2E-3,8.0000000000000002E-3,"Green","Quarterly",0,0,"N/A","Yearly ","Refers to a flow-proportional composite sample taken over a period of 24 hours or, provided that sufficient flow stability is demonstrated, a time-proportional sample.\n\nNot all parameters and sampling frequencies are applicable to effluent from gas refining sites"]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Copper","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Cadmium and its compounds (100 - <200 mg/l CaCO3)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l",0.02,0.1,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Copper","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Cadmium and its compounds (100 - <200 mg/l CaCO3)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l",0.02,0.1,"Green","Once per month",0,0,0,"Daily average",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Ferro alloys Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Cadmium and its compounds (100 - <200 mg/l CaCO3)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.05,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Ferro alloys Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Cadmium and its compounds (100 - <200 mg/l CaCO3)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.05,"Green","Once per month",0,0,0,"Daily average",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Lead and Tin Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Cadmium and its compounds (100 - <200 mg/l CaCO3)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.1,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Lead and Tin Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Cadmium and its compounds (100 - <200 mg/l CaCO3)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.1,"Green","Once per month",0,0,0,"Daily average",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Nickel and Cobalt Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Cadmium and its compounds (100 - <200 mg/l CaCO3)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.1,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Nickel and Cobalt Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Cadmium and its compounds (100 - <200 mg/l CaCO3)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.1,"Green","Once per month",0,0,0,"Daily average",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Precious metals","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Cadmium and its compounds (100 - <200 mg/l CaCO3)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.05,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Precious metals","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Cadmium and its compounds (100 - <200 mg/l CaCO3)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.05,"Green","Once per month",0,0,0,"Daily average",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Zinc and Cadmium Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Cadmium and its compounds (100 - <200 mg/l CaCO3)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.1,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Zinc and Cadmium Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Cadmium and its compounds (100 - <200 mg/l CaCO3)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.1,"Green","Once per month",0,0,0,"Daily average",0]
["Refineries","1. Energy industries","Unspecified","Unspecified","All","Unspecified","All","Unspecified","Whole refinery ","Water","Cadmium and its compounds (100 - <200 mg/l CaCO3)","Removal of insoluble substances by recovering oil: \n— API Separators (APIs)\n— Corrugated Plate Interceptors (CPIs)\n— Parallel Plate Interceptors (PPIs)\n— Tilted Plate Interceptors (TPIs)\n— Buffer and/or equalisation tanks \n\nRemoval of insoluble substances by recovering suspended solid and dispersed oil:\nThese techniques generally include:\n— Dissolved Gas Flotation (DGF)\n— Induced Gas Flotation (IGF)\n— Sand Filtration \n\nRemoval of soluble substances including biological treatment and clarification:\nBiological treatment techniques may include:\n— Fixed bed systems\n— Suspended bed systems.\nOne of the most commonly used suspended bed system in refineries WWTP is\nthe activated sludge process. Fixed bed systems may include a biofilter or trickling\nfilter\n\nAdditional treatment step:\nA specific waste water treatment intended to complement the previous treatment\nsteps e.g. for further reducing nitrogen or carbon compounds. Generally used\nwhere specific local requirements for water preservation exist\n","mg/l",2E-3,8.0000000000000002E-3,"Green","Quarterly",0,0,"N/A","Yearly ","Refers to a flow-proportional composite sample taken over a period of 24 hours or, provided that sufficient flow stability is demonstrated, a time-proportional sample.\n\nNot all parameters and sampling frequencies are applicable to effluent from gas refining sites",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Refineries","1. Energy industries","Unspecified","Unspecified","All","Unspecified","All","Unspecified","Whole refinery ","Water","Cadmium and its compounds (100 - <200 mg/l CaCO3)","Removal of insoluble substances by recovering oil: \n— API Separators (APIs)\n— Corrugated Plate Interceptors (CPIs)\n— Parallel Plate Interceptors (PPIs)\n— Tilted Plate Interceptors (TPIs)\n— Buffer and/or equalisation tanks \n\nRemoval of insoluble substances by recovering suspended solid and dispersed oil:\nThese techniques generally include:\n— Dissolved Gas Flotation (DGF)\n— Induced Gas Flotation (IGF)\n— Sand Filtration \n\nRemoval of soluble substances including biological treatment and clarification:\nBiological treatment techniques may include:\n— Fixed bed systems\n— Suspended bed systems.\nOne of the most commonly used suspended bed system in refineries WWTP is\nthe activated sludge process. Fixed bed systems may include a biofilter or trickling\nfilter\n\nAdditional treatment step:\nA specific waste water treatment intended to complement the previous treatment\nsteps e.g. for further reducing nitrogen or carbon compounds. Generally used\nwhere specific local requirements for water preservation exist\n","mg/l",2E-3,8.0000000000000002E-3,"Green","Quarterly",0,0,"N/A","Yearly ","Refers to a flow-proportional composite sample taken over a period of 24 hours or, provided that sufficient flow stability is demonstrated, a time-proportional sample.\n\nNot all parameters and sampling frequencies are applicable to effluent from gas refining sites"]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Copper","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Cadmium and its compounds (40 - < 50 mg/l CaCO3)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l",0.02,0.1,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Copper","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Cadmium and its compounds (40 - < 50 mg/l CaCO3)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l",0.02,0.1,"Green","Once per month",0,0,0,"Daily average",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Ferro alloys Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Cadmium and its compounds (40 - < 50 mg/l CaCO3)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.05,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Ferro alloys Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Cadmium and its compounds (40 - < 50 mg/l CaCO3)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.05,"Green","Once per month",0,0,0,"Daily average",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Lead and Tin Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Cadmium and its compounds (40 - < 50 mg/l CaCO3)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.1,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Lead and Tin Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Cadmium and its compounds (40 - < 50 mg/l CaCO3)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.1,"Green","Once per month",0,0,0,"Daily average",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Nickel and Cobalt Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Cadmium and its compounds (40 - < 50 mg/l CaCO3)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.1,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Nickel and Cobalt Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Cadmium and its compounds (40 - < 50 mg/l CaCO3)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.1,"Green","Once per month",0,0,0,"Daily average",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Precious metals","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Cadmium and its compounds (40 - < 50 mg/l CaCO3)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.05,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Precious metals","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Cadmium and its compounds (40 - < 50 mg/l CaCO3)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.05,"Green","Once per month",0,0,0,"Daily average",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Zinc and Cadmium Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Cadmium and its compounds (40 - < 50 mg/l CaCO3)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.1,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Zinc and Cadmium Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Cadmium and its compounds (40 - < 50 mg/l CaCO3)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.1,"Green","Once per month",0,0,0,"Daily average",0]
["Refineries","1. Energy industries","Unspecified","Unspecified","All","Unspecified","All","Unspecified","Whole refinery ","Water","Cadmium and its compounds (40 - < 50 mg/l CaCO3)","Removal of insoluble substances by recovering oil: \n— API Separators (APIs)\n— Corrugated Plate Interceptors (CPIs)\n— Parallel Plate Interceptors (PPIs)\n— Tilted Plate Interceptors (TPIs)\n— Buffer and/or equalisation tanks \n\nRemoval of insoluble substances by recovering suspended solid and dispersed oil:\nThese techniques generally include:\n— Dissolved Gas Flotation (DGF)\n— Induced Gas Flotation (IGF)\n— Sand Filtration \n\nRemoval of soluble substances including biological treatment and clarification:\nBiological treatment techniques may include:\n— Fixed bed systems\n— Suspended bed systems.\nOne of the most commonly used suspended bed system in refineries WWTP is\nthe activated sludge process. Fixed bed systems may include a biofilter or trickling\nfilter\n\nAdditional treatment step:\nA specific waste water treatment intended to complement the previous treatment\nsteps e.g. for further reducing nitrogen or carbon compounds. Generally used\nwhere specific local requirements for water preservation exist\n","mg/l",2E-3,8.0000000000000002E-3,"Green","Quarterly",0,0,"N/A","Yearly ","Refers to a flow-proportional composite sample taken over a period of 24 hours or, provided that sufficient flow stability is demonstrated, a time-proportional sample.\n\nNot all parameters and sampling frequencies are applicable to effluent from gas refining sites",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Refineries","1. Energy industries","Unspecified","Unspecified","All","Unspecified","All","Unspecified","Whole refinery ","Water","Cadmium and its compounds (40 - < 50 mg/l CaCO3)","Removal of insoluble substances by recovering oil: \n— API Separators (APIs)\n— Corrugated Plate Interceptors (CPIs)\n— Parallel Plate Interceptors (PPIs)\n— Tilted Plate Interceptors (TPIs)\n— Buffer and/or equalisation tanks \n\nRemoval of insoluble substances by recovering suspended solid and dispersed oil:\nThese techniques generally include:\n— Dissolved Gas Flotation (DGF)\n— Induced Gas Flotation (IGF)\n— Sand Filtration \n\nRemoval of soluble substances including biological treatment and clarification:\nBiological treatment techniques may include:\n— Fixed bed systems\n— Suspended bed systems.\nOne of the most commonly used suspended bed system in refineries WWTP is\nthe activated sludge process. Fixed bed systems may include a biofilter or trickling\nfilter\n\nAdditional treatment step:\nA specific waste water treatment intended to complement the previous treatment\nsteps e.g. for further reducing nitrogen or carbon compounds. Generally used\nwhere specific local requirements for water preservation exist\n","mg/l",2E-3,8.0000000000000002E-3,"Green","Quarterly",0,0,"N/A","Yearly ","Refers to a flow-proportional composite sample taken over a period of 24 hours or, provided that sufficient flow stability is demonstrated, a time-proportional sample.\n\nNot all parameters and sampling frequencies are applicable to effluent from gas refining sites"]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Copper","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Cadmium and its compounds (50 - <100 mg/l CaCO3)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l",0.02,0.1,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Copper","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Cadmium and its compounds (50 - <100 mg/l CaCO3)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l",0.02,0.1,"Green","Once per month",0,0,0,"Daily average",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Ferro alloys Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Cadmium and its compounds (50 - <100 mg/l CaCO3)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.05,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Ferro alloys Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Cadmium and its compounds (50 - <100 mg/l CaCO3)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.05,"Green","Once per month",0,0,0,"Daily average",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Lead and Tin Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Cadmium and its compounds (50 - <100 mg/l CaCO3)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.1,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Lead and Tin Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Cadmium and its compounds (50 - <100 mg/l CaCO3)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.1,"Green","Once per month",0,0,0,"Daily average",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Nickel and Cobalt Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Cadmium and its compounds (50 - <100 mg/l CaCO3)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.1,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Nickel and Cobalt Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Cadmium and its compounds (50 - <100 mg/l CaCO3)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.1,"Green","Once per month",0,0,0,"Daily average",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Precious metals","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Cadmium and its compounds (50 - <100 mg/l CaCO3)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.05,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Precious metals","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Cadmium and its compounds (50 - <100 mg/l CaCO3)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.05,"Green","Once per month",0,0,0,"Daily average",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Zinc and Cadmium Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Cadmium and its compounds (50 - <100 mg/l CaCO3)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.1,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Zinc and Cadmium Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Cadmium and its compounds (50 - <100 mg/l CaCO3)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.1,"Green","Once per month",0,0,0,"Daily average",0]
["Refineries","1. Energy industries","Unspecified","Unspecified","All","Unspecified","All","Unspecified","Whole refinery ","Water","Cadmium and its compounds (50 - <100 mg/l CaCO3)","Removal of insoluble substances by recovering oil: \n— API Separators (APIs)\n— Corrugated Plate Interceptors (CPIs)\n— Parallel Plate Interceptors (PPIs)\n— Tilted Plate Interceptors (TPIs)\n— Buffer and/or equalisation tanks \n\nRemoval of insoluble substances by recovering suspended solid and dispersed oil:\nThese techniques generally include:\n— Dissolved Gas Flotation (DGF)\n— Induced Gas Flotation (IGF)\n— Sand Filtration \n\nRemoval of soluble substances including biological treatment and clarification:\nBiological treatment techniques may include:\n— Fixed bed systems\n— Suspended bed systems.\nOne of the most commonly used suspended bed system in refineries WWTP is\nthe activated sludge process. Fixed bed systems may include a biofilter or trickling\nfilter\n\nAdditional treatment step:\nA specific waste water treatment intended to complement the previous treatment\nsteps e.g. for further reducing nitrogen or carbon compounds. Generally used\nwhere specific local requirements for water preservation exist\n","mg/l",2E-3,8.0000000000000002E-3,"Green","Quarterly",0,0,"N/A","Yearly ","Refers to a flow-proportional composite sample taken over a period of 24 hours or, provided that sufficient flow stability is demonstrated, a time-proportional sample.\n\nNot all parameters and sampling frequencies are applicable to effluent from gas refining sites",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Refineries","1. Energy industries","Unspecified","Unspecified","All","Unspecified","All","Unspecified","Whole refinery ","Water","Cadmium and its compounds (50 - <100 mg/l CaCO3)","Removal of insoluble substances by recovering oil: \n— API Separators (APIs)\n— Corrugated Plate Interceptors (CPIs)\n— Parallel Plate Interceptors (PPIs)\n— Tilted Plate Interceptors (TPIs)\n— Buffer and/or equalisation tanks \n\nRemoval of insoluble substances by recovering suspended solid and dispersed oil:\nThese techniques generally include:\n— Dissolved Gas Flotation (DGF)\n— Induced Gas Flotation (IGF)\n— Sand Filtration \n\nRemoval of soluble substances including biological treatment and clarification:\nBiological treatment techniques may include:\n— Fixed bed systems\n— Suspended bed systems.\nOne of the most commonly used suspended bed system in refineries WWTP is\nthe activated sludge process. Fixed bed systems may include a biofilter or trickling\nfilter\n\nAdditional treatment step:\nA specific waste water treatment intended to complement the previous treatment\nsteps e.g. for further reducing nitrogen or carbon compounds. Generally used\nwhere specific local requirements for water preservation exist\n","mg/l",2E-3,8.0000000000000002E-3,"Green","Quarterly",0,0,"N/A","Yearly ","Refers to a flow-proportional composite sample taken over a period of 24 hours or, provided that sufficient flow stability is demonstrated, a time-proportional sample.\n\nNot all parameters and sampling frequencies are applicable to effluent from gas refining sites"]
["LCP","1. Energy industries","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Water","Cadmium and its compounds (≥ 200 mg/l CaCO3)","In order to reduce emissions to water from flue-gas treatment, BAT is to use an appropriate combination of the techniques given below, and to use secondary techniques as close as possible to the source in order to avoid dilution: (i) Optimised combustion (see BAT 6) and flue-gas treatment systems (e.g. SCR/SNCR, see BAT 7); (ii) Adsorption on activated carbon; (iii) Aerobic biological treatment; (iv) Anoxic/anaerobic biological treatment; (v) Coagulation and flocculation; (vi) Crystallisation; (vii) Filtration (e.g. sand filtration, microfiltration, ultrafiltration); (viii) Flotation; (ix) Ion exchange; (x) Neutralisation; (xi) Oxidation; (xii) Precipitation; (xiii) Sedimentation; (xiv) Stripping","ug/l",2,5,"Green","Once every month",0,0,"Unspecified ","Daily ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Water","Cadmium and its compounds (≥ 200 mg/l CaCO3)","In order to reduce emissions to water from flue-gas treatment, BAT is to use an appropriate combination of the techniques given below, and to use secondary techniques as close as possible to the source in order to avoid dilution: (i) Optimised combustion (see BAT 6) and flue-gas treatment systems (e.g. SCR/SNCR, see BAT 7); (ii) Adsorption on activated carbon; (iii) Aerobic biological treatment; (iv) Anoxic/anaerobic biological treatment; (v) Coagulation and flocculation; (vi) Crystallisation; (vii) Filtration (e.g. sand filtration, microfiltration, ultrafiltration); (viii) Flotation; (ix) Ion exchange; (x) Neutralisation; (xi) Oxidation; (xii) Precipitation; (xiii) Sedimentation; (xiv) Stripping","ug/l",2,5,"Green","Once every month",0,0,"Unspecified ","Daily ",0]
["LCP","1. Energy industries","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Water","Cadmium and its compounds (100 - <200 mg/l CaCO3)","In order to reduce emissions to water from flue-gas treatment, BAT is to use an appropriate combination of the techniques given below, and to use secondary techniques as close as possible to the source in order to avoid dilution: (i) Optimised combustion (see BAT 6) and flue-gas treatment systems (e.g. SCR/SNCR, see BAT 7); (ii) Adsorption on activated carbon; (iii) Aerobic biological treatment; (iv) Anoxic/anaerobic biological treatment; (v) Coagulation and flocculation; (vi) Crystallisation; (vii) Filtration (e.g. sand filtration, microfiltration, ultrafiltration); (viii) Flotation; (ix) Ion exchange; (x) Neutralisation; (xi) Oxidation; (xii) Precipitation; (xiii) Sedimentation; (xiv) Stripping","ug/l",2,5,"Green","Once every month",0,0,"Unspecified ","Daily ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Water","Cadmium and its compounds (100 - <200 mg/l CaCO3)","In order to reduce emissions to water from flue-gas treatment, BAT is to use an appropriate combination of the techniques given below, and to use secondary techniques as close as possible to the source in order to avoid dilution: (i) Optimised combustion (see BAT 6) and flue-gas treatment systems (e.g. SCR/SNCR, see BAT 7); (ii) Adsorption on activated carbon; (iii) Aerobic biological treatment; (iv) Anoxic/anaerobic biological treatment; (v) Coagulation and flocculation; (vi) Crystallisation; (vii) Filtration (e.g. sand filtration, microfiltration, ultrafiltration); (viii) Flotation; (ix) Ion exchange; (x) Neutralisation; (xi) Oxidation; (xii) Precipitation; (xiii) Sedimentation; (xiv) Stripping","ug/l",2,5,"Green","Once every month",0,0,"Unspecified ","Daily ",0]
["LCP","1. Energy industries","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Water","Cadmium and its compounds (40 - < 50 mg/l CaCO3)","In order to reduce emissions to water from flue-gas treatment, BAT is to use an appropriate combination of the techniques given below, and to use secondary techniques as close as possible to the source in order to avoid dilution: (i) Optimised combustion (see BAT 6) and flue-gas treatment systems (e.g. SCR/SNCR, see BAT 7); (ii) Adsorption on activated carbon; (iii) Aerobic biological treatment; (iv) Anoxic/anaerobic biological treatment; (v) Coagulation and flocculation; (vi) Crystallisation; (vii) Filtration (e.g. sand filtration, microfiltration, ultrafiltration); (viii) Flotation; (ix) Ion exchange; (x) Neutralisation; (xi) Oxidation; (xii) Precipitation; (xiii) Sedimentation; (xiv) Stripping","ug/l",2,5,"Green","Once every month",0,0,"Unspecified ","Daily ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Water","Cadmium and its compounds (40 - < 50 mg/l CaCO3)","In order to reduce emissions to water from flue-gas treatment, BAT is to use an appropriate combination of the techniques given below, and to use secondary techniques as close as possible to the source in order to avoid dilution: (i) Optimised combustion (see BAT 6) and flue-gas treatment systems (e.g. SCR/SNCR, see BAT 7); (ii) Adsorption on activated carbon; (iii) Aerobic biological treatment; (iv) Anoxic/anaerobic biological treatment; (v) Coagulation and flocculation; (vi) Crystallisation; (vii) Filtration (e.g. sand filtration, microfiltration, ultrafiltration); (viii) Flotation; (ix) Ion exchange; (x) Neutralisation; (xi) Oxidation; (xii) Precipitation; (xiii) Sedimentation; (xiv) Stripping","ug/l",2,5,"Green","Once every month",0,0,"Unspecified ","Daily ",0]
["LCP","1. Energy industries","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Water","Cadmium and its compounds (50 - <100 mg/l CaCO3)","In order to reduce emissions to water from flue-gas treatment, BAT is to use an appropriate combination of the techniques given below, and to use secondary techniques as close as possible to the source in order to avoid dilution: (i) Optimised combustion (see BAT 6) and flue-gas treatment systems (e.g. SCR/SNCR, see BAT 7); (ii) Adsorption on activated carbon; (iii) Aerobic biological treatment; (iv) Anoxic/anaerobic biological treatment; (v) Coagulation and flocculation; (vi) Crystallisation; (vii) Filtration (e.g. sand filtration, microfiltration, ultrafiltration); (viii) Flotation; (ix) Ion exchange; (x) Neutralisation; (xi) Oxidation; (xii) Precipitation; (xiii) Sedimentation; (xiv) Stripping","ug/l",2,5,"Green","Once every month",0,0,"Unspecified ","Daily ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Water","Cadmium and its compounds (50 - <100 mg/l CaCO3)","In order to reduce emissions to water from flue-gas treatment, BAT is to use an appropriate combination of the techniques given below, and to use secondary techniques as close as possible to the source in order to avoid dilution: (i) Optimised combustion (see BAT 6) and flue-gas treatment systems (e.g. SCR/SNCR, see BAT 7); (ii) Adsorption on activated carbon; (iii) Aerobic biological treatment; (iv) Anoxic/anaerobic biological treatment; (v) Coagulation and flocculation; (vi) Crystallisation; (vii) Filtration (e.g. sand filtration, microfiltration, ultrafiltration); (viii) Flotation; (ix) Ion exchange; (x) Neutralisation; (xi) Oxidation; (xii) Precipitation; (xiii) Sedimentation; (xiv) Stripping","ug/l",2,5,"Green","Once every month",0,0,"Unspecified ","Daily ",0]
["Common Waste Water and Waste Gas Treatment","4. Chemical industry","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Whole plant","Water","Chromium III (95%ile) (dissolved)","Appropriate final waste water treatment techniques, depending on the pollutant, include:\n\nPreliminary and primary treatment:(i) Equalisation; (ii) Neutralisation; (iii) Physical separation, e.g.\nscreens, sieves, grit separators,\ngrease separators or\nprimary settlement tanks \n\nBiological treatment: (i) Activated sludge process; (ii) Membrane bioreactor\n\nNitrogen removal: (i) Nitrification/denitrification\n\nPhosphorus removal: (i) Chemical precipitation\n\nFinal solids removal: (i) Coagulation and flocculation; (ii) Sedimentation; (iii) Filtration (e.g. sand filtration,\nmicrofiltration, ultrafiltration); (iv) Flotation\n","mg/l",5,25,"Green","Monthly",0,0,"N/A","Yearly","The lower end of the range is typically achieved when few of the corresponding metal (compounds) are used or produced by the installation\n\nThis BAT-AEL may not apply to inorganic effluents when the main pollutant load originates from the production of inorganic\nheavy metal compounds.\n\nThis BAT-AEL may not apply when the main pollutant load originates from the processing of large volumes of solid inorganic raw\nmaterials that are contaminated with metals (e.g. soda ash from the Solvay process, titanium dioxide).       \n\nThis BAT-AEL may not apply when the main pollutant load originates from the production of chromium-organic compounds.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Common Waste Water and Waste Gas Treatment","4. Chemical industry","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Whole plant","Water","Chromium III (95%ile) (dissolved)","Appropriate final waste water treatment techniques, depending on the pollutant, include:\n\nPreliminary and primary treatment:(i) Equalisation; (ii) Neutralisation; (iii) Physical separation, e.g.\nscreens, sieves, grit separators,\ngrease separators or\nprimary settlement tanks \n\nBiological treatment: (i) Activated sludge process; (ii) Membrane bioreactor\n\nNitrogen removal: (i) Nitrification/denitrification\n\nPhosphorus removal: (i) Chemical precipitation\n\nFinal solids removal: (i) Coagulation and flocculation; (ii) Sedimentation; (iii) Filtration (e.g. sand filtration,\nmicrofiltration, ultrafiltration); (iv) Flotation\n","mg/l",5,25,"Green","Monthly",0,0,"N/A","Yearly","The lower end of the range is typically achieved when few of the corresponding metal (compounds) are used or produced by the installation\n\nThis BAT-AEL may not apply to inorganic effluents when the main pollutant load originates from the production of inorganic\nheavy metal compounds.\n\nThis BAT-AEL may not apply when the main pollutant load originates from the processing of large volumes of solid inorganic raw\nmaterials that are contaminated with metals (e.g. soda ash from the Solvay process, titanium dioxide).       \n\nThis BAT-AEL may not apply when the main pollutant load originates from the production of chromium-organic compounds."]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Ferro alloys Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Chromium III (95%ile) (dissolved)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.2,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Ferro alloys Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Chromium III (95%ile) (dissolved)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.2,"Green","Once per month",0,0,0,"Daily average",0]
["LCP","1. Energy industries","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Water","Chromium III (95%ile) (dissolved)","In order to reduce emissions to water from flue-gas treatment, BAT is to use an appropriate combination of the techniques given below, and to use secondary techniques as close as possible to the source in order to avoid dilution: (i) Optimised combustion (see BAT 6) and flue-gas treatment systems (e.g. SCR/SNCR, see BAT 7); (ii) Adsorption on activated carbon; (iii) Aerobic biological treatment; (iv) Anoxic/anaerobic biological treatment; (v) Coagulation and flocculation; (vi) Crystallisation; (vii) Filtration (e.g. sand filtration, microfiltration, ultrafiltration); (viii) Flotation; (ix) Ion exchange; (x) Neutralisation; (xi) Oxidation; (xii) Precipitation; (xiii) Sedimentation; (xiv) Stripping","ug/l",10,50,"Green","Once every month",0,0,"Unspecified ","Daily ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Water","Chromium III (95%ile) (dissolved)","In order to reduce emissions to water from flue-gas treatment, BAT is to use an appropriate combination of the techniques given below, and to use secondary techniques as close as possible to the source in order to avoid dilution: (i) Optimised combustion (see BAT 6) and flue-gas treatment systems (e.g. SCR/SNCR, see BAT 7); (ii) Adsorption on activated carbon; (iii) Aerobic biological treatment; (iv) Anoxic/anaerobic biological treatment; (v) Coagulation and flocculation; (vi) Crystallisation; (vii) Filtration (e.g. sand filtration, microfiltration, ultrafiltration); (viii) Flotation; (ix) Ion exchange; (x) Neutralisation; (xi) Oxidation; (xii) Precipitation; (xiii) Sedimentation; (xiv) Stripping","ug/l",10,50,"Green","Once every month",0,0,"Unspecified ","Daily ",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Lead and Tin Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Cobalt (dissolved)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.1,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Lead and Tin Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Cobalt (dissolved)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.1,"Green","Once per month",0,0,0,"Daily average",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Nickel and Cobalt Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Cobalt (dissolved)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l",0.1,0.5,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Nickel and Cobalt Production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Cobalt (dissolved)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l",0.1,0.5,"Green","Once per month",0,0,0,"Daily average",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Precious metals","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Silver (dissolved)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.6,"Green","Once per month",0,0,0,"Daily average",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Precious metals","All","Unspecified ","Unspecified","Unspecified","Unspecified","Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates","Water","Silver (dissolved)","In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below: (i) Chemical precipitation ; (ii) Sedimentation; (iii) Filtration; (iv) Filtration ; (v) Ultrafiltration; (vi) Activated carbon filtration; (vii) Reverse osmosis ","mg/l","N/A",0.6,"Green","Once per month",0,0,0,"Daily average",0]
["Refineries","1. Energy industries","Unspecified","Unspecified","All","Unspecified","All","Unspecified","Whole refinery ","Water","Vanadium (0 - 200 mg/l CaCO3)","Removal of insoluble substances by recovering oil: \n— API Separators (APIs)\n— Corrugated Plate Interceptors (CPIs)\n— Parallel Plate Interceptors (PPIs)\n— Tilted Plate Interceptors (TPIs)\n— Buffer and/or equalisation tanks \n\nRemoval of insoluble substances by recovering suspended solid and dispersed oil:\nThese techniques generally include:\n— Dissolved Gas Flotation (DGF)\n— Induced Gas Flotation (IGF)\n— Sand Filtration \n\nRemoval of soluble substances including biological treatment and clarification:\nBiological treatment techniques may include:\n— Fixed bed systems\n— Suspended bed systems.\nOne of the most commonly used suspended bed system in refineries WWTP is\nthe activated sludge process. Fixed bed systems may include a biofilter or trickling\nfilter\n\nAdditional treatment step:\nA specific waste water treatment intended to complement the previous treatment\nsteps e.g. for further reducing nitrogen or carbon compounds. Generally used\nwhere specific local requirements for water preservation exist\n","mg/l","N/A","N/A","Green","Quarterly",0,0,"N/A","Yearly ","Refers to a flow-proportional composite sample taken over a period of 24 hours or, provided that sufficient flow stability is demonstrated, a time-proportional sample.\n\nNot all parameters and sampling frequencies are applicable to effluent from gas refining sites",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Refineries","1. Energy industries","Unspecified","Unspecified","All","Unspecified","All","Unspecified","Whole refinery ","Water","Vanadium (0 - 200 mg/l CaCO3)","Removal of insoluble substances by recovering oil: \n— API Separators (APIs)\n— Corrugated Plate Interceptors (CPIs)\n— Parallel Plate Interceptors (PPIs)\n— Tilted Plate Interceptors (TPIs)\n— Buffer and/or equalisation tanks \n\nRemoval of insoluble substances by recovering suspended solid and dispersed oil:\nThese techniques generally include:\n— Dissolved Gas Flotation (DGF)\n— Induced Gas Flotation (IGF)\n— Sand Filtration \n\nRemoval of soluble substances including biological treatment and clarification:\nBiological treatment techniques may include:\n— Fixed bed systems\n— Suspended bed systems.\nOne of the most commonly used suspended bed system in refineries WWTP is\nthe activated sludge process. Fixed bed systems may include a biofilter or trickling\nfilter\n\nAdditional treatment step:\nA specific waste water treatment intended to complement the previous treatment\nsteps e.g. for further reducing nitrogen or carbon compounds. Generally used\nwhere specific local requirements for water preservation exist\n","mg/l","N/A","N/A","Green","Quarterly",0,0,"N/A","Yearly ","Refers to a flow-proportional composite sample taken over a period of 24 hours or, provided that sufficient flow stability is demonstrated, a time-proportional sample.\n\nNot all parameters and sampling frequencies are applicable to effluent from gas refining sites"]
["Glass","3. Mineral industry","Filament glass fibre","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes (forming and coating)","Air","Ammonia (human health receptor)","BAT is to reduce emissions from downstream processes by using one or a combination of the following techniques: (i) Wet scrubbing systems; (ii) Wet electrostatic precipitator; (iii) Filtration system (bag filter)","mg/Nm3","N/A","20","Amber",0,"273.15","101.3","N/A","Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Filament glass fibre","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes (forming and coating)","Air","Ammonia (human health receptor)","BAT is to reduce emissions from downstream processes by using one or a combination of the following techniques: (i) Wet scrubbing systems; (ii) Wet electrostatic precipitator; (iii) Filtration system (bag filter)","mg/Nm3","N/A","20","Amber",0,"273.15","101.3","N/A","Daily average (continuous)",0]
["Glass","3. Mineral industry","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes- Curing oven emissions ","Air","Ammonia (human health receptor)","BAT is to reduce emissions from downstream processes by using one or a combination of the following techniques: (i) Impact jets and cyclones; (ii) Wet scrubbers; (iii) Wet electrostatic precipitators; (iv) Stone wool filters; (v) Waste gas incineration","mg/Nm3","20","60","Green","Continuous or regular periodic measurements of NH 3 emissions, when selective catalytic reduction (SCR) or selective non-catalytic reduction (SNCR) techniques are applied","273.15","101.3","N/A","Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes- Curing oven emissions ","Air","Ammonia (human health receptor)","BAT is to reduce emissions from downstream processes by using one or a combination of the following techniques: (i) Impact jets and cyclones; (ii) Wet scrubbers; (iii) Wet electrostatic precipitators; (iv) Stone wool filters; (v) Waste gas incineration","mg/Nm3","20","60","Green","Continuous or regular periodic measurements of NH 3 emissions, when selective catalytic reduction (SCR) or selective non-catalytic reduction (SNCR) techniques are applied","273.15","101.3","N/A","Daily average (continuous)",0]
["Glass","3. Mineral industry","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes- Curing oven emissions ","Air","Ammonia (human health receptor)","BAT is to reduce emissions from downstream processes by using one or a combination of the following techniques: (i) Impact jets and cyclones; (ii) Wet scrubbers; (iii) Wet electrostatic precipitators; (iv) Stone wool filters; (v) Waste gas incineration","kg/tonne melted glass","N/A","0.4","Amber",0,"273.15","101.3","N/A","Daily average (continuous)","The specific mass emissions refer to 1 tonne of produced glass",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes- Curing oven emissions ","Air","Ammonia (human health receptor)","BAT is to reduce emissions from downstream processes by using one or a combination of the following techniques: (i) Impact jets and cyclones; (ii) Wet scrubbers; (iii) Wet electrostatic precipitators; (iv) Stone wool filters; (v) Waste gas incineration","kg/tonne melted glass","N/A","0.4","Amber",0,"273.15","101.3","N/A","Daily average (continuous)","The specific mass emissions refer to 1 tonne of produced glass"]
["Glass","3. Mineral industry","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes- Forming area ","Air","Ammonia (human health receptor)","BAT is to reduce emissions from downstream processes by using one or a combination of the following techniques: (i) Impact jets and cyclones; (ii) Wet scrubbers; (iii) Wet electrostatic precipitators; (iv) Stone wool filters; (v) Waste gas incineration","mg/Nm3","30","60","Green","Continuous or regular periodic measurements of NH 3 emissions, when selective catalytic reduction (SCR) or selective non-catalytic reduction (SNCR) techniques are applied","273.15","101.3","N/A","Daily average (continuous)",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass","3. Mineral industry","Mineral wool","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Downstream processes- Forming area ","Air","Ammonia (human health receptor)","BAT is to reduce emissions from downstream processes by using one or a combination of the following techniques: (i) Impact jets and cyclones; (ii) Wet scrubbers; (iii) Wet electrostatic precipitators; (iv) Stone wool filters; (v) Waste gas incineration","mg/Nm3","30","60","Green","Continuous or regular periodic measurements of NH 3 emissions, when selective catalytic reduction (SCR) or selective non-catalytic reduction (SNCR) techniques are applied","273.15","101.3","N/A","Daily average (continuous)",0]
["Refineries","1. Energy industries","Unspecified","Unspecified","All","Unspecified","All","Unspecified","All units equipped with SCR or SNCR","Air","Ammonia (human health receptor)","In order to prevent and reduce ammonia (NH3) emissions to air when applying selective catalytic reduction (SCR) or selective non-catalytic reduction (SNCR) techniques, BAT is to maintain suitable operating conditions of the SCR or SNCR waste gas treatment systems, with the aim of limiting emissions of unreacted NH3.","mg/Nm3",5,15,"Green","Continuous",0,0,0.03,"Monthly average","The higher end of the range is associated with higher inlet NOX concentrations, higher NOX reduction rates and the ageing\nof the catalyst. \n\nThe lower end of the range is associated with the use of the SCR technique. ",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Refineries","1. Energy industries","Unspecified","Unspecified","All","Unspecified","All","Unspecified","All units equipped with SCR or SNCR","Air","Ammonia (human health receptor)","In order to prevent and reduce ammonia (NH3) emissions to air when applying selective catalytic reduction (SCR) or selective non-catalytic reduction (SNCR) techniques, BAT is to maintain suitable operating conditions of the SCR or SNCR waste gas treatment systems, with the aim of limiting emissions of unreacted NH3.","mg/Nm3",5,15,"Green","Continuous",0,0,0.03,"Monthly average","The higher end of the range is associated with higher inlet NOX concentrations, higher NOX reduction rates and the ageing\nof the catalyst. \n\nThe lower end of the range is associated with the use of the SCR technique. "]
["Iron and steel","2. Production and processing of metals","Coke Oven Plants","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Coke grading and handling","Air","Particulates (PM10) (Annual Mean)","BAT for coke grading and handling is to prevent or reduce dust emissions by using the following techniques in combination: (i)use of building or device enclosures; (ii) efficient extraction and subsequent dry dedusting ","mg/Nm3","N/A",10,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Coke Oven Plants","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Coke grading and handling","Air","Particulates (PM10) (Annual Mean)","BAT for coke grading and handling is to prevent or reduce dust emissions by using the following techniques in combination: (i)use of building or device enclosures; (ii) efficient extraction and subsequent dry dedusting ","mg/Nm3","N/A",10,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0]
["Iron and steel","2. Production and processing of metals","Coke Oven Plants","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Coke pushing","Air","Particulates (PM10) (Annual Mean)","BAT for coke pushing is to reduce dust emissions by using the following techniques: (i)  extraction by means of an integrated coke transfer machine equipped with a hood; (ii) using a one point or a mobile quenching car","mg/Nm3","N/A",20,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Coke Oven Plants","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Coke pushing","Air","Particulates (PM10) (Annual Mean)","BAT for coke pushing is to reduce dust emissions by using the following techniques: (i)  extraction by means of an integrated coke transfer machine equipped with a hood; (ii) using a one point or a mobile quenching car","mg/Nm3","N/A",20,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0]
["Iron and steel","2. Production and processing of metals","Coke Oven Plants","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Coke pushing","Air","Particulates (PM10) (Annual Mean)","BAT for coke pushing is to reduce dust emissions by using the following techniques: (i) using land-based extraction gas treatment with a bag filter or other abatement systems","mg/Nm3","N/A",10,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Coke Oven Plants","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Coke pushing","Air","Particulates (PM10) (Annual Mean)","BAT for coke pushing is to reduce dust emissions by using the following techniques: (i) using land-based extraction gas treatment with a bag filter or other abatement systems","mg/Nm3","N/A",10,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0]
["Iron and steel","2. Production and processing of metals","Coke Oven Plants","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Coke quenching","Air","Particulates (PM10) (Annual Mean)","BAT for coke quenching is to reduce dust emissions by using one of the following techniques: (i) using coke dry quenching (CDQ) with the recovery of sensible heat and the removal of dust from charging, handling\nand screening operations by means of a bag filter","mg/Nm3","N/A",20,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Coke Oven Plants","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Coke quenching","Air","Particulates (PM10) (Annual Mean)","BAT for coke quenching is to reduce dust emissions by using one of the following techniques: (i) using coke dry quenching (CDQ) with the recovery of sensible heat and the removal of dust from charging, handling\nand screening operations by means of a bag filter","mg/Nm3","N/A",20,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0]
["Iron and steel","2. Production and processing of metals","Coke Oven Plants","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Coke quenching","Air","Particulates (PM10) (Annual Mean)","BAT for coke quenching is to reduce dust emissions by using one of the following techniques: (i) using coke stabilisation quenching (CSQ)","g/t","N/A",10,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Coke Oven Plants","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Coke quenching","Air","Particulates (PM10) (Annual Mean)","BAT for coke quenching is to reduce dust emissions by using one of the following techniques: (i) using coke stabilisation quenching (CSQ)","g/t","N/A",10,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0]
["Iron and steel","2. Production and processing of metals","Coke Oven Plants","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Coke quenching","Air","Particulates (PM10) (Annual Mean)","BAT for coke quenching is to reduce dust emissions by using one of the following techniques: (i) using emission-minimised conventional wet quenching","g/t","N/A",25,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Coke Oven Plants","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Coke quenching","Air","Particulates (PM10) (Annual Mean)","BAT for coke quenching is to reduce dust emissions by using one of the following techniques: (i) using emission-minimised conventional wet quenching","g/t","N/A",25,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0]
["Iron and steel","2. Production and processing of metals","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: Basic oxygen furnace (BOF) gas recovery by supressed combustion","Air","Particulates (PM10) (Annual Mean)","BAT for basic oxygen furnace (BOF) gas recovery by suppressed combustion is to extract the BOF gas during blowing as much as possible and to clean it by using the following techniques in combination: (i) use of a suppressed combustion process; (ii) prededusting to remove coarse dust by means of dry separation techniques (e.g. deflector, cyclone) or wet separators; (iii) dust abatement by means of dry dedusting for new and existing plants or wet dedusting for existing plants\n","mg/Nm3",10,30,"Green","Continuous",0,0,"Unspecified ",0,"This BAT AEL is for dust abatement by dry dedusting",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: Basic oxygen furnace (BOF) gas recovery by supressed combustion","Air","Particulates (PM10) (Annual Mean)","BAT for basic oxygen furnace (BOF) gas recovery by suppressed combustion is to extract the BOF gas during blowing as much as possible and to clean it by using the following techniques in combination: (i) use of a suppressed combustion process; (ii) prededusting to remove coarse dust by means of dry separation techniques (e.g. deflector, cyclone) or wet separators; (iii) dust abatement by means of dry dedusting for new and existing plants or wet dedusting for existing plants\n","mg/Nm3",10,30,"Green","Continuous",0,0,"Unspecified ",0,"This BAT AEL is for dust abatement by dry dedusting"]
["Iron and steel","2. Production and processing of metals","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: Basic oxygen furnace (BOF) gas recovery by supressed combustion","Air","Particulates (PM10) (Annual Mean)","BAT for basic oxygen furnace (BOF) gas recovery by suppressed combustion is to extract the BOF gas during blowing as much as possible and to clean it by using the following techniques in combination: (i) use of a suppressed combustion process; (ii) prededusting to remove coarse dust by means of dry separation techniques (e.g. deflector, cyclone) or wet separators; (iii) dust abatement by means of dry dedusting for new and existing plants or wet dedusting for existing plants\n","mg/Nm3","N/A",50,"Green","Continuous",0,0,"Unspecified ",0,"This BAT AEL is for dust abatement by wet dedusting",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: Basic oxygen furnace (BOF) gas recovery by supressed combustion","Air","Particulates (PM10) (Annual Mean)","BAT for basic oxygen furnace (BOF) gas recovery by suppressed combustion is to extract the BOF gas during blowing as much as possible and to clean it by using the following techniques in combination: (i) use of a suppressed combustion process; (ii) prededusting to remove coarse dust by means of dry separation techniques (e.g. deflector, cyclone) or wet separators; (iii) dust abatement by means of dry dedusting for new and existing plants or wet dedusting for existing plants\n","mg/Nm3","N/A",50,"Green","Continuous",0,0,"Unspecified ",0,"This BAT AEL is for dust abatement by wet dedusting"]
["Iron and steel","2. Production and processing of metals","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: Basic oxygen furnace (BOF) gas recovery during oxygen blowing in the case of full combustion","Air","Particulates (PM10) (Annual Mean)","BAT for basic oxygen furnace (BOF) gas recovery during oxygen blowing in the case of full combustion is to\nreduce dust emissions by using one of the following techniques:  dry dedusting (e.g. ESP or bag filter) for new and existing plants","mg/Nm3",10,30,"Green","Continuous",0,0,"Unspecified ","Average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: Basic oxygen furnace (BOF) gas recovery during oxygen blowing in the case of full combustion","Air","Particulates (PM10) (Annual Mean)","BAT for basic oxygen furnace (BOF) gas recovery during oxygen blowing in the case of full combustion is to\nreduce dust emissions by using one of the following techniques:  dry dedusting (e.g. ESP or bag filter) for new and existing plants","mg/Nm3",10,30,"Green","Continuous",0,0,"Unspecified ","Average over the sampling period",0]
["Iron and steel","2. Production and processing of metals","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: Basic oxygen furnace (BOF) gas recovery during oxygen blowing in the case of full combustion","Air","Particulates (PM10) (Annual Mean)","BAT for basic oxygen furnace (BOF) gas recovery during oxygen blowing in the case of full combustion is to\nreduce dust emissions by using one of the following techniques:  wet dedusting (e.g. ESP or bag filter) for existing plants","mg/Nm3","N/A",50,"Green","Continuous",0,0,"Unspecified ","Average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: Basic oxygen furnace (BOF) gas recovery during oxygen blowing in the case of full combustion","Air","Particulates (PM10) (Annual Mean)","BAT for basic oxygen furnace (BOF) gas recovery during oxygen blowing in the case of full combustion is to\nreduce dust emissions by using one of the following techniques:  wet dedusting (e.g. ESP or bag filter) for existing plants","mg/Nm3","N/A",50,"Green","Continuous",0,0,"Unspecified ","Average over the sampling period",0]
["Iron and steel","2. Production and processing of metals","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: On-site slag processing ","Air","Particulates (PM10) (Annual Mean)","BAT for on-site slag processing is to reduce dust emissions by using one or a combination of the following\ntechniques: (i) Efficient extraction of the slag crusher and screening devices with subsequent off-gas cleaning, if relevant; (ii) transport of untreated slag by shovel loaders; (iii) extraction or wetting of conveyor transfer points for broken material; (iv) wetting of slag storage heaps; (v) use of water fogs when broken slag is loaded\n","mg/Nm3",10,20,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: On-site slag processing ","Air","Particulates (PM10) (Annual Mean)","BAT for on-site slag processing is to reduce dust emissions by using one or a combination of the following\ntechniques: (i) Efficient extraction of the slag crusher and screening devices with subsequent off-gas cleaning, if relevant; (ii) transport of untreated slag by shovel loaders; (iii) extraction or wetting of conveyor transfer points for broken material; (iv) wetting of slag storage heaps; (v) use of water fogs when broken slag is loaded\n","mg/Nm3",10,20,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0]
["Iron and steel","2. Production and processing of metals","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: Waste water from continous casting machines ","Air","Particulates (PM10) (Annual Mean)","BAT is to minimise the waste water discharge from continuous casting by using the following techniques in combination: (i) the removal of solids by flocculation, sedimentation and/or filtration; (ii) the removal of oil in skimming tanks or any other effective device; (iii) the recirculation of cooling water and water from vacuum generation as much as possible.","mg/l","N/A",20,"Green","Discontinuous ",0,0,"Unspecified ","Random sample or a 24 hour composite sample ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: Waste water from continous casting machines ","Air","Particulates (PM10) (Annual Mean)","BAT is to minimise the waste water discharge from continuous casting by using the following techniques in combination: (i) the removal of solids by flocculation, sedimentation and/or filtration; (ii) the removal of oil in skimming tanks or any other effective device; (iii) the recirculation of cooling water and water from vacuum generation as much as possible.","mg/l","N/A",20,"Green","Discontinuous ",0,0,"Unspecified ","Random sample or a 24 hour composite sample ",0]
["Iron and steel","2. Production and processing of metals","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: Waste water from continous casting machines ","Air","Particulates (PM10) (Annual Mean)","BAT is to minimise the waste water discharge from continuous casting by using the following techniques in combination: (i) the removal of solids by flocculation, sedimentation and/or filtration; (ii) the removal of oil in skimming tanks or any other effective device; (iii) the recirculation of cooling water and water from vacuum generation as much as possible.","mg/l","N/A",5,"Green","Discontinuous ",0,0,"Unspecified ","Random sample or a 24 hour composite sample ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: Waste water from continous casting machines ","Air","Particulates (PM10) (Annual Mean)","BAT is to minimise the waste water discharge from continuous casting by using the following techniques in combination: (i) the removal of solids by flocculation, sedimentation and/or filtration; (ii) the removal of oil in skimming tanks or any other effective device; (iii) the recirculation of cooling water and water from vacuum generation as much as possible.","mg/l","N/A",5,"Green","Discontinuous ",0,0,"Unspecified ","Random sample or a 24 hour composite sample ",0]
["Iron and steel","2. Production and processing of metals","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: Waste water from continous casting machines ","Air","Particulates (PM10) (Annual Mean)","BAT is to minimise the waste water discharge from continuous casting by using the following techniques in combination: (i) the removal of solids by flocculation, sedimentation and/or filtration; (ii) the removal of oil in skimming tanks or any other effective device; (iii) the recirculation of cooling water and water from vacuum generation as much as possible.","mg/l","N/A",2,"Green","Discontinuous ",0,0,"Unspecified ","Random sample or a 24 hour composite sample ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: Waste water from continous casting machines ","Air","Particulates (PM10) (Annual Mean)","BAT is to minimise the waste water discharge from continuous casting by using the following techniques in combination: (i) the removal of solids by flocculation, sedimentation and/or filtration; (ii) the removal of oil in skimming tanks or any other effective device; (iii) the recirculation of cooling water and water from vacuum generation as much as possible.","mg/l","N/A",2,"Green","Discontinuous ",0,0,"Unspecified ","Random sample or a 24 hour composite sample ",0]
["Iron and steel","2. Production and processing of metals","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: Waste water from continous casting machines ","Air","Particulates (PM10) (Annual Mean)","BAT is to minimise the waste water discharge from continuous casting by using the following techniques in combination: (i) the removal of solids by flocculation, sedimentation and/or filtration; (ii) the removal of oil in skimming tanks or any other effective device; (iii) the recirculation of cooling water and water from vacuum generation as much as possible.","mg/l","N/A",0.5,"Green","Discontinuous ",0,0,"Unspecified ","Random sample or a 24 hour composite sample ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: Waste water from continous casting machines ","Air","Particulates (PM10) (Annual Mean)","BAT is to minimise the waste water discharge from continuous casting by using the following techniques in combination: (i) the removal of solids by flocculation, sedimentation and/or filtration; (ii) the removal of oil in skimming tanks or any other effective device; (iii) the recirculation of cooling water and water from vacuum generation as much as possible.","mg/l","N/A",0.5,"Green","Discontinuous ",0,0,"Unspecified ","Random sample or a 24 hour composite sample ",0]
["Iron and steel","2. Production and processing of metals","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: Waste water from continous casting machines ","Air","Particulates (PM10) (Annual Mean)","BAT is to minimise the waste water discharge from continuous casting by using the following techniques in combination: (i) the removal of solids by flocculation, sedimentation and/or filtration; (ii) the removal of oil in skimming tanks or any other effective device; (iii) the recirculation of cooling water and water from vacuum generation as much as possible.","mg/l","N/A",0.5,"Green","Discontinuous ",0,0,"Unspecified ","Random sample or a 24 hour composite sample ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: Waste water from continous casting machines ","Air","Particulates (PM10) (Annual Mean)","BAT is to minimise the waste water discharge from continuous casting by using the following techniques in combination: (i) the removal of solids by flocculation, sedimentation and/or filtration; (ii) the removal of oil in skimming tanks or any other effective device; (iii) the recirculation of cooling water and water from vacuum generation as much as possible.","mg/l","N/A",0.5,"Green","Discontinuous ",0,0,"Unspecified ","Random sample or a 24 hour composite sample ",0]
["Iron and steel","2. Production and processing of metals","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: Waste water from continous casting machines ","Air","Particulates (PM10) (Annual Mean)","BAT is to minimise the waste water discharge from continuous casting by using the following techniques in combination: (i) the removal of solids by flocculation, sedimentation and/or filtration; (ii) the removal of oil in skimming tanks or any other effective device; (iii) the recirculation of cooling water and water from vacuum generation as much as possible.","mg/l","N/A",5,"Green","Discontinuous ",0,0,"Unspecified ","Random sample or a 24 hour composite sample ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Basic Oxygen Steelmaking and Casting: Waste water from continous casting machines ","Air","Particulates (PM10) (Annual Mean)","BAT is to minimise the waste water discharge from continuous casting by using the following techniques in combination: (i) the removal of solids by flocculation, sedimentation and/or filtration; (ii) the removal of oil in skimming tanks or any other effective device; (iii) the recirculation of cooling water and water from vacuum generation as much as possible.","mg/l","N/A",5,"Green","Discontinuous ",0,0,"Unspecified ","Random sample or a 24 hour composite sample ",0]
["Iron and steel","2. Production and processing of metals","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Blast Furnaces: Blast furnace gas ","Air","Particulates (PM10) (Annual Mean)","BAT is to reduce dust emissions from the blast furnace gas by using one or a combination of the following techniques:\n\nUsing dry predusting devices: (i) deflectors; (ii) dust catchers; (iii) cyclones; (iv) electrostatic precipitators.\n\nSubsequent dust abatement: (i) hurdle-type scrubbers; (ii) venturi scrubbers; (iii) annular gap scrubbers; (iv) wet electrostatic precipitators; (v) disintegrators ","mg/Nm3","N/A",10,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Blast Furnaces: Blast furnace gas ","Air","Particulates (PM10) (Annual Mean)","BAT is to reduce dust emissions from the blast furnace gas by using one or a combination of the following techniques:\n\nUsing dry predusting devices: (i) deflectors; (ii) dust catchers; (iii) cyclones; (iv) electrostatic precipitators.\n\nSubsequent dust abatement: (i) hurdle-type scrubbers; (ii) venturi scrubbers; (iii) annular gap scrubbers; (iv) wet electrostatic precipitators; (v) disintegrators ","mg/Nm3","N/A",10,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0]
["Iron and steel","2. Production and processing of metals","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Blast Furnaces: Loading from the storage bunkers of the coal injection unit","Air","Particulates (PM10) (Annual Mean)","BAT for displaced air during loading from the storage bunkers of the coal injection unit is to capture dust emissions and perform subsequent dry dedusting.","mg/Nm3","N/A",20,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Blast Furnaces: Loading from the storage bunkers of the coal injection unit","Air","Particulates (PM10) (Annual Mean)","BAT for displaced air during loading from the storage bunkers of the coal injection unit is to capture dust emissions and perform subsequent dry dedusting.","mg/Nm3","N/A",20,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0]
["Iron and steel","2. Production and processing of metals","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Electric arc furnace steelmaking and casting: On-site slag processing ","Air","Particulates (PM10) (Annual Mean)","BAT for on-site slag processing is to reduce dust emissions by using one or a combination of the following techniques: (i) efficient extraction of the slag crusher and screening devices with subsequent off-gas cleaning, if relevant; (ii) transport of untreated slag by shovel loaders; (iii) extraction or wetting of conveyor transfer points for broken material; (iv) wetting of slag storage heaps; (v) use of water fogs when broken slag is loaded","mg/Nm3",10,20,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Electric arc furnace steelmaking and casting: On-site slag processing ","Air","Particulates (PM10) (Annual Mean)","BAT for on-site slag processing is to reduce dust emissions by using one or a combination of the following techniques: (i) efficient extraction of the slag crusher and screening devices with subsequent off-gas cleaning, if relevant; (ii) transport of untreated slag by shovel loaders; (iii) extraction or wetting of conveyor transfer points for broken material; (iv) wetting of slag storage heaps; (v) use of water fogs when broken slag is loaded","mg/Nm3",10,20,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0]
["Iron and steel","2. Production and processing of metals","Coke Oven Plants","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Coal charging systems ","Air","Particulates (PM10) (Annual Mean)","BAT is to charge coke oven chambers with emission-reduced charging systems. \n\nIf, however, the gases are extracted and treated outside the coke oven, charging with a land-based treatment of the\nextracted gases is the preferred method. Treatment should consist of an efficient extraction of the emissions with\nsubsequent combustion to reduce organic compounds and the use of a bag filter to reduce particulates.","g/t","N/A",5,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Coke Oven Plants","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Coal charging systems ","Air","Particulates (PM10) (Annual Mean)","BAT is to charge coke oven chambers with emission-reduced charging systems. \n\nIf, however, the gases are extracted and treated outside the coke oven, charging with a land-based treatment of the\nextracted gases is the preferred method. Treatment should consist of an efficient extraction of the emissions with\nsubsequent combustion to reduce organic compounds and the use of a bag filter to reduce particulates.","g/t","N/A",5,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0]
["Iron and steel","2. Production and processing of metals","Coke Oven Plants","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Coal charging systems ","Air","Particulates (PM10) (Annual Mean)","BAT is to charge coke oven chambers with emission-reduced charging systems. \n\nIf, however, the gases are extracted and treated outside the coke oven, charging with a land-based treatment of the\nextracted gases is the preferred method. Treatment should consist of an efficient extraction of the emissions with\nsubsequent combustion to reduce organic compounds and the use of a bag filter to reduce particulates.","mg/Nm3","N/A",50,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Coke Oven Plants","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Coal charging systems ","Air","Particulates (PM10) (Annual Mean)","BAT is to charge coke oven chambers with emission-reduced charging systems. \n\nIf, however, the gases are extracted and treated outside the coke oven, charging with a land-based treatment of the\nextracted gases is the preferred method. Treatment should consist of an efficient extraction of the emissions with\nsubsequent combustion to reduce organic compounds and the use of a bag filter to reduce particulates.","mg/Nm3","N/A",50,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0]
["Iron and steel","2. Production and processing of metals","Coke Oven Plants","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Storage and handling of pulverised coal","Air","Particulates (PM10) (Annual Mean)","BAT for storage and handling of pulverised coal is to prevent or reduce diffuse dust emissions by using one or a combination of the following techniques: (i) storing pulverised materials in bunkers and warehouses; (ii) using closed or enclosed conveyors; (iii)  minimising the drop heights depending on the plant size and construction; (iv) reducing emissions from charging of the coal tower and the charging car; (v) using efficient extraction and subsequent dedusting\n","mg/Nm3",10,20,"Amber",0,0,0,"Unspecified ","Average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Coke Oven Plants","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Storage and handling of pulverised coal","Air","Particulates (PM10) (Annual Mean)","BAT for storage and handling of pulverised coal is to prevent or reduce diffuse dust emissions by using one or a combination of the following techniques: (i) storing pulverised materials in bunkers and warehouses; (ii) using closed or enclosed conveyors; (iii)  minimising the drop heights depending on the plant size and construction; (iv) reducing emissions from charging of the coal tower and the charging car; (v) using efficient extraction and subsequent dedusting\n","mg/Nm3",10,20,"Amber",0,0,0,"Unspecified ","Average over the sampling period",0]
["Iron and steel","2. Production and processing of metals","Coke Oven Plants","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Coal grinding plants ","Air","Particulates (PM10) (Annual Mean)","BAT for coal grinding plants (coal preparation including crushing, grinding, pulverising and screening) is to prevent or reduce dust emissions by using one or a combination of the following techniques: (i) building and/or device enclosure (crusher, pulveriser, sieves); (ii) efficient extraction and use of a subsequent dry dedusting systems.","mg/Nm3",10,20,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Coke Oven Plants","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Coal grinding plants ","Air","Particulates (PM10) (Annual Mean)","BAT for coal grinding plants (coal preparation including crushing, grinding, pulverising and screening) is to prevent or reduce dust emissions by using one or a combination of the following techniques: (i) building and/or device enclosure (crusher, pulveriser, sieves); (ii) efficient extraction and use of a subsequent dry dedusting systems.","mg/Nm3",10,20,"Green","Discontinuous ",0,0,"Unspecified ","Average over the sampling period",0]
["LCP","1. Energy industries","Unspecified","Unspecified","IGCC","Unspecified","Unspecified","≥ 100 MWth","Unspecified","Air","Particulates (PM10) (Annual Mean)",0,"mg/Nm3","N/A","0.025","Green","Continuous",0,0,0.15,"Average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","IGCC","Unspecified","Unspecified","≥ 100 MWth","Unspecified","Air","Particulates (PM10) (Annual Mean)",0,"mg/Nm3","N/A","0.025","Green","Continuous",0,0,0.15,"Average over the sampling period",0]
["LCP","1. Energy industries","Unspecified","Unspecified","IGCC","Unspecified","Unspecified","≥ 100 MWth","Unspecified","Air","Particulates (PM10) (Annual Mean)",0,"ug/Nm3","N/A","1","Green","Continuous",0,0,0.15,"Average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LCP","1. Energy industries","Unspecified","Unspecified","IGCC","Unspecified","Unspecified","≥ 100 MWth","Unspecified","Air","Particulates (PM10) (Annual Mean)",0,"ug/Nm3","N/A","1","Green","Continuous",0,0,0.15,"Average over the sampling period",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Alumina and Anode production","Primary aluminium production","Unspecified","Unspecified","Unspecified","Unspecified","Storage, handling and transport of raw materials","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust emissions from the storage, handling and transport of raw materials, BAT is to use a bag filter.","mg/Nm3",5,10,"Green","Oncer per year ",0,0,0,"Average over sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Alumina and Anode production","Primary aluminium production","Unspecified","Unspecified","Unspecified","Unspecified","Storage, handling and transport of raw materials","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust emissions from the storage, handling and transport of raw materials, BAT is to use a bag filter.","mg/Nm3",5,10,"Green","Oncer per year ",0,0,0,"Average over sampling period",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Alumina and Anode production","Secondary aluminium production ","Unspecified","Unspecified","Unspecified","Unspecified","Remelting","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust and metal emissions to air from remelting in secondary aluminium production, BAT is to use one or a combination of the techniques given below: (i) Use of uncontaminated aluminium material i.e. solid material free of substances such as paint, plastic\nor oil (e.g. billets); (ii) Optimise combustion conditions to reduce the emissions of dust; (iii) Bag filter","mg/Nm3",2,5,"Green","Once per year",0,0,0,"Average over the sampling period","For furnaces designed to use and using only uncontaminated raw material, for which dust emissions are below 1 kg/h, the upper end of the range is 25 mg/Nm3 as an average of the samples obtained over a year.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Alumina and Anode production","Secondary aluminium production ","Unspecified","Unspecified","Unspecified","Unspecified","Remelting","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust and metal emissions to air from remelting in secondary aluminium production, BAT is to use one or a combination of the techniques given below: (i) Use of uncontaminated aluminium material i.e. solid material free of substances such as paint, plastic\nor oil (e.g. billets); (ii) Optimise combustion conditions to reduce the emissions of dust; (iii) Bag filter","mg/Nm3",2,5,"Green","Once per year",0,0,0,"Average over the sampling period","For furnaces designed to use and using only uncontaminated raw material, for which dust emissions are below 1 kg/h, the upper end of the range is 25 mg/Nm3 as an average of the samples obtained over a year."]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Alumina and Anode production","Secondary aluminium production ","Unspecified","Unspecified","Unspecified","Unspecified","Swarf drying and the removal of oil and organic compounds from the swarf, from the crushing, milling and dry separation of non-metallic constituents and metals other than aluminium, and from the storage, handling and transport","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust and metal emissions from the swarf drying and the removal of oil and organic compounds from the swarf, from the crushing, milling and dry separation of non-metallic constituents and metals other than aluminium, and from the storage, handling and transport in secondary aluminium production, BAT is to use a bag filter.","mg/Nm3","N/A",5,"Green","Oncer per year ",0,0,0,"Average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Alumina and Anode production","Secondary aluminium production ","Unspecified","Unspecified","Unspecified","Unspecified","Swarf drying and the removal of oil and organic compounds from the swarf, from the crushing, milling and dry separation of non-metallic constituents and metals other than aluminium, and from the storage, handling and transport","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust and metal emissions from the swarf drying and the removal of oil and organic compounds from the swarf, from the crushing, milling and dry separation of non-metallic constituents and metals other than aluminium, and from the storage, handling and transport in secondary aluminium production, BAT is to use a bag filter.","mg/Nm3","N/A",5,"Green","Oncer per year ",0,0,0,"Average over the sampling period",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Carbon and Graphite Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Baking","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust and PAH emissions to air from baking, BAT is to use one or a combination of the techniques given below: (i) ESP, in combination with a thermal oxidation step (e.g.\nregenerative thermal oxidiser) when highly volatile\ncompounds are expected; (ii) Regenerative thermal oxidiser, in combination with a\npretreatment (e.g. ESP) in cases of a high dust content\nin the exhaust gas; (iii) Thermal oxidiser","mg/Nm3",2,10,"Green","Once per year",0,0,0,"Average over the sampling period","The lower end of the range is associated with the use of a combination of an ESP and a regenerative thermal oxidiser. The higher end of the range is associated with the use of a thermal oxidiser.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Carbon and Graphite Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Baking","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust and PAH emissions to air from baking, BAT is to use one or a combination of the techniques given below: (i) ESP, in combination with a thermal oxidation step (e.g.\nregenerative thermal oxidiser) when highly volatile\ncompounds are expected; (ii) Regenerative thermal oxidiser, in combination with a\npretreatment (e.g. ESP) in cases of a high dust content\nin the exhaust gas; (iii) Thermal oxidiser","mg/Nm3",2,10,"Green","Once per year",0,0,0,"Average over the sampling period","The lower end of the range is associated with the use of a combination of an ESP and a regenerative thermal oxidiser. The higher end of the range is associated with the use of a thermal oxidiser."]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Carbon and Graphite Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Impregnation","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust and PAH emissions to air from impregnation, BAT is to use one or a combination of the techniques given below: (i) Dry scrubber followed by a bag filter; (ii) Coke filter; (iii) Thermal oxidiser","mg/Nm3",2,10,"Green","Once per year",0,0,0,"Average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Carbon and Graphite Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Impregnation","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust and PAH emissions to air from impregnation, BAT is to use one or a combination of the techniques given below: (i) Dry scrubber followed by a bag filter; (ii) Coke filter; (iii) Thermal oxidiser","mg/Nm3",2,10,"Green","Once per year",0,0,0,"Average over the sampling period",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Carbon and Graphite Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Production of green paste and green shapes","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust and PAH emissions to air from the production of green paste and green shapes, BAT is to use one or a combination of the techniques given below: (i) Dry scrubber using coke as the adsorbent agent and with or without precooling, followed by a bag\nfilter; (ii) Coke filter; (iii) Regenerative thermal oxidiser; (iv) Thermal oxidiser","mg/Nm3",2,10,"Green","Once per year",0,0,0,"Average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Carbon and Graphite Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Production of green paste and green shapes","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust and PAH emissions to air from the production of green paste and green shapes, BAT is to use one or a combination of the techniques given below: (i) Dry scrubber using coke as the adsorbent agent and with or without precooling, followed by a bag\nfilter; (ii) Coke filter; (iii) Regenerative thermal oxidiser; (iv) Thermal oxidiser","mg/Nm3",2,10,"Green","Once per year",0,0,0,"Average over the sampling period",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Carbon and Graphite Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Storage, handling and transportation of coke and pitch, and mechanical processes (such as grinding) and graphitising and machining","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust emissions to air from the storage, handling and transportation of coke and pitch, and mechanical processes (such as grinding) and graphitising and machining, BAT is to use a bag filter.","mg/Nm3",2,5,"Green","Once per year",0,0,0,"Average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Carbon and Graphite Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Storage, handling and transportation of coke and pitch, and mechanical processes (such as grinding) and graphitising and machining","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust emissions to air from the storage, handling and transportation of coke and pitch, and mechanical processes (such as grinding) and graphitising and machining, BAT is to use a bag filter.","mg/Nm3",2,5,"Green","Once per year",0,0,0,"Average over the sampling period",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Copper production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Copper-rich slag furnace processing","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust and metal emissions to air from copper-rich slag furnace processing, BAT is to use a bag filter or a scrubber in combination with an ESP.","mg/Nm3",2,5,"Green","Once per year ",0,0,0,"Average over sampling period","Dust emissions are expected to be towards the lower end of the range when emissions of lead are above 1 mg/Nm3",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Copper production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Copper-rich slag furnace processing","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust and metal emissions to air from copper-rich slag furnace processing, BAT is to use a bag filter or a scrubber in combination with an ESP.","mg/Nm3",2,5,"Green","Once per year ",0,0,0,"Average over sampling period","Dust emissions are expected to be towards the lower end of the range when emissions of lead are above 1 mg/Nm3"]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Copper production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Reception,           storage,           handling,           transport,           metering,           mixing,           \nblending,  crushing,  drying,  cutting  and  screening  of  raw  \nmaterials,  and  the  pyrolytic  treatment  of  copper  turnings  \nin  primary  and  secondary  copper  production","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust and metal emissions to air from the reception, storage, handling, transport, metering, mixing, blending, crushing, drying, cutting and screening of raw materials, and the pyrolytic treatment of copper turnings in primary and secondary copper production, BAT is to use a bag filter.","mg/Nm3",2,5,"Green","Once per year ",0,0,0,"Average over sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Copper production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Reception,           storage,           handling,           transport,           metering,           mixing,           \nblending,  crushing,  drying,  cutting  and  screening  of  raw  \nmaterials,  and  the  pyrolytic  treatment  of  copper  turnings  \nin  primary  and  secondary  copper  production","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust and metal emissions to air from the reception, storage, handling, transport, metering, mixing, blending, crushing, drying, cutting and screening of raw materials, and the pyrolytic treatment of copper turnings in primary and secondary copper production, BAT is to use a bag filter.","mg/Nm3",2,5,"Green","Once per year ",0,0,0,"Average over sampling period",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Copper production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Secondary copper holding furnace","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust and metal emissions to air from the secondary copper holding furnace, BAT is to use a bag filter","mg/Nm3","N/A",5,"Green","Once per year ",0,0,0,"Average over sampling period","Dust emissions are expected to be towards the lower end of the range when emissions of heavy metals are above the following levels: 1 mg/Nm3 for lead, 1 mg/Nm3 for copper, 0,05 mg/Nm3 for arsenic, 0,05 mg/Nm3 for cadmium",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Copper production","All","Unspecified ","Unspecified","Unspecified","Unspecified","Secondary copper holding furnace","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust and metal emissions to air from the secondary copper holding furnace, BAT is to use a bag filter","mg/Nm3","N/A",5,"Green","Once per year ",0,0,0,"Average over sampling period","Dust emissions are expected to be towards the lower end of the range when emissions of heavy metals are above the following levels: 1 mg/Nm3 for lead, 1 mg/Nm3 for copper, 0,05 mg/Nm3 for arsenic, 0,05 mg/Nm3 for cadmium"]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Ferro alloys Production","All","Unspecified","Unspecified","Unspecified","Unspecified","— Storage, handling and transport of solid materials — Pretreatment operations such as metering, mixing, blending and degreasing — Tapping, casting and packaging","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust and metal emissions to air from the storage, handling and transport of solid materials, and from pretreatment operations such as metering, mixing, blending and degreasing, and from tapping, casting and packaging, BAT is to use a bag filter.","mg/Nm3",2,5,"Green","Continuous",0,0,0,"As an average over the sampling period.",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Ferro alloys Production","All","Unspecified","Unspecified","Unspecified","Unspecified","— Storage, handling and transport of solid materials — Pretreatment operations such as metering, mixing, blending and degreasing — Tapping, casting and packaging","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust and metal emissions to air from the storage, handling and transport of solid materials, and from pretreatment operations such as metering, mixing, blending and degreasing, and from tapping, casting and packaging, BAT is to use a bag filter.","mg/Nm3",2,5,"Green","Continuous",0,0,0,"As an average over the sampling period.",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Lead and Tin Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Battery preparation (crushing, screning and classifying) ","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust and metal emissions to air from battery preparation (crushing, screening and classifying), BAT is to use a bag filter or a wet scrubber.","mg/Nm3","N/A",5,"Green","Once per year",0,0,0,"Average over the sampling period ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Lead and Tin Production","All","Unspecified","Unspecified","Unspecified","Unspecified","Battery preparation (crushing, screning and classifying) ","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust and metal emissions to air from battery preparation (crushing, screening and classifying), BAT is to use a bag filter or a wet scrubber.","mg/Nm3","N/A",5,"Green","Once per year",0,0,0,"Average over the sampling period ",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Zinc and Cadmium Production","Cadmium Production","Unspecified","Unspecified","Unspecified","Unspecified","Pyrometallurgical cadmium production and the melting, alloying and casting of cadmium ingots","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust and metal emissions to air from pyrometallurgical cadmium production and the melting, alloying and casting of cadmium ingots, BAT is to use one or a combination of the techniques given below: (i) Bag filter; (ii) ESP; (iii) Wet scrubber ","mg/Nm3",2,3,"Green","Once per year",0,0,0,"Average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Zinc and Cadmium Production","Cadmium Production","Unspecified","Unspecified","Unspecified","Unspecified","Pyrometallurgical cadmium production and the melting, alloying and casting of cadmium ingots","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust and metal emissions to air from pyrometallurgical cadmium production and the melting, alloying and casting of cadmium ingots, BAT is to use one or a combination of the techniques given below: (i) Bag filter; (ii) ESP; (iii) Wet scrubber ","mg/Nm3",2,3,"Green","Once per year",0,0,0,"Average over the sampling period",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Zinc and Cadmium Production","Hydrometallurgical zinc production","Unspecified","Unspecified","Unspecified","Unspecified","Handling and storage of raw materials, dry roaster feed preparation, dry roaster feeding and calcine processing","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust and metal emissions to air from the handling and storage of raw materials, dry roaster feed preparation, dry roaster feeding and calcine processing, BAT is to use a bag filter.","mg/Nm3","N/A",5,"Green","Once per year",0,0,0,"Average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Zinc and Cadmium Production","Hydrometallurgical zinc production","Unspecified","Unspecified","Unspecified","Unspecified","Handling and storage of raw materials, dry roaster feed preparation, dry roaster feeding and calcine processing","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust and metal emissions to air from the handling and storage of raw materials, dry roaster feed preparation, dry roaster feeding and calcine processing, BAT is to use a bag filter.","mg/Nm3","N/A",5,"Green","Once per year",0,0,0,"Average over the sampling period",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Zinc and Cadmium Production","Melting, alloying and casting of zinc ingots and zinc power production","Unspecified","Unspecified","Unspecified","Unspecified","Melting, alloying and casting of zinc ingots and zinc powder production","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust and metal emissions to air from the melting, alloying and casting of zinc ingots and zinc powder production, BAT is to use a bag filter.","mg/Nm3","N/A",5,"Green","Once per year",0,0,0,"Average over the sampling period",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Zinc and Cadmium Production","Melting, alloying and casting of zinc ingots and zinc power production","Unspecified","Unspecified","Unspecified","Unspecified","Melting, alloying and casting of zinc ingots and zinc powder production","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust and metal emissions to air from the melting, alloying and casting of zinc ingots and zinc powder production, BAT is to use a bag filter.","mg/Nm3","N/A",5,"Green","Once per year",0,0,0,"Average over the sampling period",0]
["Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Zinc and Cadmium Production","Secondary ","Unspecified","Unspecified","Unspecified","Unspecified","Pelletising and slag processing","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust and metal emissions to air from pelletising and slag processing, BAT is to use a bag filter.","mg/Nm3","N/A",5,"Green","Once per year",0,0,0,"Average over the sampling period ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non Ferrous Metals Industries","2.  Processing of non-ferrous metals","Zinc and Cadmium Production","Secondary ","Unspecified","Unspecified","Unspecified","Unspecified","Pelletising and slag processing","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust and metal emissions to air from pelletising and slag processing, BAT is to use a bag filter.","mg/Nm3","N/A",5,"Green","Once per year",0,0,0,"Average over the sampling period ",0]
["Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Recovery boiler","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust and SO2 emissions from a recovery boiler, BAT is to use one of the techniques given below and to limit ‘acid operation’ of the scrubbers to the minimum required to ensure their proper functioning: (i) ESP or multicyclones with multistage venturi scrubbers; (ii) ESP or multicyclones with multistage double inlet downstream scrubbers","mg/Nm3",5,20,"Green","Periodic ",0,0," ","Average over the sampling period","For recovery boilers operated in mills using more than 25 % of hardwood (potassium-rich) in raw materials, higher dust emissions up to 30 mg/Nm3 may occur.\n\nThe BAT-AEL for dust does not apply for ammonium-based mills.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp and paper","6. Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Recovery boiler","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust and SO2 emissions from a recovery boiler, BAT is to use one of the techniques given below and to limit ‘acid operation’ of the scrubbers to the minimum required to ensure their proper functioning: (i) ESP or multicyclones with multistage venturi scrubbers; (ii) ESP or multicyclones with multistage double inlet downstream scrubbers","mg/Nm3",5,20,"Green","Periodic ",0,0," ","Average over the sampling period","For recovery boilers operated in mills using more than 25 % of hardwood (potassium-rich) in raw materials, higher dust emissions up to 30 mg/Nm3 may occur.\n\nThe BAT-AEL for dust does not apply for ammonium-based mills."]
["Refineries","1. Energy industries","Unspecified","Unspecified","All","Unspecified","All","Unspecified","Unit for calcining of green coke","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust emissions to air from the calcining of green coke process, BAT is to use a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Multistage cyclone\nseparators ","mg/Nm3",10,50,"Amber","Continuous",0,0,0,"Monthly ","The lower end of the range can be achieved with a 4-field ESP\n\nWhen an ESP is not applicable, values of up to 150 mg/Nm3 may occur. ",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Refineries","1. Energy industries","Unspecified","Unspecified","All","Unspecified","All","Unspecified","Unit for calcining of green coke","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust emissions to air from the calcining of green coke process, BAT is to use a combination of the techniques given below: (i) Electrostatic precipitator (ESP); (ii) Multistage cyclone\nseparators ","mg/Nm3",10,50,"Amber","Continuous",0,0,0,"Monthly ","The lower end of the range can be achieved with a 4-field ESP\n\nWhen an ESP is not applicable, values of up to 150 mg/Nm3 may occur. "]
["Refineries","1. Energy industries","Unspecified","Unspecified","All","Existing","All","Unspecified","Regenerator in the catalytic cracking process","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust and metals emissions to air from the catalytic cracking process (regenerator), BAT is to use one or a combination of the techniques given below:\n\nPrimary techniques:\n(i) Use of an attrition-resistant catalyst; (ii) Use of low sulphur feedstock (e.g. by feedstock selection or by hydrotreatment of feed) \n\nSecondary techniqyes:\n(i) Electrostatic precipitator (ESP); (ii) Multistage cyclone separators; (iii) Third stage blowback\nfilter; (iv) Wet scrubbing ","mg/Nm3",10,50,"Green","Continuous",0,0,0.03,"Monthly ","Soot blowing in CO boiler and through the gas cooler is excluded.\n\nThe lower end of the range can be achieved with a 4-field ESP.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Refineries","1. Energy industries","Unspecified","Unspecified","All","Existing","All","Unspecified","Regenerator in the catalytic cracking process","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust and metals emissions to air from the catalytic cracking process (regenerator), BAT is to use one or a combination of the techniques given below:\n\nPrimary techniques:\n(i) Use of an attrition-resistant catalyst; (ii) Use of low sulphur feedstock (e.g. by feedstock selection or by hydrotreatment of feed) \n\nSecondary techniqyes:\n(i) Electrostatic precipitator (ESP); (ii) Multistage cyclone separators; (iii) Third stage blowback\nfilter; (iv) Wet scrubbing ","mg/Nm3",10,50,"Green","Continuous",0,0,0.03,"Monthly ","Soot blowing in CO boiler and through the gas cooler is excluded.\n\nThe lower end of the range can be achieved with a 4-field ESP."]
["Refineries","1. Energy industries","Unspecified","Unspecified","All","New","All","Unspecified","Regenerator in the catalytic cracking process","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust and metals emissions to air from the catalytic cracking process (regenerator), BAT is to use one or a combination of the techniques given below:\n\nPrimary techniques:\n(i) Use of an attrition-resistant catalyst; (ii) Use of low sulphur feedstock (e.g. by feedstock selection or by hydrotreatment of feed) \n\nSecondary techniqyes:\n(i) Electrostatic precipitator (ESP); (ii) Multistage cyclone separators; (iii) Third stage blowback\nfilter; (iv) Wet scrubbing ","mg/Nm3",10,25,"Green","Continuous",0,0,0.03,"Monthly ","Soot blowing in CO boiler and through the gas cooler is excluded.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Refineries","1. Energy industries","Unspecified","Unspecified","All","New","All","Unspecified","Regenerator in the catalytic cracking process","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust and metals emissions to air from the catalytic cracking process (regenerator), BAT is to use one or a combination of the techniques given below:\n\nPrimary techniques:\n(i) Use of an attrition-resistant catalyst; (ii) Use of low sulphur feedstock (e.g. by feedstock selection or by hydrotreatment of feed) \n\nSecondary techniqyes:\n(i) Electrostatic precipitator (ESP); (ii) Multistage cyclone separators; (iii) Third stage blowback\nfilter; (iv) Wet scrubbing ","mg/Nm3",10,25,"Green","Continuous",0,0,0.03,"Monthly ","Soot blowing in CO boiler and through the gas cooler is excluded."]
["Refineries","1. Energy industries","Unspecified","Unspecified","All","Existing","All","Unspecified","Multi-fuel fired combustion unit  with the exception\nof gas turbines","Air","Particulates (PM10) (Annual Mean)","In order to prevent or reduce dust and metal emissions to air from the combustion units, BAT is to use one or a combination of the techniques given below: \n\nPrimary techniques:\n(i) Selection or treatment of fuel; (ii) Combustion modifications\n\nSecondary techniques:\n(i) Electrostatic precipitator (ESP); (ii) Third stage blowback filter; (iii) Wet scrubbing; (iv) Centrifugal washers ","mg/Nm3",5,50,"Amber",0,0,0,0.03,"Monthly ","The lower end of the range is achievable for units with the use of end-of-pipe techniques. \n\nThe upper end of the range refers to the use of a high percentage of oil burning and where only primary techniques are\napplicable.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Refineries","1. Energy industries","Unspecified","Unspecified","All","Existing","All","Unspecified","Multi-fuel fired combustion unit  with the exception\nof gas turbines","Air","Particulates (PM10) (Annual Mean)","In order to prevent or reduce dust and metal emissions to air from the combustion units, BAT is to use one or a combination of the techniques given below: \n\nPrimary techniques:\n(i) Selection or treatment of fuel; (ii) Combustion modifications\n\nSecondary techniques:\n(i) Electrostatic precipitator (ESP); (ii) Third stage blowback filter; (iii) Wet scrubbing; (iv) Centrifugal washers ","mg/Nm3",5,50,"Amber",0,0,0,0.03,"Monthly ","The lower end of the range is achievable for units with the use of end-of-pipe techniques. \n\nThe upper end of the range refers to the use of a high percentage of oil burning and where only primary techniques are\napplicable."]
["Refineries","1. Energy industries","Unspecified","Unspecified","All","New","All","<50 MW","Multi-fuel fired combustion unit  with the exception\nof gas turbines","Air","Particulates (PM10) (Annual Mean)","In order to prevent or reduce dust and metal emissions to air from the combustion units, BAT is to use one or a combination of the techniques given below: \n\nPrimary techniques:\n(i) Selection or treatment of fuel; (ii) Combustion modifications\n\nSecondary techniques:\n(i) Electrostatic precipitator (ESP); (ii) Third stage blowback filter; (iii) Wet scrubbing; (iv) Centrifugal washers ","mg/Nm3",5,25,"Green","Once a year and after significant fuel changes",0,0,0.03,"Monthly ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Refineries","1. Energy industries","Unspecified","Unspecified","All","New","All","<50 MW","Multi-fuel fired combustion unit  with the exception\nof gas turbines","Air","Particulates (PM10) (Annual Mean)","In order to prevent or reduce dust and metal emissions to air from the combustion units, BAT is to use one or a combination of the techniques given below: \n\nPrimary techniques:\n(i) Selection or treatment of fuel; (ii) Combustion modifications\n\nSecondary techniques:\n(i) Electrostatic precipitator (ESP); (ii) Third stage blowback filter; (iii) Wet scrubbing; (iv) Centrifugal washers ","mg/Nm3",5,25,"Green","Once a year and after significant fuel changes",0,0,0.03,"Monthly ",0]
["Woodbased Panels Production","6.   Other activities","Unspecified","Fibre","Unspecified","Unspecified","Unspecified","Unspecified","Dryer- all types ","Air","Particulates (PM10) (Annual Mean)","In order to prevent or reduce emissions to air from the dryer, BAT is to achieve and manage a balanced operation of the\ndrying process and to use one or a combination of the techniques given below: (i) Dust abatement of inlet hot gas to a\ndirectly heated dryer in combination with one or a combination of the other techniques listed below; (ii) Bag filter; (iii) Cyclone; (iv) UTWS dryer and combustion with heat exchanger and thermal treatment of discharged dryer waste gasl (v) Wet electrostatic precipitator; (vi) Wet scrubber; (vii) Bioscrubber; (viii) Chemical degradation or capture of formaldehyde with chemicals in combination with a wet scrubbing system \n\n","mg/Nm3",3,20,"Green","Periodic (at least once every 6 months)",0,0,"N/A","Average over sampling period ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Woodbased Panels Production","6.   Other activities","Unspecified","Fibre","Unspecified","Unspecified","Unspecified","Unspecified","Dryer- all types ","Air","Particulates (PM10) (Annual Mean)","In order to prevent or reduce emissions to air from the dryer, BAT is to achieve and manage a balanced operation of the\ndrying process and to use one or a combination of the techniques given below: (i) Dust abatement of inlet hot gas to a\ndirectly heated dryer in combination with one or a combination of the other techniques listed below; (ii) Bag filter; (iii) Cyclone; (iv) UTWS dryer and combustion with heat exchanger and thermal treatment of discharged dryer waste gasl (v) Wet electrostatic precipitator; (vi) Wet scrubber; (vii) Bioscrubber; (viii) Chemical degradation or capture of formaldehyde with chemicals in combination with a wet scrubbing system \n\n","mg/Nm3",3,20,"Green","Periodic (at least once every 6 months)",0,0,"N/A","Average over sampling period ",0]
["Woodbased Panels Production","6.   Other activities","Unspecified","PB or OSB","Unspecified","Unspecified","Unspecified","Unspecified","Dryer- Directly heated","Air","Particulates (PM10) (Annual Mean)","In order to prevent or reduce emissions to air from the dryer, BAT is to achieve and manage a balanced operation of the\ndrying process and to use one or a combination of the techniques given below: (i) Dust abatement of inlet hot gas to a\ndirectly heated dryer in combination with one or a combination of the other techniques listed below; (ii) Bag filter; (iii) Cyclone; (iv) UTWS dryer and combustion with heat exchanger and thermal treatment of discharged dryer waste gasl (v) Wet electrostatic precipitator; (vi) Wet scrubber; (vii) Bioscrubber; (viii) Chemical degradation or capture of formaldehyde with chemicals in combination with a wet scrubbing system \n\n","mg/Nm3",3,30,"Green","Periodic (at least once every 6 months)",0,0,0.15,"Average over sampling period ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Woodbased Panels Production","6.   Other activities","Unspecified","PB or OSB","Unspecified","Unspecified","Unspecified","Unspecified","Dryer- Directly heated","Air","Particulates (PM10) (Annual Mean)","In order to prevent or reduce emissions to air from the dryer, BAT is to achieve and manage a balanced operation of the\ndrying process and to use one or a combination of the techniques given below: (i) Dust abatement of inlet hot gas to a\ndirectly heated dryer in combination with one or a combination of the other techniques listed below; (ii) Bag filter; (iii) Cyclone; (iv) UTWS dryer and combustion with heat exchanger and thermal treatment of discharged dryer waste gasl (v) Wet electrostatic precipitator; (vi) Wet scrubber; (vii) Bioscrubber; (viii) Chemical degradation or capture of formaldehyde with chemicals in combination with a wet scrubbing system \n\n","mg/Nm3",3,30,"Green","Periodic (at least once every 6 months)",0,0,0.15,"Average over sampling period ",0]
["Woodbased Panels Production","6.   Other activities","Unspecified","PB or OSB","Unspecified","Unspecified","Unspecified","Unspecified","Dryer-Indirectly heated ","Air","Particulates (PM10) (Annual Mean)","In order to prevent or reduce emissions to air from the dryer, BAT is to achieve and manage a balanced operation of the\ndrying process and to use one or a combination of the techniques given below: (i) Dust abatement of inlet hot gas to a\ndirectly heated dryer in combination with one or a combination of the other techniques listed below; (ii) Bag filter; (iii) Cyclone; (iv) UTWS dryer and combustion with heat exchanger and thermal treatment of discharged dryer waste gasl (v) Wet electrostatic precipitator; (vi) Wet scrubber; (vii) Bioscrubber; (viii) Chemical degradation or capture of formaldehyde with chemicals in combination with a wet scrubbing system \n\n","mg/Nm3",3,10,"Green","Periodic (at least once every 6 months)",0,0,0.15,"Average over sampling period ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Woodbased Panels Production","6.   Other activities","Unspecified","PB or OSB","Unspecified","Unspecified","Unspecified","Unspecified","Dryer-Indirectly heated ","Air","Particulates (PM10) (Annual Mean)","In order to prevent or reduce emissions to air from the dryer, BAT is to achieve and manage a balanced operation of the\ndrying process and to use one or a combination of the techniques given below: (i) Dust abatement of inlet hot gas to a\ndirectly heated dryer in combination with one or a combination of the other techniques listed below; (ii) Bag filter; (iii) Cyclone; (iv) UTWS dryer and combustion with heat exchanger and thermal treatment of discharged dryer waste gasl (v) Wet electrostatic precipitator; (vi) Wet scrubber; (vii) Bioscrubber; (viii) Chemical degradation or capture of formaldehyde with chemicals in combination with a wet scrubbing system \n\n","mg/Nm3",3,10,"Green","Periodic (at least once every 6 months)",0,0,0.15,"Average over sampling period ",0]
["Woodbased Panels Production","6.   Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Press","Air","Particulates (PM10) (Annual Mean)","In order to prevent or reduce emissions to air from the press, BAT is to use in-duct quenching of collected press waste gas and an appropriate combination of the techniques given below.: (i) Select resins with a low formaldehyde content; (ii) Controlled operation of the press with balanced press temperature, applied pressure and press speed; (iii) Wet scrubbing of collected press\nwaste gases using Venturi scrubbers or hydrocyclones, etc.; (iv) Wet electrostatic precipitator; (v) Bioscrubber; (vi) Post-combustion as the last treatment step after application of a wet scrubber ","mg/Nm3",3,15,"Green","Periodic (at least once every 6 months)",0,0,"N/A","Average over sampling period ",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Woodbased Panels Production","6.   Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Press","Air","Particulates (PM10) (Annual Mean)","In order to prevent or reduce emissions to air from the press, BAT is to use in-duct quenching of collected press waste gas and an appropriate combination of the techniques given below.: (i) Select resins with a low formaldehyde content; (ii) Controlled operation of the press with balanced press temperature, applied pressure and press speed; (iii) Wet scrubbing of collected press\nwaste gases using Venturi scrubbers or hydrocyclones, etc.; (iv) Wet electrostatic precipitator; (v) Bioscrubber; (vi) Post-combustion as the last treatment step after application of a wet scrubber ","mg/Nm3",3,15,"Green","Periodic (at least once every 6 months)",0,0,"N/A","Average over sampling period ",0]
["Woodbased Panels Production","6.   Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Upstream and downstream wood processing, conveying of wood materials and mat forming ","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust emissions to air from upstream and downstream wood processing, conveying of wood materials and mat forming, BAT is to use either a bag filter or a cyclofilter.","mg/Nm3",3,5,"Green","Periodic (at least once a year)",0,0,"N/A","Average over sampling period ","When a bag filter or a cyclofilter is not applicable, the upper end of the range can be up to 10 mg/Nm3",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Woodbased Panels Production","6.   Other activities","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Upstream and downstream wood processing, conveying of wood materials and mat forming ","Air","Particulates (PM10) (Annual Mean)","In order to reduce dust emissions to air from upstream and downstream wood processing, conveying of wood materials and mat forming, BAT is to use either a bag filter or a cyclofilter.","mg/Nm3",3,5,"Green","Periodic (at least once a year)",0,0,"N/A","Average over sampling period ","When a bag filter or a cyclofilter is not applicable, the upper end of the range can be up to 10 mg/Nm3"]
["Iron and steel","2. Production and processing of metals","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Electric arc furnace steelmaking and casting: Waste water from continous casting machines ","Air","Chromium, chromium (II) compounds and chromium (III) compounds as Cr","BAT is to minimise the waste water discharge from continuous casting by using the following techniques in combination: (i) the removal of solids by flocculation, sedimentation and/or filtration; (ii) the removal of oil in skimming tanks or any other effective device; (iii) the recirculation of cooling water and water from vacuum generation as much as possible","mg/Nm3","N/A",0.5,"Green","Discontinuous ",0,0,"Unspecified ","Qualified random sample or a 24 hour composite",0,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Iron and steel","2. Production and processing of metals","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Electric arc furnace steelmaking and casting: Waste water from continous casting machines ","Air","Chromium, chromium (II) compounds and chromium (III) compounds as Cr","BAT is to minimise the waste water discharge from continuous casting by using the following techniques in combination: (i) the removal of solids by flocculation, sedimentation and/or filtration; (ii) the removal of oil in skimming tanks or any other effective device; (iii) the recirculation of cooling water and water from vacuum generation as much as possible","mg/Nm3","N/A",0.5,"Green","Discontinuous ",0,0,"Unspecified ","Qualified random sample or a 24 hour composite",0]

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["Sector","IED Annex I Activity Category","Product / sub-sector","Sub-Product / sub-sub-sector","Plant type","Plant age","Fuel type","Plant capacity","Emission Source","Release type","Pollutant","BAT","BAT-AEL units","BAT-AEL lower value","BAT-AEL upper value","Colour","Monitoring","Reference temperature (K)","Reference Pressure (kPa)","Reference O2 content (% waste gas volume)","Averaging period","Notes","Notes"]

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[null,null,"Product",null,null,null,null,null,null,null,null,null,null,"Plant type",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Plant age",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"REF","Alumina",null,null,null,null,null,null,null,null,null,null,null,"LCP starts"]
[null,"Sector","Product / sub-sector glass","Product / sub-sector  Iron and steel","Product / sub-sector  Tanning of Hides and Skins","Product / sub-sector  Cement, lime and MgO","Product / sub-sector  Chlor-Alkali","Product / sub-sector  Pulp and paper","Product / sub-sector  Refineries","Product / sub-sector  Wood-based Panels Production","Product / sub-sector  Non-ferrous Metals Industries","Product / sub-sector  Common Waste Water and Waste Gas Treatment","Product / sub-sector  LCP","Mineral wool","Filament glass fibre","Container glass","Domestic glass","Flat glass","Frits ","HTIW wools","Special glass ","Coke Oven Plants","Other","Pelletisation plans","Sinter Plant","Extraction ventilation and abatement system is used as an alternative to the use of waterborne finishing materials","Post treatment","Unspecified","Lime","Magnesium oxide","Cement","Chloralkali industry","Unspecified","Excluding speciality paper ","Bleached kraft pulp mill","Bleached sulphite paper grade pulp   ","Paper and board from recycled fibres pulp produced with deinking on site ","Paper and board from recycled fibres pulp produced without deinking on site ","Magnefite paper grade pulp","NSSC pulp","Paper and board","Unbleached fraft pulp mill","Tissue paper excluding speciality paper","Paper and board from mechanical pupls produced on site","Unspecified","Unspecified","Alumina and Anode production","Carbon and Graphite Production","Zinc and Cadmium Production","Metals Production","Nickel and Cobalt Production","Aluminium Production","Copper production","Ferro alloys Production","Lead and Tin Production","All","Precious metals","Unspecified","Unspecified",null,"Mineral wool","Filament glass fibre","Container glass","Domestic glass","Flat glass","Frits ","HTIW wools","Special glass ","Coke Oven Plants","Other","Pelletisation plans","Sinter Plant","Extraction ventilation and abatement system is used as an alternative to the use of waterborne finishing materials","Post treatment","Unspecified","Lime","Lime","Lime","Lime","Lime","Lime","Lime","Lime","Magnesium oxide","Cement","Cement","Cement",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Sub-Product / sub-sub-sector","Plant age","Fuel type","Plant capacity","Emission Source","Release type","Pollutant",null,null,null,null,null,"Measurement",null,null,"Country"]
[null,"Glass","Mineral wool","Coke Oven Plants","Extraction ventilation and abatement system is used as an alternative to the use of waterborne finishing materials","Lime","Chloralkali industry","Unspecified","Unspecified","Unspecified","Alumina and Anode production","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","PFRK, OSK, LRK, PRK","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified",null,"Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","PFRK, OSK, LRK, PRK","ESP or other filters","Fabric filter","Wet scrubber","Unspecified","LRK, PRK","PFRK, ASK, MFSK, OSK","ASK, MFSK, PFRK","Unspecified","Unspecified","Lepol and long rotary kilns","Preheater kilns","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","All","Coalfired PC boiler","FBC boiler combusting coal andor lignite and lignitefired PC boiler","Boilers","CCGT","Fired engines ","IGCC","Spark ignited lean burn gas engine","CCGT with a net total fuel utilisation of less than 75 %","CCGT with a net total fuel utilisation of equal or more than 75 %","Dual fuel gas turbines ","Engine","Gas turbine for mechanical drive applications. All but plants operated less than 500 h per yr","Gas turbine put into operation no later than 27 November 2003 or existing gas turbine for emergency use and operated less than 500 h per yr","OCGT","OCGT (excluding turbines for mechanical drive applications) — All but plants operated < 500 h/yr","Opencycle gas turbines on offshore platforms","Biomass, peat, coal and or lignite fired combustion plant","Fluidised bed boiler","Gas turbines including dual fuel turbines","PC boiler ",null,null,null,"Unspecified","Unspecified","Unspecified","Unspecified","Kiln firing process","Air","Carbon monoxide, expressed as CO ",null,null,null,null,null,"Continuous",null,null,"Environment Agency"]
[null,"Iron and steel","Filament glass fibre","Other","Post treatment","Magnesium oxide",null,"Excluding speciality paper ",null,null,"Carbon and Graphite Production",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"ESP or other filters",null,"Lepol and long rotary kilns",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"All",null,"Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Unspecified","Plants operated more than 1 500 h per yr or for new combustion plants","Plants operated more than 1 500 h per yr or for new combustion plants","Plants operated more than 1 500 h per yr or for new combustion plants","Unspecified","Unspecified","New","Unspecified","Unspecified","Existing","Existing","Unspecified","Existing","Existing","Existing","New","Existing","New","Unspecified","Existing","New and existing ","Existing",null,null,null,"Glass wool ","New or substantially revamped","Natural gas ","< 300 MWth ","Chanelled dust emissions from dusty oeprations","Water","Particulates (PM10) (24 hr Mean)",null,null,null,null,null,"Estimated",null,null,"Natural Resources Wales"]
[null,"Tanning of Hides and Skins","Container glass","Pelletisation plans","Unspecified","Cement",null,"Bleached kraft pulp mill",null,null,"Zinc and Cadmium Production",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Fabric filter",null,"Preheater kilns",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Coalfired PC boiler",null,null,null,null,null,null,null,null,null,"New or substantially revamped",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Existing","New",null,null,null,null,null,null,null,null,null,null,null,null,"Existing","Existing","Existing","New","New","Existing","New","New",null,null,null,"New",null,null,null,null,"Existing",null,"New",null,"New",null,null,null,"Stone wool","Plants operated ≥ 1 500 h/yr or for new combustion plants","Electric melting","≥ 300 MWth","Cooling and milling processes","Consumption","Mercury and compounds, except mercury alkyls, (as",null,null,null,null,null,"Spot",null,null,"Northern Ireland Environment Agency"]
[null,"Cement lime and MgO","Domestic glass","Sinter Plant",null,null,null,"Bleached sulphite paper grade pulp   ",null,null,"Metals Production",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Wet scrubber",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"FBC boiler combusting coal andor lignite and lignitefired PC boiler",null,null,null,null,null,null,null,null,null,"Old",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"New","Existing",null,null,null,null,null,null,null,null,null,null,null,null,"New","New","New","Existing","Existing",null,"Existing","Existing",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"All products","New","Fuel oil","Unspecified ","Unspecified",null,"Hydrogen chloride, expressed as HCl",null,null,null,null,null,null,null,null,"Scottish Environment Protection Agency"]
[null,"Chlor Alkali","Flat glass",null,null,null,null,"Paper and board from recycled fibres pulp produced with deinking on site ",null,null,"Nickel and Cobalt Production",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Unspecified",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Boilers",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Lead crystal glass","Existing","Natural gas, Electric melting","<100 MWth","Kiln firing proceeses",null,"Hydrogen flouride, expressed as HF"]
[null,"Pulp and paper","Frits ",null,null,null,null,"Paper and board from recycled fibres pulp produced without deinking on site ",null,null,"Aluminium Production",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"LRK, PRK",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"CCGT",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Nitrates in batch formulation","New and existing ","Co-incineration of waste with coal and/or lignite","≥ 1 000 MWth","Kiln firing processes",null,"Metals (Cd, Tl) "]
[null,"Refineries","HTIW wools",null,null,null,null,"Magnefite paper grade pulp",null,null,"Copper production",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"PFRK, ASK, MFSK, OSK",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Fired engines ",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Glass wool",null,"Co-incineration of waste with biomass and/or peat","100-300 MWth","Processing of chlorine",null,"Metals( As, Sb, Pb, Cr, Co, Cu, Mn, Ni, V)",null,null,null,null,null,null,null,null,"Environment Agency/Natural Resources Wales/Northern Ireland Environment Agency"]
[null,"Woodbased Panels Production","Special glass ",null,null,null,null,"NSSC pulp",null,null,"Ferro alloys Production",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"ASK, MFSK, PFRK",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"IGCC",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Colored Glass",null,"Coal and/or lignite ","300-1000 MWth","Whole plant",null,"NH3 slip "]
[null,"Non ferrous Metals Industries",null,null,null,null,null,"Paper and board",null,null,"Lead and Tin Production",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Spark ignited lean burn gas engine",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Anode production",null,"Solid biomass and/or peat","< 100 MWth","Downstream processes- Curing oven emissions ",null,"Nitrogen dioxide"]
[null,"Common Waste Water and Waste Gas Treatment",null,null,null,null,null,"Unbleached fraft pulp mill",null,null,"All",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"CCGT with a net total fuel utilisation of less than 75 %",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"All",null,"100% iron and steel process gases ","≥ 50 MWth","Downstream processes- Forming area ",null,"PCDD/F"]
[null,"LCP",null,null,null,null,null,"Tissue paper excluding speciality paper",null,null,"Precious metals",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"CCGT with a net total fuel utilisation of equal or more than 75 %",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Cadmium Production",null,"100 % process fuels from the chemical industry in boilers","≥ 100 MWth","Downstream processes (forming and coating)",null,"Sulphur Dioxide (24 Hour Mean)"]
[null,null,null,null,null,null,null,"Paper and board from mechanical pupls produced on site",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Dual fuel gas turbines ",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Secondary aluminium production ",null,"HFO and/or gas oil in boilers","< 100 MWth ","Downstream processes",null,"Total organic compounds"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Engine",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Primary aluminium production",null,"HFO and/or gas oil in reciprocating engines","50-600 MWth","Melting furnace",null,"Chlorine"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Gas turbine for mechanical drive applications. All but plants operated less than 500 h per yr",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Salt slag recycling process",null,"Process fuels from the chemical industry","50-100 MWth","Dusty downstreatm processes ",null,"Chlorine (95%ile)"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Gas turbine put into operation no later than 27 November 2003 or existing gas turbine for emergency use and operated less than 500 h per yr",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Primary and secondary ",null,"Coal","≥ 600 MWth","Downstream processes (cutting and milling)",null,"Adsorbable organically bound halogens (AOX)"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"OCGT",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Hydrometallurgical zinc production",null,"Lignite","All sizes","Downstream processes ",null,"COD"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"OCGT (excluding turbines for mechanical drive applications) — All but plants operated < 500 h/yr",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Melting, alloying and casting of zinc ingots and zinc power production",null,"Gases only ","Gaseous fuels ","Acid polishing processes",null,"Chromium VI (95%ile) (dissolved)"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Opencycle gas turbines on offshore platforms",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pyrometallurgical zinc production",null,"Mixture of gases and liquids","Liquid fuels","Lubricant burn-off oven ",null,"Copper (expressed as Cu)"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Biomass, peat, coal and or lignite fired combustion plant",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Secondary ",null,"Gas oil ","<50 MW","Unspecified",null,"Nickel and its compounds"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Fluidised bed boiler",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Wet strength paper ",null,"Gaseous fuels ",null,"Coke grading and handling",null,"Total inorganic nitrogen (Ninorg)"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Gas turbines including dual fuel turbines",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Tissue Paper",null,"Co-incineration of waste with biomass, peat, coal and/or lignite",null,"Coke pushing",null,"Total Nitrogen (TN)"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"PC boiler ",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Fibre",null,"100 % process fuels from the chemical industry",null,"Coke quenching",null,"Total Organic Carbon (TOC)"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"PB or OSB",null,"All",null,"Basic Oxygen Steelmaking and Casting: Basic oxygen furnace (BOF) gas recovery by supressed combustion",null,"Total phosphorous"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"OSB",null,"Refinery fuel gas (RFG)",null,"Basic Oxygen Steelmaking and Casting: Basic oxygen furnace (BOF) gas recovery during oxygen blowing in the case of full combustion",null,"Total Suspended Solids (TSS) "]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"PB",null,null,null,"Basic Oxygen Steelmaking and Casting: On-site slag processing ",null,"Zinc (expressed as Zn)"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Impregnation of paper ",null,null,null,"Basic Oxygen Steelmaking and Casting: Secondary dusting, reladling of hot metal from the torpedo ladle, hot metal pretreatment, BOF-related processes, secondary metallurgy and continuous casting",null,"Amines"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Wood fibre",null,null,null,"Basic Oxygen Steelmaking and Casting: Waste water from continous casting machines ",null,"Ammonia (ecological receptor - Sensitive Lichens)"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Blast Furnaces: Blast furnace gas ",null,"Formaldehyde"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Blast Furnaces: casting house ",null,"Hydrogen chloride"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Blast Furnaces: Hot blast stoves",null,"Hydrogen fluoride (as F) (Ecological - Daily Mean)"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Blast Furnaces: Loading from the storage bunkers of the coal injection unit",null,"Hydrogen sulphide"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Electric arc furnace steelmaking and casting: Electric Arc Furnace (EAF) primary and secondary dedusting",null,"Lead"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Electric arc furnace steelmaking and casting: On-site slag processing ",null,"Metals (Group 1 + Group 2)"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Crushing. Grinding and drying",null,"Metals (Group 1)"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Induration strand; Pellet handling and screening ",null,"Metals (Group 1+ Group 2) "]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Sinter strand",null,"Phenol"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Coal charging systems ",null,"Selenium and compounds, except hydrogen selenide (as Se)"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Storage and handling of pulverised coal",null,"SOX expressed as SO3"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Induration strand",null,"SOX expressed as SO4"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Electric arc furnace steelmaking and casting: Waste water from continous casting machines ",null,"SOX expressed as SO5"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Coke oven gas (COG)",null,"Tin compounds, including organotin, expressed as Sn"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Blast Furnaces: Pretreated waste water from the coking process and coke oven gas (COG)",null,"Titanium compounds expressed as Ti"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Coal grinding plants ",null,"VOC"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Baking plant in a stand-alone anode production plant",null,"Iron"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Baking plant with a primary aluminium smelter ",null,"Nickel (total Ni compounds in the PM10 fraction)"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Paste plant (hot pitch storage, paste\nmixing, cooling and forming)",null,"Suspended solids"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Baking",null,"Chromium (VI) compounds (as Cr)"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Impregnation",null,"Total hydrocarbons"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Production of green paste and green shapes",null,"Zinc"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Storage, handling and transportation of coke and pitch, and mechanical processes (such as grinding) and graphitising and machining",null,"Cadmium and its compounds (as Cd)"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pyrometallurgical cadmium production and the melting, alloying and casting of cadmium ingots",null,"Carbon monoxide"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Thermal treatment of contaminated secondary raw materials (e.g. swarf), the melting furnace, and remelting and molten metal treatment",null,"Particulates (PM10) (Annual Mean)"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Hydrometallurgical operation, including the associated incineration, calcining and drying operations",null,"Formaldehyde and CH4"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Atmospheric or pressure leaching processes",null,"Sb + As + Pb + Cr + Co + Cu + Mn + Ni + V"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Electrolysis house (collected from the electrolytic cells and roof vents) ",null,"Benzo-a-pyrene"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Electrolytic cells",null,"Sulphuric acid"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Melting and molten metal treatment and casting",null,"Phosphine"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Storage, handling and transport of raw materials",null,"Sum of AsH3 and SbH3"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Furnace processes such as charging, melting, tapping and molten metal treatment",null,"Total fluorides"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Remelting",null,"Gaseous S (TRS- S + SO2-S) DS 75- 83%"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Swarf drying and the removal of oil and organic compounds from the swarf, from the crushing, milling and dry separation of non-metallic constituents and metals other than aluminium, and from the storage, handling and transport",null,"Gaseous S (TRS- S + SO2-S) DS< 75%"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Crushing and dry milling associated with the salt slag recovery process",null,"Gaseous S (TRS-S + SO2-S)"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Anode casting (in primary and secondary copper production)",null,"Gaseous S (TRS-S + SO2-S) when strong gases are burnt in the lime kiln"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Anode furnace (in primary and secondary copper production)",null,"Gaseous S (TRS-S + SO2-S) when strong gases are not burnt in the lime kiln"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Concentrate drying in primary copper production",null,"NH3 (ammonia slip from SNCR)"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Copper melting furnace",null,"NOx (Hardwood)"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Copper-rich slag furnace processing",null,"NOx (Hardwood) DS < 75%"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Primary copper smelter and converter (emissions other than those that are routed to the sulphuric acid or liquid SO2 plant or power plant)",null,"NOx (Hardwood) DS 75-83%"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Reception,           storage,           handling,           transport,           metering,           mixing,           \nblending,  crushing,  drying,  cutting  and  screening  of  raw  \nmaterials,  and  the  pyrolytic  treatment  of  copper  turnings  \nin  primary  and  secondary  copper  production",null,"NOx (softwood)"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Secondary copper holding furnace",null,"NOx (softwood) DS 75- 83%"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Secondary copper smelter and converter and processing of secondary copper intermediates (emissions other than those that are routed to the sulphuric acid plant)",null,"NOx (softwood) DS< 75%"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"— Closed submerged arc furnace or closed plasma\ndust process\n— Refractory-lined crucible for the production of\nferro-molybdenum and ferro-vanadium",null,"Total Reduced Sulphur (TRS) "]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"— Storage, handling and transport of solid materials — Pretreatment operations such as metering, mixing, blending and degreasing — Tapping, casting and packaging",null,"Benzene"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Crushing, briquetting, pelletising and sintering",null,"NMVOC"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Open or semi-closed submerged arc furnace",null,"NOX, expressed as NO2"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Battery preparation (crushing, screning and classifying) ",null,"NOX, expressed as NO3"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Charging, smelting and tapping",null,"NOX, expressed as NO4"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Raw material preparation",null,"BOD5"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Remelting, refining and casting",null,"Cadmium and its compounds (< 40 mg/l Ca CO3)"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Crushing, sieving, mixing, melting, smelting, incineration, calcining, drying and refining",null,"Hydrocarbon oil index (HOI)"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Handling and storage of raw materials, material pretreatment processes (such as ore preparation and ore/concentrate drying), furnace charging, smelting, converting, thermal refining and nickel powder and briquette production",null,"Lead and its compounds"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Handling and storage of raw materials, dry roaster feed preparation, dry roaster feeding and calcine processing",null,"Mercury and its compounds"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Melting, alloying and casting of zinc ingots and zinc powder production",null,"Phenol Index"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pyrometallurgical zinc production",null,"Vanadium (> 200 mg/l CaCO3)"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Melting of metallic and mixed metallic/oxidic streams, and from the slag fuming furnace and the Waelz kiln",null,"Water"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pelletising and slag processing",null,"Solvent use levels"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Wet milling and leaching from the salt slag recovery process",null,"Un-ionised ammonia as nitrogen"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Leaching, purification and electrolysis, and to reduce arsane and stibane emissions from purification",null,"Sulphide (as S)"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pyrometallurgical process",null,"Total chromium (as Cr)"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Hydrometallurgical operation using ammonia or ammonium chloride",null,"Cadmium and its compounds (≥ 200 mg/l CaCO3)"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Nickel matte refining process using ferric\nchloride with chlorine",null,"Cadmium and its compounds (100 - <200 mg/l CaCO3)"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Hydrometallurgical operation involving dissolving/leaching with nitric acid",null,"Cadmium and its compounds (40 - < 50 mg/l CaCO3)"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Thermal treatment of contaminated secondary raw materials (e.g. swarf) and from the melting furnace",null,"Cadmium and its compounds (50 - <100 mg/l CaCO3)"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pyrolytic treatment of copper turnings, smelting, melting, fire refining and converting operations in secondary copper production",null,"Chromium III (95%ile) (dissolved)"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Furnace producing ferro-alloys",null,"Cobalt (dissolved)"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Smelting of raw materials",null,"Silver (dissolved)"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Drying operation where the raw materials contain organic compounds, halogens or other PCDD/F precursors, from an incineration operation, and from a calcining operation",null,"Vanadium (0 - 200 mg/l CaCO3)"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Primary copper production ",null,"Ammonia (human health receptor)"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Secondary copper production ",null,"Chromium, chromium (II) compounds and chromium (III) compounds as Cr"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Melting and smelting operation for the production of Doré metal, including the associated incineration, calcining and drying operations"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Baking plant with in an anode production plant with a primary aluminium smelter "]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Impregnation stage where special impregnation agents such as resins and biodegradable solvents are used"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pyrolytic treatment of copper turnings, and the drying, smelting and melting of secondary raw materials"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Raw material drying and smelting process"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Lime kilns"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Recovery boiler"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"TRS burner for strong odorous gases "]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Direct waste water discharge"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Pulp mill"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Non-integrated speciality paper mill "]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Sulphite pulp mill"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Mechanical pulps prdouced on site "]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"CTMP or CMP pulp mill"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"All units equipped with SCR or SNCR"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Loading and unloading operations of volatile liquid hydrocarbon compounds"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Combustion unit"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Regenerator in the catalytic cracking process- Partical combustion"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Unit for calcining of green coke"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Regenerator in the catalytic cracking process"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Multi-fuel fired combustion unit  with the exception\nof gas turbines"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Gas-fired combustion unit, with the exception of gas turbines"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Gas turbine"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Gas turbine- Existing"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Regenerator in the catalytic cracking process-all combustion mode "]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Regenerator in the catalytic cracking process- full combustion mode"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Regenerator in the catalytic cracking process- partial combustion mode "]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Regenerator in the catalytic cracking process- full combustion"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Regenerator in the catalytic cracking process- partial combustion"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Multi-fuel fired combustion units, with the exception of gas turbines and stationary gas engines"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Whole refinery "]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Indirect discharges of waste water from tanneries into urban waste water treatment plants "]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Dryer- all types "]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Dryer- Directly heated"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Dryer-Indirectly heated "]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Press"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Upstream and downstream wood processing, conveying of wood materials and mat forming "]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Drying oven"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"All plant"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Surface run-off "]