natgillin/translations-raw huggingface dataset:
< 1-7
The higher end of the BAT-AEL range for the yearly average for new plants operated < 1500 h/yr is 15 mg/Nm3.
28-38
These BAT-AEELs do not apply to units operated < 1500 h/yr.
73-99
For industrial boilers and district heating plants put into operation no later than 27 November 2003, which are operated < 1500 h/yr and for which SCR and/or SNCR is not applicable, the higher end of the BAT-AEL range is 450 mg/Nm3.
BAT 24 For at forebygge eller reducere NOX-emissionerne til luft og samtidig begrænse CO- og N2O-emissionerne til luft fra forbrændingen af fast biomasse og/eller tørv er det BAT at anvende én eller en kombination af nedenstående teknikker.
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.
BAT 25 For at forebygge eller reducere emissionerne af SOX-, HCl- og HF til luft fra forbrændingen af fast biomasse og/eller tørv er det BAT at anvende én eller en kombination af nedenstående teknikker.
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.
BAT 26 For at reducere emissioner af støv og partikelbundet metal til luft fra forbrændingen af fast biomasse og/eller tørv er det BAT at anvende én eller en kombination af nedenstående teknikker.
For industrial boilers and district heating plants of > 100 MWth put into operation no later than 27 November 2003, which are operated < 1500 h/yr and for which SCR and/or SNCR is not applicable, the higher end of the BAT-AEL range is 365 mg/Nm3.
2-15
For industrial boilers and district heating plants put into operation no later than 27 November 2003 and operated < 1500 h/yr, the higher end of the BAT-AEL range is 400 mg/Nm3.
2-10
The higher end of the BAT-AEL range is 175 mg/Nm3 for plants put into operation no later than 7 January 2014.
2-22
For industrial boilers and district heating plants put into operation no later than 27 November 2003, which are operated < 1500 h/yr and for which wet FGD is not applicable, the higher end of the BAT-AEL range is 200 mg/Nm3.
2-12
The higher end of the BAT-AEL range is 25 mg/Nm3 for plants put into operation no later than 7 January 2014.
2-16
The higher end of the BAT-AEL range is 15 mg/Nm3 for plants put into operation no later than 7 January 2014.
BAT 27 For at forebygge eller reducere kviksølvemissionerne til luft fra forbrændingen af fast biomasse og/eller tørv er det BAT at anvende én eller en kombination af nedenstående teknikker.
As defined in point 26 of Article 2 of Directive 2009/72/EC.
35,6-37,4
As defined in point 27 of Article 2 of Directive 2009/72/EC.
80-96
Net electrical efficiency BAT-AEELs apply to CHP units whose design is oriented towards power generation, and to units generating only power.
BAT 28 For at forebygge eller reducere NOX-emissionerne til luft og samtidig begrænse CO-emissionerne til luft fra forbrændingen af HFO og/eller gasolie i kedler er det BAT at anvende én eller en kombination af nedenstående teknikker.
These levels may be difficult to achieve in the case of engines fitted with energy-intensive secondary abatement techniques.
75-200
This level may be difficult to achieve in the case of engines using a radiator as a cooling system in dry, hot geographical locations.
150-270
These BAT-AELs do not apply to plants operated < 1500 h/yr or to plants that cannot be fitted with secondary abatement techniques.
100-215
The BAT-AEL range is 1150–1900 mg/Nm3 for plants operated < 1500 h/yr and for plants that cannot be fitted with secondary abatement techniques.
210-330 [105]
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.
45-75
These BAT-AELs do not apply to plants operated < 1500 h/yr.
45-100 [106]
The higher end of the BAT-AEL range is 280 mg/Nm3 if no secondary abatement technique can be applied.
85-100
This corresponds to a sulphur content of the fuel of 0,5 wt-% (dry).
85-110 [107] [108]
These BAT-AELs do not apply to existing plants operated < 1500 h/yr.
BAT 29 For at forebygge eller reducere SOX-, HCl- og HF-emissionerne til luft fra forbrændingen af HFO og/eller gasolie i kedler er det BAT at anvende én eller en kombination af nedenstående teknikker.
For existing plants operated < 500 h/yr, these levels are indicative.
50-175
In the case of CHP units, only one of the two BAT-AEELs ‘Net electrical efficiency’ or ‘Net total fuel utilisation’ applies, depending on the CHP unit design (i.e. either more oriented towards electricity generation or heat generation).
150-200 [111]
Net total fuel utilisation BAT-AEELs may not be achievable if the potential heat demand is too low.
35-50
These BAT-AEELs apply to units used for mechanical drive applications.
50-110
These levels may be difficult to achieve in the case of engines tuned in order to reach NOX levels lower than 190 mg/Nm3.
50-120
These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines.
150-165 [112] [113]
In the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective.
BAT 30 For at reducere emissioner af støv og partikelbundet metal til luft fra forbrændingen af HFO og/eller gasolie i kedler er det BAT at anvende én eller en kombination af nedenstående teknikker.
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.
2-20
These BAT-AELs do not apply to existing turbines for mechanical drive applications or to plants operated < 500 h/yr.
7-18
For 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.
7-22 [116]
The 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 1500 h/yr.
7-10
For 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.
41,5-44,5 [122]
For existing plants put into operation no later than 7 January 2014, the higher end of the BAT-AEL range is 55 mg/Nm3.
38,3-44,5 [122]
For existing plants put into operation no later than 7 January 2014, the higher end of the BAT-AEL range is 80 mg/Nm3.
BAT 32 For at forebygge eller reducere NOX-emissionerne til luft fra forbrændingen af HFO og/eller gasolie i stempelmotorer er det BAT at anvende én eller en kombination af nedenstående teknikker.
The lower end of the BAT-AEL range for NOX can be achieved with DLN burners.
BAT 33 For at forebygge eller reducere emissionerne af CO og flygtige organiske forbindelser til luft fra forbrændingen af HFO og/eller gasolie i stempelmotorer er det BAT at anvende en eller begge nedenstående teknikker.
These levels are indicative.
115-190 [127]
For existing plants put into operation no later than 7 January 2014, the higher end of the BAT-AEL range is 60 mg/Nm3.
125-625
These BAT-AELs only apply to spark-ignited and dual-fuel engines.
145-300
They do not apply to gas-diesel engines.
150-750
In 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.
BAT 34 For at forebygge eller reducere SOX-, HCl- og HF-emissionerne til luft fra forbrændingen af HFO og/eller gasolie i stempelmotorer er det BAT at anvende én eller en kombination af nedenstående teknikker.
For existing plants operated < 500 h/yr, these levels are indicative.
45-100
This BAT-AEL is expressed as C at full load operation.
100-200 [130]
The wide range of energy efficiencies in CHP units is largely dependent on the local demand for electricity and heat.
60-110
These BAT-AEELs do not apply in the case of units operated < 1500 h/yr.
105-235 [130]
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.
BAT 35 For at forebygge eller reducere emissioner af støv og partikelbundet metal fra forbrændingen af HFO og/eller gasolie i stempelmotorer er det BAT at anvende én eller en kombination af nedenstående teknikker.
The lower end of the BAT-AEL range can be achieved when using SCR.
5-10
For plants operated < 1500 h/yr, these BAT AELs do not apply.
5-35
In 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.
10-20
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.
BAT 36 Den bedste tilgængelige teknik til at gøre forbrændingen af gasolie i gasturbiner mere effektiv er at anvende en passende kombination af teknikkerne angivet i BAT 12 og nedenfor.
In this case, the higher end of the BAT-AEL range is 220 mg/Nm3.
25-35,7
In 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.
33-44
For existing plants operated < 1500 h/yr, these BAT AELs do not apply.
BAT 37 For at forebygge eller reducere NOX-emissionerne til luft fra forbrændingen af gasolie i gasturbiner er det BAT at anvende én eller en kombination af nedenstående teknikker.
The higher end of the BAT-AEL range may be exceeded when using a high share of COG (e.g. > 50 %).
BAT 38 For at forebygge eller reducere CO-emissionerne til luft fra forbrændingen af gasolie i gasturbiner er det BAT at anvende én eller en kombination af nedenstående teknikker.
In this case, the higher end of the BAT-AEL range is 300 mg/Nm3.
BAT 39 For at forebygge eller reducere emissionerne af SOX og støv til luft fra forbrændingen af gasolie i gasturbiner er det BAT at anvende nedenstående teknik.
For existing plants operated < 1500 h/yr, these BAT-AELs do not apply.
35-60
For existing plants operated < 500 h/yr, these levels are indicative
50-66
These BAT-AELs are based on > 70 % of baseload power available on the day.
BAT 40 BAT for øget energieffektivitet af forbrændingen af naturgas er at anvende en passende kombination af teknikkerne angivet i BAT 12 og nedenfor.
This includes single fuel and dual fuel gas turbines.
39,5-44 [142]
The higher end of the BAT-AEL range is 250 mg/Nm3 if DLN burners are not applicable.
35-44 [142]
The lower end of the BAT-AEL range can be achieved with DLN burners.
56-85 [142]
In the case of CHP units, only one of the two BAT-AEELs ‘Net electrical efficiency’ or ‘Net total fuel utilisation’ applies, depending on the CHP unit design (i.e. either more oriented towards generation electricity or towards heat generation).
39-42,5
These BAT-AEELs may not be achievable if the potential heat demand is too low.
38-40
For 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.
78-95
For existing plants put into operation no later than 7 January 2014, the higher end of the BAT-AEL range is 180 mg/Nm3.
36-41,5
For existing plants put into operation no later than 7 January 2014, the higher end of the BAT-AEL range is 210 mg/Nm3.
33-41,5
In the case of plants operated < 1500 h/yr, the higher end of the BAT-AEL range is 20 mg/Nm3.
36,5-41
In the case of plants operated < 1500 h/yr, the higher end of the BAT-AEL range is 7 mg/Nm3.
33,5-41
For plants operated < 1500 h/yr, these BAT-AELs do not apply.
53-58,5
For plants put into operation no later than 7 January 2014, the higher end of the BAT-AEL range is 25 mg/Nm3.
46-54
For plants put into operation no later than 7 January 2014, the higher end of the BAT-AEL range is 15 mg/Nm3.
BAT 41 For at forebygge eller reducere NOX-emissionerne til luft fra forbrændingen af naturgas i kedler er det BAT at anvende én eller en kombination af nedenstående teknikker.
Monitoring of Emissions to Air and Water from IED installations (ROM)
BAT 42 For at forebygge eller reducere NOX-emissionerne til luft fra forbrændingen af naturgas i gasturbiner er det BAT at anvende én eller en kombination af nedenstående teknikker.
Production of Pulp, Paper and Board (PP)
BAT 43 For at forebygge eller reducere NOX-emissionerne til luft fra forbrændingen af naturgas i motorer er det BAT at anvende én eller en kombination af nedenstående teknikker.
A CCGT is a combustion plant where two thermodynamic cycles are used (i.e. Brayton and Rankine cycles).
BAT 44 For at forebygge eller reducere CO-emissionerne til luft fra forbrændingen af naturgas er det BAT at sikre optimeret forbrænding og/eller at bruge oxidationskatalysatorer.
In a CCGT, heat from the flue-gas of a gas turbine (operating according to the Brayton cycle to produce electricity) is converted to useful energy in a heat recovery steam generator (HRSG), where it is used to generate steam, which then expands in a steam turbine (operating according to the Rankine cycle to produce additional electricity).
15-35
Chemical oxygen demand.
25-50
Amount of oxygen needed for the total oxidation of the organic matter to carbon dioxide
15-50
Polychlorinated dibenzo-p-dioxins and -furans RCG
25-55 [149]
Recovery of heat (mainly from the steam system) for producing hot water/steam to be used in industrial processes/activities or in a public network for district heating.
10-30
Additional heat recovery is possible from:
15-40
Net electrical efficiency (%) [39]
10-40
100–150
18-50
100–270
10-50
155–200
50-600
50–100
35-55
100–180
25-50 [152]
80–130
35-55 [153]
155–210
60-140 [154] [155]
< 30–140
15-50 [156]
< 30–100 [55]
25-55 [157]
< 5–100 [55]
10-60
2–8
30-85
BAT conclusions for the combustion of solid biomass and/or peat Unless otherwise stated, the BAT conclusions presented in this section are generally applicable to the combustion of solid biomass and/or peat.
85-110
Net electrical efficiency (%) [76]
20-100
70–150 [82]
55-85
70–225 [83]
55-110 [162]
120–200 [84]
BAT 45 For at reducere emissionerne af ikke-methan, flygtige, organiske forbindelser end metan (NMVOC) og metan (CH4) til luft fra forbrændingen af naturgas i gnisttændte lean burn-gasmotorer er det BAT at sikre optimeret forbrænding og/eller at bruge oxidationskatalysatorer.
120–275 [85]
5-15 [163]
100–300
215-500 [164]
50–140
215-560 [163] [164]
50–180
BAT 46 Den bedste tilgængelige teknik til at gøre forbrændingen af procesgasser fra jern- og stålproduktion mere effektiv er at anvende en passende kombination af teknikkerne angivet i BAT 12 og nedenfor.
100–200
30-40
100–220
50-84
40–140
36-42,5
40–150 [86]
40-48
65–150
60-82
95–165 [87]
BAT 47 For at forebygge eller reducere NOX-emissionerne til luft fra forbrændingen af procesgasser fra jern- og stålproduktion i kedler er det BAT at anvende én eller en kombination af nedenstående teknikker.
15–70
BAT 48 For at forebygge eller reducere NOX-emissionerne til luft fra forbrændingen af procesgasser fra jern- og stålproduktion i kedler er det BAT at anvende én eller en kombination af nedenstående teknikker.
15–100
BAT 49 For at forebygge eller reducere CO-emissionerne til luft fra forbrændingen af procesgasser fra jern- og stålproduktion er det BAT at anvende én eller en kombination af nedenstående teknikker.
30–175
15-65
30–215
22-100
< 10–50
22-110 [173] [175] [176]
< 20–85
20-35
< 20–175 [91]
30-50
< 10–35
20-50 [173] [174]
< 10–50 [90]
30-55 [176] [177]
< 20–70
BAT 50 For at forebygge eller reducere SOX-emissionerne til luft fra forbrændingen af procesgasser fra jern- og stålproduktion er det BAT at anvende en kombination af nedenstående teknikker.
< 20–85 [92]
BAT 51 For at reducere støvemissionerne til luft fra forbrændingen af procesgasser fra jern- og stålproduktion er det BAT at anvende én eller en kombination af nedenstående teknikker.
Net electrical efficiency (%) [121]
BAT 52 For at forbedre de overordnede miljøpræstationer i forbindelse med forbrændingen af gasformigt og/eller flydende brændsel på offshoreplatforme er det BAT at anvende én eller en kombination af nedenstående teknikker.
They do not apply to combustion plants on offshore platforms; these are covered by Section.
BAT 53 For at forebygge eller reducere NOX-emissionerne til luft fra forbrændingen af gasformigt og/eller flydende brændsel på offshoreplatforme er det BAT at anvende én eller en kombination af nedenstående teknikker.
Existing OCGT of ≥ 50 MWth (excluding turbines for mechanical drive applications): < 5–40 mg/Nm3.
BAT 54 For at forebygge eller reducere CO-emissionerne til luft fra forbrændingen af gasformigt og/eller flydende brændsel i gasturbiner på offshoreplatforme er det BAT at anvende én eller en kombination af nedenstående teknikker.
The higher end of this range will generally be 80 mg/Nm3 in the case of existing plants that cannot be fitted with dry techniques for NOX reduction, or 50 mg/Nm3 for plants that operate at low load.
15-50 [185]
25–150
< 50-350 [186]
50–200 [180]
BAT 55 For at forbedre de overordnede miljøpræstationer i forbindelse med forbrændingen af procesbrændsel fra kemikalieindustrien i kedler er det BAT at anvende en passende kombination af teknikkerne angivet i BAT 6 og nedenfor.
10–45
BAT 56 For at forebygge eller reducere NOX-emissionerne til luft og samtidig begrænse CO-emissionerne til luft fra forbrændingen af procesbrændsel fra kemikalieindustrien er det BAT at anvende én eller en kombination af nedenstående teknikker.
20–70
80-290 [193]
Sb + As + Pb + Cr + Co + Cu + Mn + Ni + V (mg/Nm3)
100-330 [193]
For circulating fluidised bed boilers, the lower end of the range can be achieved by using high-efficiency wet FGD.
20-80
The higher end of the range can be achieved by using boiler in-bed sorbent injection.
70-100 [194]
These BAT-AELs only apply to spark-ignited and dual-fuel engines.
30-100
They do not apply to gas-diesel engines.
85-110 [195]
Common Waste Water and Waste Gas Treatment/Management Systems in the Chemical Sector (CWW)
10-110
Chemical BREF series (LVOC, etc.)
90-200
BAT 1.
2-15 [199]
In order to improve the overall environmental performance, BAT is to implement and adhere to an environmental management system (EMS) that incorporates all of the following features:
< 1-6 [200]
BAT 2.
1-9 [199]
BAT is to determine the net electrical efficiency and/or the net total fuel utilisation and/or the net mechanical energy efficiency of the gasification, IGCC and/or combustion units by carrying out a performance test at full load [3], according to EN standards, after the commissioning of the unit and after each modification that could significantly affect the net electrical efficiency and/or the net total fuel utilisation and/or the net mechanical energy efficiency of the unit.
< 1-3 [200]
BAT 3.
BAT 58 For at reducere emissioner af støv og partikelbundet metal til luft og spore stoffer fra forbrændingen af procesbrændsel fra kemikalieindustrien i kedler er det BAT at anvende én eller en kombination af nedenstående teknikker.
BAT is to monitor key process parameters relevant for emissions to air and water including those given below.
2-22 [203]
BAT 4.
2-10 [204]
BAT is to monitor emissions to air with at least the frequency given below and in accordance with EN standards.
2-11 [203]
BAT 5.
BAT 59 For at reducere emissionerne til luft af flygtige organiske forbindelser og polychlorerede dibenzodioxiner/furaner fra forbrændingen af procesbrændsel fra kemikalieindustrien i kedler er det BAT at anvende én eller en kombination af teknikkerne angivet i BAT 6 og nedenfor.
BAT is to monitor emissions to water from flue-gas treatment with at least the frequency given below and in accordance with EN standards.
< 0,012-0,036
BAT 6.
0,6-12
In order to improve the general environmental performance of combustion plants and to reduce emissions to air of CO and unburnt substances, BAT is to ensure optimised combustion and to use an appropriate combination of the techniques given below.
BAT 60 For at forbedre de overordnede miljøpræstationer i forbindelse med affaldsmedforbrænding i fyringsanlæg, sikre stabile forbrændingsvilkår og reducere emissionerne til luft er det BAT at anvende teknik BAT 60, litra a, nedenfor og en kombination af teknikkerne anført i BAT 6 og/eller de andre nedenstående teknikker.
BAT 7.
BAT 61 For at forebygge øgede emissioner fra affaldsmedforbrænding i fyringsanlæg er det BAT at træffe passende foranstaltninger for at sikre, at emissionerne af forurenende stoffer i den del af røggasserne, der opstår ved affaldsmedforbrændingen, ikke er højere end de emissioner, der opstår ved anvendelse af BAT-konklusionerne for affaldsforbrænding.
In order to reduce emissions of ammonia to air from the use of selective catalytic reduction (SCR) and/or selective non-catalytic reduction (SNCR) for the abatement of NOX emissions, BAT is to optimise the design and/or operation of SCR and/or SNCR (e.g. optimised reagent to NOX ratio, homogeneous reagent distribution and optimum size of the reagent drops).
BAT 62 For at minimere indvirkningen af genanvendelsen af reststoffer fra affaldsmedforbrænding i fyringsanlæg er det BAT at opretholde en god kvalitet af gips, aske og slagge samt andre reststoffer i overensstemmelse med kravene for genanvendelse heraf, når anlægget ikke medforbrænder affald, ved at anvende en af de i BAT 60 angivne teknikker eller en kombination af disse og/eller ved at begrænse medforbrændingen til affaldsfraktioner med koncentrationer af forurenende stoffer, der svarer til koncentrationerne i andre forbrændte brændsler.
BAT 8.
BAT 63 Til at gøre affaldsmedforbrændingen mere effektiv er det BAT at anvende en passende kombination af teknikkerne angivet i BAT 12 og BAT 19, afhængigt af den anvendte primære brændselstype i anlægskonfigurationen.
In order to prevent or reduce emissions to air during normal operating conditions, BAT is to ensure, by appropriate design, operation and maintenance, that the emission abatement systems are used at optimal capacity and availability.
BAT 64 For at forebygge eller reducere NOX-emissionerne til luft og samtidig begrænse CO- og N2O-emissionerne fra affaldsmedforbrænding med kul og/eller brunkul er det BAT at anvende én eller en kombination af teknikkerne i BAT 20.
BAT 9.
BAT 65 For at forebygge eller reducere NOX-emissionerne til luft og samtidig begrænse CO- og N2O-emissionerne fra affaldsmedforbrænding med biomasse og/eller tørv er det BAT at anvende én eller en kombination af nedenstående teknikker BAT 24.
In order to improve the general environmental performance of combustion and/or gasification plants and to reduce emissions to air, BAT is to include the following elements in the quality assurance/quality control programmes for all the fuels used, as part of the environmental management system (see BAT 1):
BAT 66 For at forebygge eller reducere SOX-, HCl- og HF-emissionerne til luft fra affaldsmedforbrændingen med kul og/eller brunkul er det BAT at anvende én eller en kombination af teknikkerne angivet i BAT 21.
BAT 10.
BAT 67 For at forebygge eller reducere SOX-, HCl- og HF-emissionerne til luft fra affaldsmedforbrændingen med biomasse og/eller tørv er det BAT at anvende én eller en kombination af teknikkerne angivet i BAT 25.
In order to reduce emissions to air and/or to water during other than normal operating conditions (OTNOC), BAT is to set up and implement a management plan as part of the environmental management system (see BAT 1), commensurate with the relevance of potential pollutant releases, that includes the following elements:
BAT 68 For at reducere emissioner af støv og partikelbundet metal til luft fra affaldsmedforbrændingen med kul og/eller brunkul er det BAT at anvende én eller en kombination af teknikkerne angivet i BAT 22.
BAT 11.
Cd+Tl (μg/Nm3)
BAT is to appropriately monitor emissions to air and/or to water during OTNOC.
0,005-0,5
BAT 12.