(1) | the entries for Annex II and Annexes IV to XII are replaced by the following:‘Annex II:Guidelines for combustion emissions from activities as listed in Annex I to Directive 2003/87/EC carried out in installationsAnnex IV:Activity-specific guidelines for the production of coke as listed in Annex I to Directive 2003/87/ECAnnex V:Activity-specific guidelines for metal ore roasting and sintering as listed in Annex I to Directive 2003/87/ECAnnex VI:Activity-specific guidelines for the production of pig iron and steel including continuous casting as listed in Annex I to Directive 2003/87/ECAnnex VII:Activity-specific guidelines for the production of cement clinker as listed in Annex I to Directive 2003/87/ECAnnex VIII:Activity-specific guidelines for the production of lime or calcination of dolomite or magnesite as listed in Annex I to Directive 2003/87/ECAnnex IX:Activity-specific guidelines for the manufacture of glass or mineral wool insulation material as listed in Annex I to Directive 2003/87/ECAnnex X:Activity-specific guidelines for the manufacture of ceramic products as listed in Annex I to Directive 2003/87/ECAnnex XI:Activity-specific guidelines for pulp and paper production as listed in Annex I to Directive 2003/87/ECAnnex XII:Guidelines for determination of emissions or amount of transfer of greenhouse gases by continuous measurement systems’; | ‘Annex II | : | Guidelines for combustion emissions from activities as listed in Annex I to Directive 2003/87/EC carried out in installations | Annex IV | : | Activity-specific guidelines for the production of coke as listed in Annex I to Directive 2003/87/EC | Annex V | : | Activity-specific guidelines for metal ore roasting and sintering as listed in Annex I to Directive 2003/87/EC | Annex VI | : | Activity-specific guidelines for the production of pig iron and steel including continuous casting as listed in Annex I to Directive 2003/87/EC | Annex VII | : | Activity-specific guidelines for the production of cement clinker as listed in Annex I to Directive 2003/87/EC | Annex VIII | : | Activity-specific guidelines for the production of lime or calcination of dolomite or magnesite as listed in Annex I to Directive 2003/87/EC | Annex IX | : | Activity-specific guidelines for the manufacture of glass or mineral wool insulation material as listed in Annex I to Directive 2003/87/EC | Annex X | : | Activity-specific guidelines for the manufacture of ceramic products as listed in Annex I to Directive 2003/87/EC | Annex XI | : | Activity-specific guidelines for pulp and paper production as listed in Annex I to Directive 2003/87/EC | Annex XII | : | Guidelines for determination of emissions or amount of transfer of greenhouse gases by continuous measurement systems’;
‘Annex II | : | Guidelines for combustion emissions from activities as listed in Annex I to Directive 2003/87/EC carried out in installations
Annex IV | : | Activity-specific guidelines for the production of coke as listed in Annex I to Directive 2003/87/EC
Annex V | : | Activity-specific guidelines for metal ore roasting and sintering as listed in Annex I to Directive 2003/87/EC
Annex VI | : | Activity-specific guidelines for the production of pig iron and steel including continuous casting as listed in Annex I to Directive 2003/87/EC
Annex VII | : | Activity-specific guidelines for the production of cement clinker as listed in Annex I to Directive 2003/87/EC
Annex VIII | : | Activity-specific guidelines for the production of lime or calcination of dolomite or magnesite as listed in Annex I to Directive 2003/87/EC
Annex IX | : | Activity-specific guidelines for the manufacture of glass or mineral wool insulation material as listed in Annex I to Directive 2003/87/EC
Annex X | : | Activity-specific guidelines for the manufacture of ceramic products as listed in Annex I to Directive 2003/87/EC
Annex XI | : | Activity-specific guidelines for pulp and paper production as listed in Annex I to Directive 2003/87/EC
Annex XII | : | Guidelines for determination of emissions or amount of transfer of greenhouse gases by continuous measurement systems’;
(2) | the following titles of new Annexes XIX, XX, XXI, XXII, XXIII and XXIV are added:‘Annex XIX:Activity-specific guidelines for the production of soda ash and sodium bicarbonate as listed in Annex I to Directive 2003/87/ECAnnex XX:Activity-specific guidelines for the production of ammonia as listed in Annex I to Directive 2003/87/ECAnnex XXI:Activity-specific guidelines for the production of hydrogen and synthesis gas as listed in Annex I to Directive 2003/87/ECAnnex XXII:Activity-specific guidelines for the production of bulk organic chemicals as listed in Annex I to Directive 2003/87/ECAnnex XXIII:Activity-specific guidelines for the production or processing of ferrous and non-ferrous metals as listed in Annex I to Directive 2003/87/ECAnnex XXIV:Activity-specific guidelines for the production or processing of primary aluminium as listed in Annex I to Directive 2003/87/EC’. | ‘Annex XIX | : | Activity-specific guidelines for the production of soda ash and sodium bicarbonate as listed in Annex I to Directive 2003/87/EC | Annex XX | : | Activity-specific guidelines for the production of ammonia as listed in Annex I to Directive 2003/87/EC | Annex XXI | : | Activity-specific guidelines for the production of hydrogen and synthesis gas as listed in Annex I to Directive 2003/87/EC | Annex XXII | : | Activity-specific guidelines for the production of bulk organic chemicals as listed in Annex I to Directive 2003/87/EC | Annex XXIII | : | Activity-specific guidelines for the production or processing of ferrous and non-ferrous metals as listed in Annex I to Directive 2003/87/EC | Annex XXIV | : | Activity-specific guidelines for the production or processing of primary aluminium as listed in Annex I to Directive 2003/87/EC’.
‘Annex XIX | : | Activity-specific guidelines for the production of soda ash and sodium bicarbonate as listed in Annex I to Directive 2003/87/EC
Annex XX | : | Activity-specific guidelines for the production of ammonia as listed in Annex I to Directive 2003/87/EC
Annex XXI | : | Activity-specific guidelines for the production of hydrogen and synthesis gas as listed in Annex I to Directive 2003/87/EC
Annex XXII | : | Activity-specific guidelines for the production of bulk organic chemicals as listed in Annex I to Directive 2003/87/EC
Annex XXIII | : | Activity-specific guidelines for the production or processing of ferrous and non-ferrous metals as listed in Annex I to Directive 2003/87/EC
Annex XXIV | : | Activity-specific guidelines for the production or processing of primary aluminium as listed in Annex I to Directive 2003/87/EC’.

(1) | in Section 1 entitled ‘Introduction’, the words ‘Annexes II to XI and Annexes XIII to XVIII’ are replaced by the words ‘Annexes II to XI and Annexes XIII to XXIV’;
(2) | in the introductory part of Section 2 entitled ‘Definitions’ the words ‘Annexes II to XVIII’ are replaced by the words ‘Annexes II to XXIV’;
(3) | Section 4.3 entitled ‘The Monitoring Plan’ is amended as follows:(a)in the fourth paragraph, point (e) is replaced as follows:‘(e)a list and description of the tiers for activity data, carbon content (where mass balance or other approaches directly requiring the carbon content for emission calculation are applied), emission factors, oxidation and conversion factors for each of the source streams to be monitored’;(b)the following subparagraphs are added after subparagraph (t):‘(u)where applicable, the dates when measurements for the determination of the installation specific emission factors for CF4and C2F6have been carried out, and a schedule for future repetitions of this determination;(v)where applicable, the protocol describing the procedure used to determine the installation specific emission factors for CF4and C2F6, showing also that the measurements have been and will be carried out for a sufficiently long time for measured values to converge, but at least for 72 hours;(w)where applicable, the methodology for determining the collection efficiency for fugitive emissions at installations for primary aluminium production;’; | (a) | in the fourth paragraph, point (e) is replaced as follows:‘(e)a list and description of the tiers for activity data, carbon content (where mass balance or other approaches directly requiring the carbon content for emission calculation are applied), emission factors, oxidation and conversion factors for each of the source streams to be monitored’; | ‘(e) | a list and description of the tiers for activity data, carbon content (where mass balance or other approaches directly requiring the carbon content for emission calculation are applied), emission factors, oxidation and conversion factors for each of the source streams to be monitored’; | (b) | the following subparagraphs are added after subparagraph (t):‘(u)where applicable, the dates when measurements for the determination of the installation specific emission factors for CF4and C2F6have been carried out, and a schedule for future repetitions of this determination;(v)where applicable, the protocol describing the procedure used to determine the installation specific emission factors for CF4and C2F6, showing also that the measurements have been and will be carried out for a sufficiently long time for measured values to converge, but at least for 72 hours;(w)where applicable, the methodology for determining the collection efficiency for fugitive emissions at installations for primary aluminium production;’; | ‘(u) | where applicable, the dates when measurements for the determination of the installation specific emission factors for CF4and C2F6have been carried out, and a schedule for future repetitions of this determination; | (v) | where applicable, the protocol describing the procedure used to determine the installation specific emission factors for CF4and C2F6, showing also that the measurements have been and will be carried out for a sufficiently long time for measured values to converge, but at least for 72 hours; | (w) | where applicable, the methodology for determining the collection efficiency for fugitive emissions at installations for primary aluminium production;’;
(a) | in the fourth paragraph, point (e) is replaced as follows:‘(e)a list and description of the tiers for activity data, carbon content (where mass balance or other approaches directly requiring the carbon content for emission calculation are applied), emission factors, oxidation and conversion factors for each of the source streams to be monitored’; | ‘(e) | a list and description of the tiers for activity data, carbon content (where mass balance or other approaches directly requiring the carbon content for emission calculation are applied), emission factors, oxidation and conversion factors for each of the source streams to be monitored’;
‘(e) | a list and description of the tiers for activity data, carbon content (where mass balance or other approaches directly requiring the carbon content for emission calculation are applied), emission factors, oxidation and conversion factors for each of the source streams to be monitored’;
(b) | the following subparagraphs are added after subparagraph (t):‘(u)where applicable, the dates when measurements for the determination of the installation specific emission factors for CF4and C2F6have been carried out, and a schedule for future repetitions of this determination;(v)where applicable, the protocol describing the procedure used to determine the installation specific emission factors for CF4and C2F6, showing also that the measurements have been and will be carried out for a sufficiently long time for measured values to converge, but at least for 72 hours;(w)where applicable, the methodology for determining the collection efficiency for fugitive emissions at installations for primary aluminium production;’; | ‘(u) | where applicable, the dates when measurements for the determination of the installation specific emission factors for CF4and C2F6have been carried out, and a schedule for future repetitions of this determination; | (v) | where applicable, the protocol describing the procedure used to determine the installation specific emission factors for CF4and C2F6, showing also that the measurements have been and will be carried out for a sufficiently long time for measured values to converge, but at least for 72 hours; | (w) | where applicable, the methodology for determining the collection efficiency for fugitive emissions at installations for primary aluminium production;’;
‘(u) | where applicable, the dates when measurements for the determination of the installation specific emission factors for CF4and C2F6have been carried out, and a schedule for future repetitions of this determination;
(v) | where applicable, the protocol describing the procedure used to determine the installation specific emission factors for CF4and C2F6, showing also that the measurements have been and will be carried out for a sufficiently long time for measured values to converge, but at least for 72 hours;
(w) | where applicable, the methodology for determining the collection efficiency for fugitive emissions at installations for primary aluminium production;’;
(4) | Section 5 is amended as follows:(a)in Section 5.1, under the heading ‘process emissions’, the second paragraph is replaced by the following:‘The calculation of process emissions is further specified in the activity-specific guidelines in the Annexes II to XI and XVI to XXIV. Not all calculation methods in Annexes II to XI and XVI to XXIV use a conversion factor.’;(b)in Section 5.2 entitled ‘Tiers of Approaches’, the words ‘Annexes II to XI and Annexes XIV to XVIII’ are replaced by the words ‘Annexes II to XI and XIV to XXIV’;(c)in Section 5.2, the following ninth paragraph is added:‘For commercial standard fuels minimum tier approaches as stated in Table 1 for Annex II on combustion activities can be applied also for other activities.’;(d)‘Table 1: Minimum Requirements’ is replaced by the following table:‘Table 1Minimum requirements(‘n.a.’ means ‘not applicable’)Column A for ‘category A installations’ (means installations with average reported annual emissions over the previous trading period (or a conservative estimate or projection if reported emissions are not available or no longer applicable) equal to or less than 50 kilotonnes of CO2-eqnot including biogenic CO2and before subtraction of transferred CO2),Column B for ‘category B installations’ (means installations with average reported annual emissions over the previous trading period (or a conservative estimate or projection if reported emissions are not available or no longer applicable) of greater than 50 kilotonnes and equal to or less than 500 kilotonnes of CO2-eqnot including biogenic CO2and before subtraction of transferred CO2),and Column C for ‘category C installations’ (means installations with average reported annual emissions over the previous trading period (or a conservative estimate or projection if reported emissions are not available or no longer applicable) of greater than 500 kilotonnes of CO2-eqnot including biogenic CO2and before subtraction of transferred CO2).Activity DataEmission FactorComposition DataOxidation FactorConversion FactorFuel FlowNet Calorific ValueAnnex/ActivityABCABCABCABCABCABCII:CombustionCommercial standard fuels2342a/2b2a/2b2a/2b2a/2b2a/2b2a/2bn.a.n.a.n.a.111n.a.n.a.n.a.Other gaseous & liquid fuels2342a/2b2a/2b32a/2b2a/2b3n.a.n.a.n.a.111n.a.n.a.n.a.Solid fuels1232a/2b332a/2b33n.a.n.a.n.a.111n.a.n.a.n.a.Mass Balance Approach for Carbon Black Production and Gas Processing Terminals123n.a.n.a.n.a.n.a.n.a.n.a.122n.a.n.a.n.a.n.a.n.a.n.a.Flares123n.a.n.a.n.a.12a/b3n.a.n.a.n.a.111n.a.n.a.n.a.ScrubbingCarbonate111n.a.n.a.n.a.111n.a.n.a.n.a.n.a.n.a.n.a.n.a.n.a.n.a.Gypsum111n.a.n.a.n.a.111n.a.n.a.n.a.n.a.n.a.n.a.n.a.n.a.n.a.Activity DataEmission FactorComposition DataConversion FactorMaterial FlowNet Calorific ValueABCABCABCABCABCIII:RefineriesCatalytic Cracker Regeneration111n.a.n.a.n.a.n.a.n.a.n.a.n.a.n.a.n.a.n.a.n.a.n.a.Hydrogen Production122n.a.n.a.n.a.122n.a.n.a.n.a.n.a.n.a.n.a.IV:Coke OvensMass balance123n.a.n.a.n.a.n.a.n.a.n.a.233n.a.n.a.n.a.Fuel as process input123223233n.a.n.a.n.a.n.a.n.a.n.a.V:Metal Ore Roasting & SinteringMass balance123n.a.n.a.n.a.n.a.n.a.n.a.233n.a.n.a.n.a.Carbonate Input112n.a.n.a.n.a.111n.a.n.a.n.a.111VI:Iron & SteelMass balance123n.a.n.a.n.a.n.a.n.a.n.a.233n.a.n.a.n.a.Fuel as process input123223233n.a.n.a.n.a.n.a.n.a.n.a.VII:CementKiln Input Based123n.a.n.a.n.a.111n.a.n.a.n.a.112Clinker Output112n.a.n.a.n.a.123n.a.n.a.n.a.112CKD112n.a.n.a.n.a.122n.a.n.a.n.a.n.a.n.a.n.a.Non-Carbonate Carbon112n.a.n.a.n.a.112n.a.n.a.n.a.112VIII:Lime, Dolomite and MagnesiteCarbonates123n.a.n.a.n.a.111n.a.n.a.n.a.112Alkali Earth Oxide112n.a.n.a.n.a.111n.a.n.a.n.a.112IX:Glass, Mineral WoolCarbonates112n.a.n.a.n.a.111n.a.n.a.n.a.n.a.n.a.n.a.X:CeramicCarbon Inputs112n.a.n.a.n.a.123n.a.n.a.n.a.1.12Alkali Oxide112n.a.n.a.n.a.123n.a.n.a.n.a.112Scrubbing111n.a.n.a.n.a.111n.a.n.a.n.a.n.a.n.a.n.a.XI:Pulp & PaperStandard Method111n.a.n.a.n.a.111n.a.n.a.n.a.n.a.n.a.n.a.XIX:Soda ash and sodium bicarbonateMass balance123n.a.n.a.n.a.n.a.n.a.n.a.233n.a.n.a.n.a.XX:AmmoniaFuel as process input2342a/2b2a/2b32a/2b2a/2b3n.a.n.a.n.a.n.a.n.a.n.a.XXI:Hydrogen and synthesis gasFuel as process input2342a/2b2a/2b32a/2b2a/2b3n.a.n.a.n.a.n.a.n.a.n.a.Mass balance123n.a.n.a.n.a.n.a.n.a.n.a.233n.a.n.a.n.a.XXII:Bulk organic chemicalsMass balance123n.a.n.a.n.a.n.a.n.a.n.a.233n.a.n.a.n.a.XXIII:Metals production or processingMass balance123n.a.n.a.n.a.n.a.n.a.n.a.233n.a.n.a.n.a.Process emissions112n.a.n.a.n.a.111n.a.n.a.n.a.112XXIV:Aluminium productionMass balance for CO2emissions123n.a.n.a.n.a.n.a.n.a.n.a.233n.a.n.a.n.a.PFC emissions (slope method)112n.a.n.a.n.a.111n.a.n.a.n.a.n.a.n.a.n.a.PFC emissions (overvoltage method)112n.a.n.a.n.a.111n.a.n.a.n.a.n.a.n.a.n.a.’(e)in Section 5.4 entitled ‘Activity Data of Stationary Installations’, in the second subparagraph, the words ‘Annexes II to XI’ are replaced by the words ‘Annexes II to XXIV’;(f)in Section 5.5, entitled ‘Emissions Factors’, the first paragraph is replaced by the following:‘Emission factors for CO2emissions are based on the carbon content of fuels or input materials and expressed as tCO2/TJ (combustion emissions), or tCO2/t or tCO2/Nm3(process emissions). For non-CO2greenhouse gases, appropriate emission factors are defined in the relevant activity-specific Annexes to these Guidelines.’;(g)Section 5.7 is amended as follows:—the first indent of the first paragraph is replaced by the following:‘as pure substance, or directly used and bound in products or as feedstock, unless other requirements as set out in Annexes XIX to XXII apply, or’,—in the second paragraph, the words ‘or XVIII’ are replaced by ‘to XXII’; | (a) | in Section 5.1, under the heading ‘process emissions’, the second paragraph is replaced by the following:‘The calculation of process emissions is further specified in the activity-specific guidelines in the Annexes II to XI and XVI to XXIV. Not all calculation methods in Annexes II to XI and XVI to XXIV use a conversion factor.’; | (b) | in Section 5.2 entitled ‘Tiers of Approaches’, the words ‘Annexes II to XI and Annexes XIV to XVIII’ are replaced by the words ‘Annexes II to XI and XIV to XXIV’; | (c) | in Section 5.2, the following ninth paragraph is added:‘For commercial standard fuels minimum tier approaches as stated in Table 1 for Annex II on combustion activities can be applied also for other activities.’; | (d) | ‘Table 1: Minimum Requirements’ is replaced by the following table:‘Table 1Minimum requirements(‘n.a.’ means ‘not applicable’)Column A for ‘category A installations’ (means installations with average reported annual emissions over the previous trading period (or a conservative estimate or projection if reported emissions are not available or no longer applicable) equal to or less than 50 kilotonnes of CO2-eqnot including biogenic CO2and before subtraction of transferred CO2),Column B for ‘category B installations’ (means installations with average reported annual emissions over the previous trading period (or a conservative estimate or projection if reported emissions are not available or no longer applicable) of greater than 50 kilotonnes and equal to or less than 500 kilotonnes of CO2-eqnot including biogenic CO2and before subtraction of transferred CO2),and Column C for ‘category C installations’ (means installations with average reported annual emissions over the previous trading period (or a conservative estimate or projection if reported emissions are not available or no longer applicable) of greater than 500 kilotonnes of CO2-eqnot including biogenic CO2and before subtraction of transferred CO2).Activity DataEmission FactorComposition DataOxidation FactorConversion FactorFuel FlowNet Calorific ValueAnnex/ActivityABCABCABCABCABCABCII:CombustionCommercial standard fuels2342a/2b2a/2b2a/2b2a/2b2a/2b2a/2bn.a.n.a.n.a.111n.a.n.a.n.a.Other gaseous & liquid fuels2342a/2b2a/2b32a/2b2a/2b3n.a.n.a.n.a.111n.a.n.a.n.a.Solid fuels1232a/2b332a/2b33n.a.n.a.n.a.111n.a.n.a.n.a.Mass Balance Approach for Carbon Black Production and Gas Processing Terminals123n.a.n.a.n.a.n.a.n.a.n.a.122n.a.n.a.n.a.n.a.n.a.n.a.Flares123n.a.n.a.n.a.12a/b3n.a.n.a.n.a.111n.a.n.a.n.a.ScrubbingCarbonate111n.a.n.a.n.a.111n.a.n.a.n.a.n.a.n.a.n.a.n.a.n.a.n.a.Gypsum111n.a.n.a.n.a.111n.a.n.a.n.a.n.a.n.a.n.a.n.a.n.a.n.a.Activity DataEmission FactorComposition DataConversion FactorMaterial FlowNet Calorific ValueABCABCABCABCABCIII:RefineriesCatalytic Cracker Regeneration111n.a.n.a.n.a.n.a.n.a.n.a.n.a.n.a.n.a.n.a.n.a.n.a.Hydrogen Production122n.a.n.a.n.a.122n.a.n.a.n.a.n.a.n.a.n.a.IV:Coke OvensMass balance123n.a.n.a.n.a.n.a.n.a.n.a.233n.a.n.a.n.a.Fuel as process input123223233n.a.n.a.n.a.n.a.n.a.n.a.V:Metal Ore Roasting & SinteringMass balance123n.a.n.a.n.a.n.a.n.a.n.a.233n.a.n.a.n.a.Carbonate Input112n.a.n.a.n.a.111n.a.n.a.n.a.111VI:Iron & SteelMass balance123n.a.n.a.n.a.n.a.n.a.n.a.233n.a.n.a.n.a.Fuel as process input123223233n.a.n.a.n.a.n.a.n.a.n.a.VII:CementKiln Input Based123n.a.n.a.n.a.111n.a.n.a.n.a.112Clinker Output112n.a.n.a.n.a.123n.a.n.a.n.a.112CKD112n.a.n.a.n.a.122n.a.n.a.n.a.n.a.n.a.n.a.Non-Carbonate Carbon112n.a.n.a.n.a.112n.a.n.a.n.a.112VIII:Lime, Dolomite and MagnesiteCarbonates123n.a.n.a.n.a.111n.a.n.a.n.a.112Alkali Earth Oxide112n.a.n.a.n.a.111n.a.n.a.n.a.112IX:Glass, Mineral WoolCarbonates112n.a.n.a.n.a.111n.a.n.a.n.a.n.a.n.a.n.a.X:CeramicCarbon Inputs112n.a.n.a.n.a.123n.a.n.a.n.a.1.12Alkali Oxide112n.a.n.a.n.a.123n.a.n.a.n.a.112Scrubbing111n.a.n.a.n.a.111n.a.n.a.n.a.n.a.n.a.n.a.XI:Pulp & PaperStandard Method111n.a.n.a.n.a.111n.a.n.a.n.a.n.a.n.a.n.a.XIX:Soda ash and sodium bicarbonateMass balance123n.a.n.a.n.a.n.a.n.a.n.a.233n.a.n.a.n.a.XX:AmmoniaFuel as process input2342a/2b2a/2b32a/2b2a/2b3n.a.n.a.n.a.n.a.n.a.n.a.XXI:Hydrogen and synthesis gasFuel as process input2342a/2b2a/2b32a/2b2a/2b3n.a.n.a.n.a.n.a.n.a.n.a.Mass balance123n.a.n.a.n.a.n.a.n.a.n.a.233n.a.n.a.n.a.XXII:Bulk organic chemicalsMass balance123n.a.n.a.n.a.n.a.n.a.n.a.233n.a.n.a.n.a.XXIII:Metals production or processingMass balance123n.a.n.a.n.a.n.a.n.a.n.a.233n.a.n.a.n.a.Process emissions112n.a.n.a.n.a.111n.a.n.a.n.a.112XXIV:Aluminium productionMass balance for CO2emissions123n.a.n.a.n.a.n.a.n.a.n.a.233n.a.n.a.n.a.PFC emissions (slope method)112n.a.n.a.n.a.111n.a.n.a.n.a.n.a.n.a.n.a.PFC emissions (overvoltage method)112n.a.n.a.n.a.111n.a.n.a.n.a.n.a.n.a.n.a.’ | | Activity Data | Emission Factor | Composition Data | Oxidation Factor | Conversion Factor | Fuel Flow | Net Calorific Value | Annex/Activity | A | B | C | A | B | C | A | B | C | A | B | C | A | B | C | A | B | C | II:Combustion | Commercial standard fuels | 2 | 3 | 4 | 2a/2b | 2a/2b | 2a/2b | 2a/2b | 2a/2b | 2a/2b | n.a. | n.a. | n.a. | 1 | 1 | 1 | n.a. | n.a. | n.a. | Other gaseous & liquid fuels | 2 | 3 | 4 | 2a/2b | 2a/2b | 3 | 2a/2b | 2a/2b | 3 | n.a. | n.a. | n.a. | 1 | 1 | 1 | n.a. | n.a. | n.a. | Solid fuels | 1 | 2 | 3 | 2a/2b | 3 | 3 | 2a/2b | 3 | 3 | n.a. | n.a. | n.a. | 1 | 1 | 1 | n.a. | n.a. | n.a. | Mass Balance Approach for Carbon Black Production and Gas Processing Terminals | 1 | 2 | 3 | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | 1 | 2 | 2 | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | Flares | 1 | 2 | 3 | n.a. | n.a. | n.a. | 1 | 2a/b | 3 | n.a. | n.a. | n.a. | 1 | 1 | 1 | n.a. | n.a. | n.a. | Scrubbing | Carbonate | 1 | 1 | 1 | n.a. | n.a. | n.a. | 1 | 1 | 1 | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | | Gypsum | 1 | 1 | 1 | n.a. | n.a. | n.a. | 1 | 1 | 1 | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | | Activity Data | Emission Factor | Composition Data | Conversion Factor | Material Flow | Net Calorific Value | | A | B | C | A | B | C | A | B | C | A | B | C | A | B | C | III:Refineries | Catalytic Cracker Regeneration | 1 | 1 | 1 | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | Hydrogen Production | 1 | 2 | 2 | n.a. | n.a. | n.a. | 1 | 2 | 2 | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | IV:Coke Ovens | Mass balance | 1 | 2 | 3 | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | 2 | 3 | 3 | n.a. | n.a. | n.a. | Fuel as process input | 1 | 2 | 3 | 2 | 2 | 3 | 2 | 3 | 3 | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | V:Metal Ore Roasting & Sintering | Mass balance | 1 | 2 | 3 | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | 2 | 3 | 3 | n.a. | n.a. | n.a. | Carbonate Input | 1 | 1 | 2 | n.a. | n.a. | n.a. | 1 | 1 | 1 | n.a. | n.a. | n.a. | 1 | 1 | 1 | VI:Iron & Steel | Mass balance | 1 | 2 | 3 | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | 2 | 3 | 3 | n.a. | n.a. | n.a. | Fuel as process input | 1 | 2 | 3 | 2 | 2 | 3 | 2 | 3 | 3 | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | VII:Cement | Kiln Input Based | 1 | 2 | 3 | n.a. | n.a. | n.a. | 1 | 1 | 1 | n.a. | n.a. | n.a. | 1 | 1 | 2 | Clinker Output | 1 | 1 | 2 | n.a. | n.a. | n.a. | 1 | 2 | 3 | n.a. | n.a. | n.a. | 1 | 1 | 2 | CKD | 1 | 1 | 2 | n.a. | n.a. | n.a. | 1 | 2 | 2 | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | Non-Carbonate Carbon | 1 | 1 | 2 | n.a. | n.a. | n.a. | 1 | 1 | 2 | n.a. | n.a. | n.a. | 1 | 1 | 2 | VIII:Lime, Dolomite and Magnesite | Carbonates | 1 | 2 | 3 | n.a. | n.a. | n.a. | 1 | 1 | 1 | n.a. | n.a. | n.a. | 1 | 1 | 2 | Alkali Earth Oxide | 1 | 1 | 2 | n.a. | n.a. | n.a. | 1 | 1 | 1 | n.a. | n.a. | n.a. | 1 | 1 | 2 | IX:Glass, Mineral Wool | Carbonates | 1 | 1 | 2 | n.a. | n.a. | n.a. | 1 | 1 | 1 | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | X:Ceramic | Carbon Inputs | 1 | 1 | 2 | n.a. | n.a. | n.a. | 1 | 2 | 3 | n.a. | n.a. | n.a. | 1. | 1 | 2 | Alkali Oxide | 1 | 1 | 2 | n.a. | n.a. | n.a. | 1 | 2 | 3 | n.a. | n.a. | n.a. | 1 | 1 | 2 | Scrubbing | 1 | 1 | 1 | n.a. | n.a. | n.a. | 1 | 1 | 1 | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | XI:Pulp & Paper | Standard Method | 1 | 1 | 1 | n.a. | n.a. | n.a. | 1 | 1 | 1 | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | XIX:Soda ash and sodium bicarbonate | Mass balance | 1 | 2 | 3 | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | 2 | 3 | 3 | n.a. | n.a. | n.a. | XX:Ammonia | Fuel as process input | 2 | 3 | 4 | 2a/2b | 2a/2b | 3 | 2a/2b | 2a/2b | 3 | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | XXI:Hydrogen and synthesis gas | Fuel as process input | 2 | 3 | 4 | 2a/2b | 2a/2b | 3 | 2a/2b | 2a/2b | 3 | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | Mass balance | 1 | 2 | 3 | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | 2 | 3 | 3 | n.a. | n.a. | n.a. | XXII:Bulk organic chemicals | Mass balance | 1 | 2 | 3 | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | 2 | 3 | 3 | n.a. | n.a. | n.a. | XXIII:Metals production or processing | Mass balance | 1 | 2 | 3 | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | 2 | 3 | 3 | n.a. | n.a. | n.a. | Process emissions | 1 | 1 | 2 | n.a. | n.a. | n.a. | 1 | 1 | 1 | n.a. | n.a. | n.a. | 1 | 1 | 2 | XXIV:Aluminium production | Mass balance for CO2emissions | 1 | 2 | 3 | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | 2 | 3 | 3 | n.a. | n.a. | n.a. | PFC emissions (slope method) | 1 | 1 | 2 | n.a. | n.a. | n.a. | 1 | 1 | 1 | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | PFC emissions (overvoltage method) | 1 | 1 | 2 | n.a. | n.a. | n.a. | 1 | 1 | 1 | n.a. | n.a. | n.a. | n.a. | n.a. | n.a.’ | (e) | in Section 5.4 entitled ‘Activity Data of Stationary Installations’, in the second subparagraph, the words ‘Annexes II to XI’ are replaced by the words ‘Annexes II to XXIV’; | (f) | in Section 5.5, entitled ‘Emissions Factors’, the first paragraph is replaced by the following:‘Emission factors for CO2emissions are based on the carbon content of fuels or input materials and expressed as tCO2/TJ (combustion emissions), or tCO2/t or tCO2/Nm3(process emissions). For non-CO2greenhouse gases, appropriate emission factors are defined in the relevant activity-specific Annexes to these Guidelines.’; | (g) | Section 5.7 is amended as follows:—the first indent of the first paragraph is replaced by the following:‘as pure substance, or directly used and bound in products or as feedstock, unless other requirements as set out in Annexes XIX to XXII apply, or’,—in the second paragraph, the words ‘or XVIII’ are replaced by ‘to XXII’; | — | the first indent of the first paragraph is replaced by the following:‘as pure substance, or directly used and bound in products or as feedstock, unless other requirements as set out in Annexes XIX to XXII apply, or’, | — | in the second paragraph, the words ‘or XVIII’ are replaced by ‘to XXII’;
(a) | in Section 5.1, under the heading ‘process emissions’, the second paragraph is replaced by the following:‘The calculation of process emissions is further specified in the activity-specific guidelines in the Annexes II to XI and XVI to XXIV. Not all calculation methods in Annexes II to XI and XVI to XXIV use a conversion factor.’;
(b) | in Section 5.2 entitled ‘Tiers of Approaches’, the words ‘Annexes II to XI and Annexes XIV to XVIII’ are replaced by the words ‘Annexes II to XI and XIV to XXIV’;
(c) | in Section 5.2, the following ninth paragraph is added:‘For commercial standard fuels minimum tier approaches as stated in Table 1 for Annex II on combustion activities can be applied also for other activities.’;
(d) | ‘Table 1: Minimum Requirements’ is replaced by the following table:‘Table 1Minimum requirements(‘n.a.’ means ‘not applicable’)Column A for ‘category A installations’ (means installations with average reported annual emissions over the previous trading period (or a conservative estimate or projection if reported emissions are not available or no longer applicable) equal to or less than 50 kilotonnes of CO2-eqnot including biogenic CO2and before subtraction of transferred CO2),Column B for ‘category B installations’ (means installations with average reported annual emissions over the previous trading period (or a conservative estimate or projection if reported emissions are not available or no longer applicable) of greater than 50 kilotonnes and equal to or less than 500 kilotonnes of CO2-eqnot including biogenic CO2and before subtraction of transferred CO2),and Column C for ‘category C installations’ (means installations with average reported annual emissions over the previous trading period (or a conservative estimate or projection if reported emissions are not available or no longer applicable) of greater than 500 kilotonnes of CO2-eqnot including biogenic CO2and before subtraction of transferred CO2).Activity DataEmission FactorComposition DataOxidation FactorConversion FactorFuel FlowNet Calorific ValueAnnex/ActivityABCABCABCABCABCABCII:CombustionCommercial standard fuels2342a/2b2a/2b2a/2b2a/2b2a/2b2a/2bn.a.n.a.n.a.111n.a.n.a.n.a.Other gaseous & liquid fuels2342a/2b2a/2b32a/2b2a/2b3n.a.n.a.n.a.111n.a.n.a.n.a.Solid fuels1232a/2b332a/2b33n.a.n.a.n.a.111n.a.n.a.n.a.Mass Balance Approach for Carbon Black Production and Gas Processing Terminals123n.a.n.a.n.a.n.a.n.a.n.a.122n.a.n.a.n.a.n.a.n.a.n.a.Flares123n.a.n.a.n.a.12a/b3n.a.n.a.n.a.111n.a.n.a.n.a.ScrubbingCarbonate111n.a.n.a.n.a.111n.a.n.a.n.a.n.a.n.a.n.a.n.a.n.a.n.a.Gypsum111n.a.n.a.n.a.111n.a.n.a.n.a.n.a.n.a.n.a.n.a.n.a.n.a.Activity DataEmission FactorComposition DataConversion FactorMaterial FlowNet Calorific ValueABCABCABCABCABCIII:RefineriesCatalytic Cracker Regeneration111n.a.n.a.n.a.n.a.n.a.n.a.n.a.n.a.n.a.n.a.n.a.n.a.Hydrogen Production122n.a.n.a.n.a.122n.a.n.a.n.a.n.a.n.a.n.a.IV:Coke OvensMass balance123n.a.n.a.n.a.n.a.n.a.n.a.233n.a.n.a.n.a.Fuel as process input123223233n.a.n.a.n.a.n.a.n.a.n.a.V:Metal Ore Roasting & SinteringMass balance123n.a.n.a.n.a.n.a.n.a.n.a.233n.a.n.a.n.a.Carbonate Input112n.a.n.a.n.a.111n.a.n.a.n.a.111VI:Iron & SteelMass balance123n.a.n.a.n.a.n.a.n.a.n.a.233n.a.n.a.n.a.Fuel as process input123223233n.a.n.a.n.a.n.a.n.a.n.a.VII:CementKiln Input Based123n.a.n.a.n.a.111n.a.n.a.n.a.112Clinker Output112n.a.n.a.n.a.123n.a.n.a.n.a.112CKD112n.a.n.a.n.a.122n.a.n.a.n.a.n.a.n.a.n.a.Non-Carbonate Carbon112n.a.n.a.n.a.112n.a.n.a.n.a.112VIII:Lime, Dolomite and MagnesiteCarbonates123n.a.n.a.n.a.111n.a.n.a.n.a.112Alkali Earth Oxide112n.a.n.a.n.a.111n.a.n.a.n.a.112IX:Glass, Mineral WoolCarbonates112n.a.n.a.n.a.111n.a.n.a.n.a.n.a.n.a.n.a.X:CeramicCarbon Inputs112n.a.n.a.n.a.123n.a.n.a.n.a.1.12Alkali Oxide112n.a.n.a.n.a.123n.a.n.a.n.a.112Scrubbing111n.a.n.a.n.a.111n.a.n.a.n.a.n.a.n.a.n.a.XI:Pulp & PaperStandard Method111n.a.n.a.n.a.111n.a.n.a.n.a.n.a.n.a.n.a.XIX:Soda ash and sodium bicarbonateMass balance123n.a.n.a.n.a.n.a.n.a.n.a.233n.a.n.a.n.a.XX:AmmoniaFuel as process input2342a/2b2a/2b32a/2b2a/2b3n.a.n.a.n.a.n.a.n.a.n.a.XXI:Hydrogen and synthesis gasFuel as process input2342a/2b2a/2b32a/2b2a/2b3n.a.n.a.n.a.n.a.n.a.n.a.Mass balance123n.a.n.a.n.a.n.a.n.a.n.a.233n.a.n.a.n.a.XXII:Bulk organic chemicalsMass balance123n.a.n.a.n.a.n.a.n.a.n.a.233n.a.n.a.n.a.XXIII:Metals production or processingMass balance123n.a.n.a.n.a.n.a.n.a.n.a.233n.a.n.a.n.a.Process emissions112n.a.n.a.n.a.111n.a.n.a.n.a.112XXIV:Aluminium productionMass balance for CO2emissions123n.a.n.a.n.a.n.a.n.a.n.a.233n.a.n.a.n.a.PFC emissions (slope method)112n.a.n.a.n.a.111n.a.n.a.n.a.n.a.n.a.n.a.PFC emissions (overvoltage method)112n.a.n.a.n.a.111n.a.n.a.n.a.n.a.n.a.n.a.’ | | Activity Data | Emission Factor | Composition Data | Oxidation Factor | Conversion Factor | Fuel Flow | Net Calorific Value | Annex/Activity | A | B | C | A | B | C | A | B | C | A | B | C | A | B | C | A | B | C | II:Combustion | Commercial standard fuels | 2 | 3 | 4 | 2a/2b | 2a/2b | 2a/2b | 2a/2b | 2a/2b | 2a/2b | n.a. | n.a. | n.a. | 1 | 1 | 1 | n.a. | n.a. | n.a. | Other gaseous & liquid fuels | 2 | 3 | 4 | 2a/2b | 2a/2b | 3 | 2a/2b | 2a/2b | 3 | n.a. | n.a. | n.a. | 1 | 1 | 1 | n.a. | n.a. | n.a. | Solid fuels | 1 | 2 | 3 | 2a/2b | 3 | 3 | 2a/2b | 3 | 3 | n.a. | n.a. | n.a. | 1 | 1 | 1 | n.a. | n.a. | n.a. | Mass Balance Approach for Carbon Black Production and Gas Processing Terminals | 1 | 2 | 3 | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | 1 | 2 | 2 | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | Flares | 1 | 2 | 3 | n.a. | n.a. | n.a. | 1 | 2a/b | 3 | n.a. | n.a. | n.a. | 1 | 1 | 1 | n.a. | n.a. | n.a. | Scrubbing | Carbonate | 1 | 1 | 1 | n.a. | n.a. | n.a. | 1 | 1 | 1 | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | | Gypsum | 1 | 1 | 1 | n.a. | n.a. | n.a. | 1 | 1 | 1 | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | | Activity Data | Emission Factor | Composition Data | Conversion Factor | Material Flow | Net Calorific Value | | A | B | C | A | B | C | A | B | C | A | B | C | A | B | C | III:Refineries | Catalytic Cracker Regeneration | 1 | 1 | 1 | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | Hydrogen Production | 1 | 2 | 2 | n.a. | n.a. | n.a. | 1 | 2 | 2 | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | IV:Coke Ovens | Mass balance | 1 | 2 | 3 | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | 2 | 3 | 3 | n.a. | n.a. | n.a. | Fuel as process input | 1 | 2 | 3 | 2 | 2 | 3 | 2 | 3 | 3 | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | V:Metal Ore Roasting & Sintering | Mass balance | 1 | 2 | 3 | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | 2 | 3 | 3 | n.a. | n.a. | n.a. | Carbonate Input | 1 | 1 | 2 | n.a. | n.a. | n.a. | 1 | 1 | 1 | n.a. | n.a. | n.a. | 1 | 1 | 1 | VI:Iron & Steel | Mass balance | 1 | 2 | 3 | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | 2 | 3 | 3 | n.a. | n.a. | n.a. | Fuel as process input | 1 | 2 | 3 | 2 | 2 | 3 | 2 | 3 | 3 | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | VII:Cement | Kiln Input Based | 1 | 2 | 3 | n.a. | n.a. | n.a. | 1 | 1 | 1 | n.a. | n.a. | n.a. | 1 | 1 | 2 | Clinker Output | 1 | 1 | 2 | n.a. | n.a. | n.a. | 1 | 2 | 3 | n.a. | n.a. | n.a. | 1 | 1 | 2 | CKD | 1 | 1 | 2 | n.a. | n.a. | n.a. | 1 | 2 | 2 | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | Non-Carbonate Carbon | 1 | 1 | 2 | n.a. | n.a. | n.a. | 1 | 1 | 2 | n.a. | n.a. | n.a. | 1 | 1 | 2 | VIII:Lime, Dolomite and Magnesite | Carbonates | 1 | 2 | 3 | n.a. | n.a. | n.a. | 1 | 1 | 1 | n.a. | n.a. | n.a. | 1 | 1 | 2 | Alkali Earth Oxide | 1 | 1 | 2 | n.a. | n.a. | n.a. | 1 | 1 | 1 | n.a. | n.a. | n.a. | 1 | 1 | 2 | IX:Glass, Mineral Wool | Carbonates | 1 | 1 | 2 | n.a. | n.a. | n.a. | 1 | 1 | 1 | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | X:Ceramic | Carbon Inputs | 1 | 1 | 2 | n.a. | n.a. | n.a. | 1 | 2 | 3 | n.a. | n.a. | n.a. | 1. | 1 | 2 | Alkali Oxide | 1 | 1 | 2 | n.a. | n.a. | n.a. | 1 | 2 | 3 | n.a. | n.a. | n.a. | 1 | 1 | 2 | Scrubbing | 1 | 1 | 1 | n.a. | n.a. | n.a. | 1 | 1 | 1 | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | XI:Pulp & Paper | Standard Method | 1 | 1 | 1 | n.a. | n.a. | n.a. | 1 | 1 | 1 | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | XIX:Soda ash and sodium bicarbonate | Mass balance | 1 | 2 | 3 | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | 2 | 3 | 3 | n.a. | n.a. | n.a. | XX:Ammonia | Fuel as process input | 2 | 3 | 4 | 2a/2b | 2a/2b | 3 | 2a/2b | 2a/2b | 3 | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | XXI:Hydrogen and synthesis gas | Fuel as process input | 2 | 3 | 4 | 2a/2b | 2a/2b | 3 | 2a/2b | 2a/2b | 3 | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | Mass balance | 1 | 2 | 3 | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | 2 | 3 | 3 | n.a. | n.a. | n.a. | XXII:Bulk organic chemicals | Mass balance | 1 | 2 | 3 | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | 2 | 3 | 3 | n.a. | n.a. | n.a. | XXIII:Metals production or processing | Mass balance | 1 | 2 | 3 | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | 2 | 3 | 3 | n.a. | n.a. | n.a. | Process emissions | 1 | 1 | 2 | n.a. | n.a. | n.a. | 1 | 1 | 1 | n.a. | n.a. | n.a. | 1 | 1 | 2 | XXIV:Aluminium production | Mass balance for CO2emissions | 1 | 2 | 3 | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | 2 | 3 | 3 | n.a. | n.a. | n.a. | PFC emissions (slope method) | 1 | 1 | 2 | n.a. | n.a. | n.a. | 1 | 1 | 1 | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | PFC emissions (overvoltage method) | 1 | 1 | 2 | n.a. | n.a. | n.a. | 1 | 1 | 1 | n.a. | n.a. | n.a. | n.a. | n.a. | n.a.’
| Activity Data | Emission Factor | Composition Data | Oxidation Factor | Conversion Factor
Fuel Flow | Net Calorific Value
Annex/Activity | A | B | C | A | B | C | A | B | C | A | B | C | A | B | C | A | B | C
II:Combustion
Commercial standard fuels | 2 | 3 | 4 | 2a/2b | 2a/2b | 2a/2b | 2a/2b | 2a/2b | 2a/2b | n.a. | n.a. | n.a. | 1 | 1 | 1 | n.a. | n.a. | n.a.
Other gaseous & liquid fuels | 2 | 3 | 4 | 2a/2b | 2a/2b | 3 | 2a/2b | 2a/2b | 3 | n.a. | n.a. | n.a. | 1 | 1 | 1 | n.a. | n.a. | n.a.
Solid fuels | 1 | 2 | 3 | 2a/2b | 3 | 3 | 2a/2b | 3 | 3 | n.a. | n.a. | n.a. | 1 | 1 | 1 | n.a. | n.a. | n.a.
Mass Balance Approach for Carbon Black Production and Gas Processing Terminals | 1 | 2 | 3 | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | 1 | 2 | 2 | n.a. | n.a. | n.a. | n.a. | n.a. | n.a.
Flares | 1 | 2 | 3 | n.a. | n.a. | n.a. | 1 | 2a/b | 3 | n.a. | n.a. | n.a. | 1 | 1 | 1 | n.a. | n.a. | n.a.
Scrubbing | Carbonate | 1 | 1 | 1 | n.a. | n.a. | n.a. | 1 | 1 | 1 | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | n.a.
| Gypsum | 1 | 1 | 1 | n.a. | n.a. | n.a. | 1 | 1 | 1 | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | n.a.
| Activity Data | Emission Factor | Composition Data | Conversion Factor
Material Flow | Net Calorific Value
| A | B | C | A | B | C | A | B | C | A | B | C | A | B | C
III:Refineries
Catalytic Cracker Regeneration | 1 | 1 | 1 | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | n.a.
Hydrogen Production | 1 | 2 | 2 | n.a. | n.a. | n.a. | 1 | 2 | 2 | n.a. | n.a. | n.a. | n.a. | n.a. | n.a.
IV:Coke Ovens
Mass balance | 1 | 2 | 3 | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | 2 | 3 | 3 | n.a. | n.a. | n.a.
Fuel as process input | 1 | 2 | 3 | 2 | 2 | 3 | 2 | 3 | 3 | n.a. | n.a. | n.a. | n.a. | n.a. | n.a.
V:Metal Ore Roasting & Sintering
Mass balance | 1 | 2 | 3 | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | 2 | 3 | 3 | n.a. | n.a. | n.a.
Carbonate Input | 1 | 1 | 2 | n.a. | n.a. | n.a. | 1 | 1 | 1 | n.a. | n.a. | n.a. | 1 | 1 | 1
VI:Iron & Steel
Mass balance | 1 | 2 | 3 | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | 2 | 3 | 3 | n.a. | n.a. | n.a.
Fuel as process input | 1 | 2 | 3 | 2 | 2 | 3 | 2 | 3 | 3 | n.a. | n.a. | n.a. | n.a. | n.a. | n.a.
VII:Cement
Kiln Input Based | 1 | 2 | 3 | n.a. | n.a. | n.a. | 1 | 1 | 1 | n.a. | n.a. | n.a. | 1 | 1 | 2
Clinker Output | 1 | 1 | 2 | n.a. | n.a. | n.a. | 1 | 2 | 3 | n.a. | n.a. | n.a. | 1 | 1 | 2
CKD | 1 | 1 | 2 | n.a. | n.a. | n.a. | 1 | 2 | 2 | n.a. | n.a. | n.a. | n.a. | n.a. | n.a.
Non-Carbonate Carbon | 1 | 1 | 2 | n.a. | n.a. | n.a. | 1 | 1 | 2 | n.a. | n.a. | n.a. | 1 | 1 | 2
VIII:Lime, Dolomite and Magnesite
Carbonates | 1 | 2 | 3 | n.a. | n.a. | n.a. | 1 | 1 | 1 | n.a. | n.a. | n.a. | 1 | 1 | 2
Alkali Earth Oxide | 1 | 1 | 2 | n.a. | n.a. | n.a. | 1 | 1 | 1 | n.a. | n.a. | n.a. | 1 | 1 | 2
IX:Glass, Mineral Wool
Carbonates | 1 | 1 | 2 | n.a. | n.a. | n.a. | 1 | 1 | 1 | n.a. | n.a. | n.a. | n.a. | n.a. | n.a.
X:Ceramic
Carbon Inputs | 1 | 1 | 2 | n.a. | n.a. | n.a. | 1 | 2 | 3 | n.a. | n.a. | n.a. | 1. | 1 | 2
Alkali Oxide | 1 | 1 | 2 | n.a. | n.a. | n.a. | 1 | 2 | 3 | n.a. | n.a. | n.a. | 1 | 1 | 2
Scrubbing | 1 | 1 | 1 | n.a. | n.a. | n.a. | 1 | 1 | 1 | n.a. | n.a. | n.a. | n.a. | n.a. | n.a.
XI:Pulp & Paper
Standard Method | 1 | 1 | 1 | n.a. | n.a. | n.a. | 1 | 1 | 1 | n.a. | n.a. | n.a. | n.a. | n.a. | n.a.
XIX:Soda ash and sodium bicarbonate
Mass balance | 1 | 2 | 3 | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | 2 | 3 | 3 | n.a. | n.a. | n.a.
XX:Ammonia
Fuel as process input | 2 | 3 | 4 | 2a/2b | 2a/2b | 3 | 2a/2b | 2a/2b | 3 | n.a. | n.a. | n.a. | n.a. | n.a. | n.a.
XXI:Hydrogen and synthesis gas
Fuel as process input | 2 | 3 | 4 | 2a/2b | 2a/2b | 3 | 2a/2b | 2a/2b | 3 | n.a. | n.a. | n.a. | n.a. | n.a. | n.a.
Mass balance | 1 | 2 | 3 | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | 2 | 3 | 3 | n.a. | n.a. | n.a.
XXII:Bulk organic chemicals
Mass balance | 1 | 2 | 3 | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | 2 | 3 | 3 | n.a. | n.a. | n.a.
XXIII:Metals production or processing
Mass balance | 1 | 2 | 3 | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | 2 | 3 | 3 | n.a. | n.a. | n.a.
Process emissions | 1 | 1 | 2 | n.a. | n.a. | n.a. | 1 | 1 | 1 | n.a. | n.a. | n.a. | 1 | 1 | 2
XXIV:Aluminium production
Mass balance for CO2emissions | 1 | 2 | 3 | n.a. | n.a. | n.a. | n.a. | n.a. | n.a. | 2 | 3 | 3 | n.a. | n.a. | n.a.
PFC emissions (slope method) | 1 | 1 | 2 | n.a. | n.a. | n.a. | 1 | 1 | 1 | n.a. | n.a. | n.a. | n.a. | n.a. | n.a.
PFC emissions (overvoltage method) | 1 | 1 | 2 | n.a. | n.a. | n.a. | 1 | 1 | 1 | n.a. | n.a. | n.a. | n.a. | n.a. | n.a.’
(e) | in Section 5.4 entitled ‘Activity Data of Stationary Installations’, in the second subparagraph, the words ‘Annexes II to XI’ are replaced by the words ‘Annexes II to XXIV’;
(f) | in Section 5.5, entitled ‘Emissions Factors’, the first paragraph is replaced by the following:‘Emission factors for CO2emissions are based on the carbon content of fuels or input materials and expressed as tCO2/TJ (combustion emissions), or tCO2/t or tCO2/Nm3(process emissions). For non-CO2greenhouse gases, appropriate emission factors are defined in the relevant activity-specific Annexes to these Guidelines.’;
(g) | Section 5.7 is amended as follows:—the first indent of the first paragraph is replaced by the following:‘as pure substance, or directly used and bound in products or as feedstock, unless other requirements as set out in Annexes XIX to XXII apply, or’,—in the second paragraph, the words ‘or XVIII’ are replaced by ‘to XXII’; | — | the first indent of the first paragraph is replaced by the following:‘as pure substance, or directly used and bound in products or as feedstock, unless other requirements as set out in Annexes XIX to XXII apply, or’, | — | in the second paragraph, the words ‘or XVIII’ are replaced by ‘to XXII’;
— | the first indent of the first paragraph is replaced by the following:‘as pure substance, or directly used and bound in products or as feedstock, unless other requirements as set out in Annexes XIX to XXII apply, or’,
— | in the second paragraph, the words ‘or XVIII’ are replaced by ‘to XXII’;
(5) | in Section 6.3(c), third paragraph, the words ‘, XVII and XVIII’ are replaced by ‘to XXIV’;
(6) | in Section 7.1, fifth paragraph, the word ‘XVIII’ is replaced by XXIV’;
(7) | Section 8 is amended as follows:(a)in subparagraph (6) of the fifth paragraph, the words ‘, XVII and XVIII’ are replaced by ‘to XXIV’;(b)the following subparagraph (11) is added to the fifth paragraph:‘(11)where applicable, the production level of primary aluminium, the frequency and average duration of anode effects during the reporting period, or the anode effect overvoltage data during the reporting period, as well as the results of the most recent determination of the installation specific emission factors for CF4and C2F6as outlined in Annex XXIV, and of the most recent determination of the collection efficiency of the ducts.’;(c)In Section 8, seventh paragraph, the words ‘under (2)’ are replaced by ‘under (2) and (11)’; | (a) | in subparagraph (6) of the fifth paragraph, the words ‘, XVII and XVIII’ are replaced by ‘to XXIV’; | (b) | the following subparagraph (11) is added to the fifth paragraph:‘(11)where applicable, the production level of primary aluminium, the frequency and average duration of anode effects during the reporting period, or the anode effect overvoltage data during the reporting period, as well as the results of the most recent determination of the installation specific emission factors for CF4and C2F6as outlined in Annex XXIV, and of the most recent determination of the collection efficiency of the ducts.’; | ‘(11) | where applicable, the production level of primary aluminium, the frequency and average duration of anode effects during the reporting period, or the anode effect overvoltage data during the reporting period, as well as the results of the most recent determination of the installation specific emission factors for CF4and C2F6as outlined in Annex XXIV, and of the most recent determination of the collection efficiency of the ducts.’; | (c) | In Section 8, seventh paragraph, the words ‘under (2)’ are replaced by ‘under (2) and (11)’;
(a) | in subparagraph (6) of the fifth paragraph, the words ‘, XVII and XVIII’ are replaced by ‘to XXIV’;
(b) | the following subparagraph (11) is added to the fifth paragraph:‘(11)where applicable, the production level of primary aluminium, the frequency and average duration of anode effects during the reporting period, or the anode effect overvoltage data during the reporting period, as well as the results of the most recent determination of the installation specific emission factors for CF4and C2F6as outlined in Annex XXIV, and of the most recent determination of the collection efficiency of the ducts.’; | ‘(11) | where applicable, the production level of primary aluminium, the frequency and average duration of anode effects during the reporting period, or the anode effect overvoltage data during the reporting period, as well as the results of the most recent determination of the installation specific emission factors for CF4and C2F6as outlined in Annex XXIV, and of the most recent determination of the collection efficiency of the ducts.’;
‘(11) | where applicable, the production level of primary aluminium, the frequency and average duration of anode effects during the reporting period, or the anode effect overvoltage data during the reporting period, as well as the results of the most recent determination of the installation specific emission factors for CF4and C2F6as outlined in Annex XXIV, and of the most recent determination of the collection efficiency of the ducts.’;
(c) | In Section 8, seventh paragraph, the words ‘under (2)’ are replaced by ‘under (2) and (11)’;
(8) | in Section 9, the following ninth paragraph is added:‘The following additional information shall be retained for primary aluminium production:—documentation of results from measurement campaigns for the determination of the installation specific emission factors for CF4and C2F6,—documentation of results of the determination of the collection efficiency for fugitive emissions,—all relevant data on primary aluminium production, anode effect frequency and duration or overvoltage data.’; | — | documentation of results from measurement campaigns for the determination of the installation specific emission factors for CF4and C2F6, | — | documentation of results of the determination of the collection efficiency for fugitive emissions, | — | all relevant data on primary aluminium production, anode effect frequency and duration or overvoltage data.’;
— | documentation of results from measurement campaigns for the determination of the installation specific emission factors for CF4and C2F6,
— | documentation of results of the determination of the collection efficiency for fugitive emissions,
— | all relevant data on primary aluminium production, anode effect frequency and duration or overvoltage data.’;
(9) | Section 14.1 is amended as follows:In footnote 2 the text is replaced by the following: ‘Only to be filled in if installation is required to report under EPRTR.’;
(10) | a new Section 14.8 is added:‘14.8. PFC EMISSIONS REPORTING FOR PRODUCTION OF PRIMARY ALUMINIUMActivityCell typeSlope method (A) or overvoltage method (B)?ParameterUnitValueTier appliedPrimary aluminium productiontMethod ANumber of anode effectsAverage duration of anode effectsminAnode effect minutes/cell-daymin/cell-daySEFCF4 …Slope emission factor(kg CF4/t Al)/(min/cell-day)Method BAEO … Anode effect overvoltage per cellmVCE … average current efficiency%AEO/CEmVOVC … Overvoltage coefficientkg CF4/ (t Al mV)FC2F6 …Weight fraction of C2F6t C2F6/t CF4CF4emissionstC2F6emissionstGWPCF4appliedt CO2(e)/tGWPC2F6appliedt CO2(e)/tTotal emissionst CO2(e)’ | | Activity | | Cell type | | Slope method (A) or overvoltage method (B)? | | Parameter | Unit | Value | Tier applied | Primary aluminium production | t | | | Method A | Number of anode effects | | | | Average duration of anode effects | min | | | Anode effect minutes/cell-day | min/cell-day | | | SEFCF4 …Slope emission factor | (kg CF4/t Al)/(min/cell-day) | | | Method B | AEO … Anode effect overvoltage per cell | mV | | | CE … average current efficiency | % | | | AEO/CE | mV | | | OVC … Overvoltage coefficient | kg CF4/ (t Al mV) | | | | FC2F6 …Weight fraction of C2F6 | t C2F6/t CF4 | | | CF4emissions | t | | | C2F6emissions | t | | | GWPCF4applied | t CO2(e)/t | | | GWPC2F6applied | t CO2(e)/t | | | | Total emissions | t CO2(e)’ | |
| Activity |
Cell type |
Slope method (A) or overvoltage method (B)? |
Parameter | Unit | Value | Tier applied
Primary aluminium production | t | |
Method A | Number of anode effects | | |
Average duration of anode effects | min | |
Anode effect minutes/cell-day | min/cell-day | |
SEFCF4 …Slope emission factor | (kg CF4/t Al)/(min/cell-day) | |
Method B | AEO … Anode effect overvoltage per cell | mV | |
CE … average current efficiency | % | |
AEO/CE | mV | |
OVC … Overvoltage coefficient | kg CF4/ (t Al mV) | |
| FC2F6 …Weight fraction of C2F6 | t C2F6/t CF4 | |
CF4emissions | t | |
C2F6emissions | t | |
GWPCF4applied | t CO2(e)/t | |
GWPC2F6applied | t CO2(e)/t | |
| Total emissions | t CO2(e)’ | |

(1) | the title of Annex II is replaced by the following:‘Guidelines for combustion emissions from activities as listed in Annex I to Directive 2003/87/EC carried out in installations’;
(2) | in Section 1, the first paragraph is replaced by the following:‘The activity-specific guidelines contained in this Annex shall be used to monitor emissions from combustion activities as listed in Annex I to Directive 2003/87/EC carried out in installations and defined pursuant to Article 3(t) and to monitor combustion emissions from other activities as listed in that Annex I to Directive 2003/87/EC where referred to in Annexes III to XI and XVI to XXIV to these Guidelines. Furthermore this Annex shall be used to monitor emissions from combustion processes being part of any activity listed in Annex I to Directive 2003/87/EC for which no other activity-specific Annex to these Guidelines applies.’;
(3) | Section 2 is amended as follows:(a)in the introductory phrase, the wording ‘installations and processes’ is replaced by ‘activities’;(b)in the first paragraph of Section 2.1.1.1, the word ‘installations’ is replaced by ‘activities’;(c)in Section 2.1.1.2(b), Carbon Content, Tier 1, the wording ‘the Annexes IV-VI’ is replaced by ‘other activity-specific Annexes.’. | (a) | in the introductory phrase, the wording ‘installations and processes’ is replaced by ‘activities’; | (b) | in the first paragraph of Section 2.1.1.1, the word ‘installations’ is replaced by ‘activities’; | (c) | in Section 2.1.1.2(b), Carbon Content, Tier 1, the wording ‘the Annexes IV-VI’ is replaced by ‘other activity-specific Annexes.’.
(a) | in the introductory phrase, the wording ‘installations and processes’ is replaced by ‘activities’;
(b) | in the first paragraph of Section 2.1.1.1, the word ‘installations’ is replaced by ‘activities’;
(c) | in Section 2.1.1.2(b), Carbon Content, Tier 1, the wording ‘the Annexes IV-VI’ is replaced by ‘other activity-specific Annexes.’.

(1) | The title of Annex IV is replaced by the following:‘Activity-specific guidelines for the production of coke as listed in Annex I to Directive 2003/87/EC’;
(2) | The first paragraph of Section 1 is replaced by the following:‘Coke ovens can be part of steel works with a direct technical connection to sintering activities and activities for the production of pig iron and steel including continuous casting, causing an intensive energy and material exchange (for example, blast furnace gas, coke oven gas or coke) to take place in regular operation. If an installation’s permit according to Articles 4, 5 and 6 of Directive 2003/87/EC encompasses the entire steel works and not solely the coke oven, the CO2-emissions may also be monitored for the integrated steel works as a whole, using the mass balance approach specified in Section 2.1.1 of this Annex.’;
(3) | In Section 2.1.1(b) Carbon Content, Tier 1, the introductory phrase is replaced by the following:‘The carbon content of input or output streams is derived from reference emission factors for fuels or materials named in Section 11 of Annex I or the Annexes IV-X. The carbon content is derived as follows:’.

(1) | the title of Annex V is replaced by the following:‘Activity-Specific Guidelines for metal ore roasting and sintering as listed in Annex I to Directive 2003/87/EC’;
(2) | the first paragraph of Section 1 is replaced by the following:‘Metal ore roasting, sintering or pelletisation activities can form an integral part of steel works with a direct technical connection to coke ovens and activities for the production of pig iron and steel including continuous casting. Thus an intensive energy and material exchange (e.g. blast furnace gas, coke oven gas, coke or limestone) takes place in regular operation. If an installation’s permit according to Articles 4, 5 and 6 of Directive 2003/87/EC encompasses the entire steel works and not solely the roasting or sintering activity, the CO2-emissions may also be monitored for the integrated steel works as a whole. In such cases the mass balance approach (Section 2.1.1 of this Annex) may be used.’;
(3) | in Section 2.1.1(b) Carbon Content, Tier 1, the introductory phrase is replaced by the following:‘The carbon content of input or output streams is derived from reference emission factors for fuels or materials named in Section 11 of Annex I or the Annexes IV-X. The carbon content is derived as follows:’.

(1) | the title of Annex VI is replaced by the following:‘Activity-specific guidelines for the production of pig iron and steel including continuous casting as listed in Annex I to Directive 2003/87/EC’;
(2) | Section 1 is modified as follows:(a)the first paragraph is replaced by the following wording: ‘The guidelines in this Annex can be applied for emissions from production of pig iron and steel activities, including continuous casting activities. They refer in particular to primary (blast furnace (BF) and basic oxygen furnace (BOF)) and secondary (electric arc furnace (EAF)) steel production.’;(b)the second paragraph is replaced by the following wording: ‘Activities for the production of pig iron and steel including continuous casting are generally integral parts of steel works with a technical connection to coke oven and sinter activities. Thus an intensive energy and material exchange (e.g. blast furnace gas, coke oven gas, coke or limestone) takes place in regular operation. If an installation’s permit according to Articles 4, 5 and 6 of Directive 2003/87/EC encompasses the entire steel works and not solely the blast furnace, the CO2-emissions may also be monitored for the integrated steel works as a whole. In such cases the mass balance approach as presented in Section 2.1.1 of this Annex may be used.’; | (a) | the first paragraph is replaced by the following wording: ‘The guidelines in this Annex can be applied for emissions from production of pig iron and steel activities, including continuous casting activities. They refer in particular to primary (blast furnace (BF) and basic oxygen furnace (BOF)) and secondary (electric arc furnace (EAF)) steel production.’; | (b) | the second paragraph is replaced by the following wording: ‘Activities for the production of pig iron and steel including continuous casting are generally integral parts of steel works with a technical connection to coke oven and sinter activities. Thus an intensive energy and material exchange (e.g. blast furnace gas, coke oven gas, coke or limestone) takes place in regular operation. If an installation’s permit according to Articles 4, 5 and 6 of Directive 2003/87/EC encompasses the entire steel works and not solely the blast furnace, the CO2-emissions may also be monitored for the integrated steel works as a whole. In such cases the mass balance approach as presented in Section 2.1.1 of this Annex may be used.’;
(a) | the first paragraph is replaced by the following wording: ‘The guidelines in this Annex can be applied for emissions from production of pig iron and steel activities, including continuous casting activities. They refer in particular to primary (blast furnace (BF) and basic oxygen furnace (BOF)) and secondary (electric arc furnace (EAF)) steel production.’;
(b) | the second paragraph is replaced by the following wording: ‘Activities for the production of pig iron and steel including continuous casting are generally integral parts of steel works with a technical connection to coke oven and sinter activities. Thus an intensive energy and material exchange (e.g. blast furnace gas, coke oven gas, coke or limestone) takes place in regular operation. If an installation’s permit according to Articles 4, 5 and 6 of Directive 2003/87/EC encompasses the entire steel works and not solely the blast furnace, the CO2-emissions may also be monitored for the integrated steel works as a whole. In such cases the mass balance approach as presented in Section 2.1.1 of this Annex may be used.’;
(3) | in Section 2.1.1(b) Carbon Content, Tier 1, the introductory phrase is replaced by the following:‘The carbon content of input or output streams is derived from reference emission factors for fuels or materials named in Section 11 of Annex I or the Annexes IV-X. The carbon content is derived as follows:’.

(1) | the title of Annex VII is replaced by the following:‘Activity-specific guidelines for the production of cement clinker as listed in Annex I to Directive 2003/87/EC’;
(2) | the first sentence of Section 2 is replaced by the following:‘In cement producing activities, CO2emissions result from the following emission sources and source streams:’.

(1) | The title of Annex VIII is replaced by the following:‘Activity-specific guidelines for the production of lime or calcination of dolomite or magnesite as listed in Annex I to Directive 2003/87/EC’;
(2) | Section 2 is amended as follows:(a)in the first paragraph, the introductory phrase is replaced as follows: ‘In the production of lime or calcination of dolomite or magnesite, CO2emissions result from the following emission sources and source streams:’;(b)in the first paragraph, first indent, the wording is replaced as follows: ‘calcination of limestone, dolomite or magnesite in the raw materials’;(c)under subsection 2.1.1, Combustion Emissions, the wording is replaced as follows: ‘Combustion processes involving different types of fuels (e.g. coal, petcoke, fuel oil, natural gas and the broad range of waste fuels) that take place at installations for the production of lime or calcination of dolomite or magnesite shall be monitored and reported in accordance with Annex II.’;(d)under subsection 2.1.2, Process Emissions, first paragraph, the wording is replaced as follows: ‘Relevant emissions occur during calcination and from the oxidation of organic carbon in the raw materials. During calcination in the kiln, CO2from carbonates is released from the raw materials. Calcination CO2is directly linked with the lime, dolime or magnesia production. On an installation level, calcination CO2can be calculated in two ways: based on the amount of calcium and magnesium carbonate from the raw material (mainly limestone, dolomite and magnesite) converted in the process (calculation method A), or based on the amount of calcium and magnesium oxides in the products (calculation method B). The two approaches are considered to be equivalent and can be mutually used by the operator to validate the results of the respective other method’;(e)under subsection 2.1.2, ‘Calculation Method A: Carbonates’, the introductory phrase is replaced as follows: ‘Calculation shall be based on the amount of calcium carbonate and magnesium carbonate – and where relevant, of other carbonates – in the raw materials consumed. The following formula shall be used:’;(f)under subsection 2.1.2(b), the following sentence is inserted at the end of the first paragraph: ‘Where relevant, carbonate content values shall be adjusted for the respective moisture and gangue content of the applied carbonate material, and take into account other magnesium bearing minerals than carbonates.’;(g)‘Table 1: Stoichiometric ratios’ is replaced by the following:‘CarbonateRatio[t CO2/t Ca-, Mg- or other Carbonate]RemarksCaCO30,440MgCO30,522general: XY(CO3)ZEmission factor = [MCO2]/{Y * [Mx] + Z * [MCO32-]}X= alkali earth or alkali metalMx= molecular weight of X in [g/mol]MCO2= molecular weight of CO2= 44 [g/mol]MCO3-= molecular weight of CO32-= 60 [g/mol]Y= stoichiometric number of X= 1 (for alkali earth metals)= 2 (for alkali metals)Z=stoichiometric number of CO32-= 1’(h)under subsection 2.1.2, Calculation method B: Alkali Earth Oxides is replaced by the following: ‘CO2emissions arise from the calcination of carbonates and shall be calculated based on the amounts of CaO and MgO contents in the lime, dolime or magnesia produced. Already calcined Ca and Mg entering the kiln, for instance through fly ash or fuels and raw materials with a relevant CaO or MgO content, as well as other magnesium bearing minerals than carbonates shall be considered appropriately by means of the conversion factor. Kiln dust leaving the kiln system shall be considered appropriately.’;(i)‘Table 2: Stoichiometric ratios’ is replaced by the following:‘OxideStoichiometric ratiosRemarksCaO0,785 [tonne CO2per tonne of oxide]MgO1,092 [tonne CO2per tonne of oxide]general: XY(O)ZEmission factor = [MCO2]/{Y * [Mx] + Z * [MO]}X= alkali earth or alkali metalMx= molecular weight of X in [g/mol]MCO2= molecular weight of CO2= 44 [g/mol]MO= molecular weight of O = 16 [g/mol]Y= stoichiometric number of X= 1 (for alkali earth metals)= 2 (for alkali metals)Z=stoichiometric number of O = 1’ | (a) | in the first paragraph, the introductory phrase is replaced as follows: ‘In the production of lime or calcination of dolomite or magnesite, CO2emissions result from the following emission sources and source streams:’; | (b) | in the first paragraph, first indent, the wording is replaced as follows: ‘calcination of limestone, dolomite or magnesite in the raw materials’; | (c) | under subsection 2.1.1, Combustion Emissions, the wording is replaced as follows: ‘Combustion processes involving different types of fuels (e.g. coal, petcoke, fuel oil, natural gas and the broad range of waste fuels) that take place at installations for the production of lime or calcination of dolomite or magnesite shall be monitored and reported in accordance with Annex II.’; | (d) | under subsection 2.1.2, Process Emissions, first paragraph, the wording is replaced as follows: ‘Relevant emissions occur during calcination and from the oxidation of organic carbon in the raw materials. During calcination in the kiln, CO2from carbonates is released from the raw materials. Calcination CO2is directly linked with the lime, dolime or magnesia production. On an installation level, calcination CO2can be calculated in two ways: based on the amount of calcium and magnesium carbonate from the raw material (mainly limestone, dolomite and magnesite) converted in the process (calculation method A), or based on the amount of calcium and magnesium oxides in the products (calculation method B). The two approaches are considered to be equivalent and can be mutually used by the operator to validate the results of the respective other method’; | (e) | under subsection 2.1.2, ‘Calculation Method A: Carbonates’, the introductory phrase is replaced as follows: ‘Calculation shall be based on the amount of calcium carbonate and magnesium carbonate – and where relevant, of other carbonates – in the raw materials consumed. The following formula shall be used:’; | (f) | under subsection 2.1.2(b), the following sentence is inserted at the end of the first paragraph: ‘Where relevant, carbonate content values shall be adjusted for the respective moisture and gangue content of the applied carbonate material, and take into account other magnesium bearing minerals than carbonates.’; | (g) | ‘Table 1: Stoichiometric ratios’ is replaced by the following:‘CarbonateRatio[t CO2/t Ca-, Mg- or other Carbonate]RemarksCaCO30,440MgCO30,522general: XY(CO3)ZEmission factor = [MCO2]/{Y * [Mx] + Z * [MCO32-]}X= alkali earth or alkali metalMx= molecular weight of X in [g/mol]MCO2= molecular weight of CO2= 44 [g/mol]MCO3-= molecular weight of CO32-= 60 [g/mol]Y= stoichiometric number of X= 1 (for alkali earth metals)= 2 (for alkali metals)Z=stoichiometric number of CO32-= 1’ | ‘Carbonate | Ratio[t CO2/t Ca-, Mg- or other Carbonate] | Remarks | CaCO3 | 0,440 | | MgCO3 | 0,522 | | general: XY(CO3)Z | Emission factor = [MCO2]/{Y * [Mx] + Z * [MCO32-]} | X= alkali earth or alkali metalMx= molecular weight of X in [g/mol]MCO2= molecular weight of CO2= 44 [g/mol]MCO3-= molecular weight of CO32-= 60 [g/mol]Y= stoichiometric number of X= 1 (for alkali earth metals)= 2 (for alkali metals)Z=stoichiometric number of CO32-= 1’ | (h) | under subsection 2.1.2, Calculation method B: Alkali Earth Oxides is replaced by the following: ‘CO2emissions arise from the calcination of carbonates and shall be calculated based on the amounts of CaO and MgO contents in the lime, dolime or magnesia produced. Already calcined Ca and Mg entering the kiln, for instance through fly ash or fuels and raw materials with a relevant CaO or MgO content, as well as other magnesium bearing minerals than carbonates shall be considered appropriately by means of the conversion factor. Kiln dust leaving the kiln system shall be considered appropriately.’; | (i) | ‘Table 2: Stoichiometric ratios’ is replaced by the following:‘OxideStoichiometric ratiosRemarksCaO0,785 [tonne CO2per tonne of oxide]MgO1,092 [tonne CO2per tonne of oxide]general: XY(O)ZEmission factor = [MCO2]/{Y * [Mx] + Z * [MO]}X= alkali earth or alkali metalMx= molecular weight of X in [g/mol]MCO2= molecular weight of CO2= 44 [g/mol]MO= molecular weight of O = 16 [g/mol]Y= stoichiometric number of X= 1 (for alkali earth metals)= 2 (for alkali metals)Z=stoichiometric number of O = 1’ | ‘Oxide | Stoichiometric ratios | Remarks | CaO | 0,785 [tonne CO2per tonne of oxide] | | MgO | 1,092 [tonne CO2per tonne of oxide] | | general: XY(O)Z | Emission factor = [MCO2]/{Y * [Mx] + Z * [MO]} | X= alkali earth or alkali metalMx= molecular weight of X in [g/mol]MCO2= molecular weight of CO2= 44 [g/mol]MO= molecular weight of O = 16 [g/mol]Y= stoichiometric number of X= 1 (for alkali earth metals)= 2 (for alkali metals)Z=stoichiometric number of O = 1’
(a) | in the first paragraph, the introductory phrase is replaced as follows: ‘In the production of lime or calcination of dolomite or magnesite, CO2emissions result from the following emission sources and source streams:’;
(b) | in the first paragraph, first indent, the wording is replaced as follows: ‘calcination of limestone, dolomite or magnesite in the raw materials’;
(c) | under subsection 2.1.1, Combustion Emissions, the wording is replaced as follows: ‘Combustion processes involving different types of fuels (e.g. coal, petcoke, fuel oil, natural gas and the broad range of waste fuels) that take place at installations for the production of lime or calcination of dolomite or magnesite shall be monitored and reported in accordance with Annex II.’;
(d) | under subsection 2.1.2, Process Emissions, first paragraph, the wording is replaced as follows: ‘Relevant emissions occur during calcination and from the oxidation of organic carbon in the raw materials. During calcination in the kiln, CO2from carbonates is released from the raw materials. Calcination CO2is directly linked with the lime, dolime or magnesia production. On an installation level, calcination CO2can be calculated in two ways: based on the amount of calcium and magnesium carbonate from the raw material (mainly limestone, dolomite and magnesite) converted in the process (calculation method A), or based on the amount of calcium and magnesium oxides in the products (calculation method B). The two approaches are considered to be equivalent and can be mutually used by the operator to validate the results of the respective other method’;
(e) | under subsection 2.1.2, ‘Calculation Method A: Carbonates’, the introductory phrase is replaced as follows: ‘Calculation shall be based on the amount of calcium carbonate and magnesium carbonate – and where relevant, of other carbonates – in the raw materials consumed. The following formula shall be used:’;
(f) | under subsection 2.1.2(b), the following sentence is inserted at the end of the first paragraph: ‘Where relevant, carbonate content values shall be adjusted for the respective moisture and gangue content of the applied carbonate material, and take into account other magnesium bearing minerals than carbonates.’;
(g) | ‘Table 1: Stoichiometric ratios’ is replaced by the following:‘CarbonateRatio[t CO2/t Ca-, Mg- or other Carbonate]RemarksCaCO30,440MgCO30,522general: XY(CO3)ZEmission factor = [MCO2]/{Y * [Mx] + Z * [MCO32-]}X= alkali earth or alkali metalMx= molecular weight of X in [g/mol]MCO2= molecular weight of CO2= 44 [g/mol]MCO3-= molecular weight of CO32-= 60 [g/mol]Y= stoichiometric number of X= 1 (for alkali earth metals)= 2 (for alkali metals)Z=stoichiometric number of CO32-= 1’ | ‘Carbonate | Ratio[t CO2/t Ca-, Mg- or other Carbonate] | Remarks | CaCO3 | 0,440 | | MgCO3 | 0,522 | | general: XY(CO3)Z | Emission factor = [MCO2]/{Y * [Mx] + Z * [MCO32-]} | X= alkali earth or alkali metalMx= molecular weight of X in [g/mol]MCO2= molecular weight of CO2= 44 [g/mol]MCO3-= molecular weight of CO32-= 60 [g/mol]Y= stoichiometric number of X= 1 (for alkali earth metals)= 2 (for alkali metals)Z=stoichiometric number of CO32-= 1’
‘Carbonate | Ratio[t CO2/t Ca-, Mg- or other Carbonate] | Remarks
CaCO3 | 0,440 |
MgCO3 | 0,522 |
general: XY(CO3)Z | Emission factor = [MCO2]/{Y * [Mx] + Z * [MCO32-]} | X= alkali earth or alkali metalMx= molecular weight of X in [g/mol]MCO2= molecular weight of CO2= 44 [g/mol]MCO3-= molecular weight of CO32-= 60 [g/mol]Y= stoichiometric number of X= 1 (for alkali earth metals)= 2 (for alkali metals)Z=stoichiometric number of CO32-= 1’
(h) | under subsection 2.1.2, Calculation method B: Alkali Earth Oxides is replaced by the following: ‘CO2emissions arise from the calcination of carbonates and shall be calculated based on the amounts of CaO and MgO contents in the lime, dolime or magnesia produced. Already calcined Ca and Mg entering the kiln, for instance through fly ash or fuels and raw materials with a relevant CaO or MgO content, as well as other magnesium bearing minerals than carbonates shall be considered appropriately by means of the conversion factor. Kiln dust leaving the kiln system shall be considered appropriately.’;
(i) | ‘Table 2: Stoichiometric ratios’ is replaced by the following:‘OxideStoichiometric ratiosRemarksCaO0,785 [tonne CO2per tonne of oxide]MgO1,092 [tonne CO2per tonne of oxide]general: XY(O)ZEmission factor = [MCO2]/{Y * [Mx] + Z * [MO]}X= alkali earth or alkali metalMx= molecular weight of X in [g/mol]MCO2= molecular weight of CO2= 44 [g/mol]MO= molecular weight of O = 16 [g/mol]Y= stoichiometric number of X= 1 (for alkali earth metals)= 2 (for alkali metals)Z=stoichiometric number of O = 1’ | ‘Oxide | Stoichiometric ratios | Remarks | CaO | 0,785 [tonne CO2per tonne of oxide] | | MgO | 1,092 [tonne CO2per tonne of oxide] | | general: XY(O)Z | Emission factor = [MCO2]/{Y * [Mx] + Z * [MO]} | X= alkali earth or alkali metalMx= molecular weight of X in [g/mol]MCO2= molecular weight of CO2= 44 [g/mol]MO= molecular weight of O = 16 [g/mol]Y= stoichiometric number of X= 1 (for alkali earth metals)= 2 (for alkali metals)Z=stoichiometric number of O = 1’
‘Oxide | Stoichiometric ratios | Remarks
CaO | 0,785 [tonne CO2per tonne of oxide] |
MgO | 1,092 [tonne CO2per tonne of oxide] |
general: XY(O)Z | Emission factor = [MCO2]/{Y * [Mx] + Z * [MO]} | X= alkali earth or alkali metalMx= molecular weight of X in [g/mol]MCO2= molecular weight of CO2= 44 [g/mol]MO= molecular weight of O = 16 [g/mol]Y= stoichiometric number of X= 1 (for alkali earth metals)= 2 (for alkali metals)Z=stoichiometric number of O = 1’

(1) | the title of Annex IX is replaced by the following:‘Activity-specific guidelines for the manufacture of glass or mineral wool insulation material as listed in Annex I to Directive 2003/87/EC’;
(2) | Section 2 is amended as following:(a)the introductory phrase is replaced by the following:‘In the production of glass or mineral wool, CO2emissions result from the following emission sources and source streams:’;(b)subsection 2.1.1, is replaced by the following:‘2.1.1.COMBUSTION EMISSIONSCombustion processes that take place in installations for the manufacture of glass or mineral wool shall be monitored and reported in accordance with Annex II. This includes emissions from carbon containing additives (coke and coal dust, organic coatings of glass fibres and mineral wool) and flue gas cleaning (post-combustion).’;(c)the second paragraph of subsection 2.1.2, is replaced by the following:‘CO2from carbonates in the raw materials released during melting in the furnace is directly linked with the glass or mineral wool production and shall be calculated based on the converted quantity of carbonates from raw material – mainly soda, lime/limestone, dolomite and other alkali and alkali earth carbonates supplemented by carbonate free recycled glass (cullet).’. | (a) | the introductory phrase is replaced by the following:‘In the production of glass or mineral wool, CO2emissions result from the following emission sources and source streams:’; | (b) | subsection 2.1.1, is replaced by the following:‘2.1.1.COMBUSTION EMISSIONSCombustion processes that take place in installations for the manufacture of glass or mineral wool shall be monitored and reported in accordance with Annex II. This includes emissions from carbon containing additives (coke and coal dust, organic coatings of glass fibres and mineral wool) and flue gas cleaning (post-combustion).’; | (c) | the second paragraph of subsection 2.1.2, is replaced by the following:‘CO2from carbonates in the raw materials released during melting in the furnace is directly linked with the glass or mineral wool production and shall be calculated based on the converted quantity of carbonates from raw material – mainly soda, lime/limestone, dolomite and other alkali and alkali earth carbonates supplemented by carbonate free recycled glass (cullet).’.
(a) | the introductory phrase is replaced by the following:‘In the production of glass or mineral wool, CO2emissions result from the following emission sources and source streams:’;
(b) | subsection 2.1.1, is replaced by the following:‘2.1.1.COMBUSTION EMISSIONSCombustion processes that take place in installations for the manufacture of glass or mineral wool shall be monitored and reported in accordance with Annex II. This includes emissions from carbon containing additives (coke and coal dust, organic coatings of glass fibres and mineral wool) and flue gas cleaning (post-combustion).’;
(c) | the second paragraph of subsection 2.1.2, is replaced by the following:‘CO2from carbonates in the raw materials released during melting in the furnace is directly linked with the glass or mineral wool production and shall be calculated based on the converted quantity of carbonates from raw material – mainly soda, lime/limestone, dolomite and other alkali and alkali earth carbonates supplemented by carbonate free recycled glass (cullet).’.

(1) | the title of Annex X is replaced by the following:‘Activity-specific guidelines for the manufacture of ceramic products as listed in Annex I to Directive 2003/87/EC’;
(2) | in the first line of Section 2 the wording ‘installations for’ is deleted.

‘
Activity-specific guidelines for pulp and paper production as listed in Annex I to Directive 2003/87/EC
’

‘
Guidelines for determination of emissions or amount of transfer of greenhouse gases by continuous measurement systems
’

‘ANNEX XIX
Activity-specific guidelines for the production of soda ash and sodium bicarbonate as listed in Annex I to Directive 2003/87/EC 1. BOUNDARIES AND COMPLETENESS
The activity-specific guidelines in this Annex shall be applied for emissions from installations for the production of soda ash and sodium bicarbonate as listed in Annex I to Directive 2003/87/EC. 2. DETERMINATION OF CO2 EMISSIONS
In installations for the production of soda ash and sodium bicarbonate emission sources and source streams for CO2 emissions include:
—
fuels used for combustion processes, e.g. with the purpose of producing hot water or steam,
—
raw materials (e.g. vent gas from calcination of limestone, to the extent it is not used for carbonation),
—
waste gases from washing or filtration steps after carbonation, to the extent they are not used for carbonation.
2.1. CALCULATION OF CO2 EMISSIONS
As soda ash and sodium bicarbonate contain carbon stemming from the process inputs, the calculation of process emissions shall be based on a mass balance approach pursuant to Section 2.1.1. Emissions from the combustion of fuels can either be monitored separately pursuant to Section 2.1.2 or be taken into account in the mass balance approach.
2.1.1. MASS-BALANCE APPROACH
The mass-balance approach shall consider all carbon in inputs, stocks, products and other exports from the installation to determine the level of emissions of greenhouse gases over the reporting period, except for emission sources monitored in accordance with Section 2.1.2 of this Annex. The amount of CO2 used for producing sodium bicarbonate from soda ash shall be considered as emitted. The following equation shall be used:
CO2 emissions [t CO2] = (input – products – export – stock changes) * conversion factor CO2/C
With:
— input [t C]: all carbon entering the boundaries of the installation,
— products [t C]: all carbon in products (1) and materials, including by-products, leaving the boundaries of the installation,
— export [t C]: carbon exported from the boundaries of the installation in liquid and/or solid phases, e.g. discharged to sewer, deposited into landfill or through losses. Export does not include the release of greenhouse gases or carbon monoxide into the atmosphere,
— stock changes [t C]: stock increases of carbon within the boundaries of the mass balance.
The calculation shall then be as follows:
CO2 emissions [t CO2] = (Σ (activity datainput * carbon contentinput) – Σ (activity dataproducts * carbon contentproducts) – Σ (activity dataexport * carbon contentexport) – Σ (activity datastock changes * carbon contentstock changes)) * 3,664
With:
(a)
activity data
The operator shall analyse and report the mass flows into and from the installation and respective stock changes for all relevant fuels and materials separately. Where the carbon content of a mass flow is usually related to energy content (fuels), the operator may determine and use the carbon content related to the energy content [t C/TJ] of the respective mass flow for the calculation of the mass balance.
Tier 1
Activity data over the reporting period are determined with a maximum uncertainty of less than ± 7,5 %.
Tier 2
Activity data over the reporting period are determined with a maximum uncertainty of less than ± 5 %.
Tier 3
Activity data over the reporting period are determined with a maximum uncertainty of less than ± 2,5 %.
Tier 4
Activity data over the reporting period are determined with a maximum uncertainty of less than ± 1,5 %.
(b)
carbon content
Tier 1
The carbon content of input or output streams is derived from reference emission factors for fuels or materials named in Section 11 of Annex I or in other activity-specific Annexes to these Guidelines. The carbon content is derived as follows:
C content [t/t or TJ] = Emission factor [t CO2/t or TJ]/3,664 [t CO2/t C]
Tier 2
The operator applies country-specific carbon content for the respective fuel or material as reported by the respective Member State in its latest national inventory submitted to the Secretariat of the United Nations Framework Convention on Climate Change.
Tier 3
The carbon content of input or output stream shall be derived following the provisions of Section 13 of Annex I in respect to representative sampling of fuels, products and by-products, the determination of their carbon contents and biomass fraction.
2.1.2. COMBUSTION EMISSIONS
Emissions from combustion of fuels shall be monitored and reported in accordance with Annex II, unless they are taken into account in the mass balance under Section 2.1.1. 2.2. MEASUREMENT OF CO2 EMISSIONS
The measurement guidelines contained in Annexes I and XII shall be applied.

(1) For the purpose of this mass balance all sodium bicarbonate produced from soda ash shall be treated as soda ash.’

‘ANNEX XX
Activity-specific guidelines for the production of ammonia as listed in Annex I to Directive 2003/87/EC 1. BOUNDARIES AND COMPLETENESS
The activity-specific guidelines contained in this Annex shall be used to monitor emissions from installations producing ammonia as listed in Annex I to Directive 2003/87/EC.
Ammonia production installations can be part of integrated installations in the chemical or refinery industry causing an intensive energy and material exchange. CO2 emissions may occur from combustion of fuels as well as from fuels used as process input for the production of ammonia. In a number of ammonia producing installations CO2 resulting from the production process is captured and used for other production processes, e.g. for the production of urea. Such captured CO2 shall be accounted for as emitted. 2. DETERMINATION OF CO2 EMISSIONS
In installations for the production of ammonia, CO2 emissions result from the following emission sources and source streams:
—
combustion of fuels supplying the heat for reforming or partial oxidation,
—
fuels used as process input in the ammonia production process (reforming or partial oxidation),
—
fuels used for other combustion processes, e.g. with the purpose of producing hot water or steam.
2.1. CALCULATION OF CO2 EMISSIONS
2.1.1. COMBUSTION EMISSIONS
Emissions from combustion of fuels not used as process input shall be monitored and reported in accordance with Annex II.
2.1.2. EMISSIONS FROM FUEL USED AS PROCESS INPUT FOR AMMONIA PRODUCTION
Emissions from fuel used as process input shall be monitored and reported in accordance with Annex II.
2.2. MEASUREMENT OF CO2 EMISSIONS
The measurement guidelines contained in Annexes I and XII shall be applied.’

‘ANNEX XXI
Activity-specific guidelines for the production of hydrogen and synthesis gas as listed in Annex I to Directive 2003/87/EC 1. BOUNDARIES AND COMPLETENESS
The activity-specific guidelines contained in this Annex shall be used to monitor emissions from installations producing hydrogen or synthesis gas as listed in Annex I to Directive 2003/87/EC. Where hydrogen production is technically integrated in a mineral oil refinery, the operator of such installation shall use the relevant provisions of Annex III instead.
Installations for the production of hydrogen or synthesis gas can be part of integrated installations in the chemical or refinery industry causing an intensive energy and material exchange. CO2 emissions may occur from combustion of fuels as well as from fuels used as process input. 2. DETERMINATION OF CO2 EMISSIONS
In installations for the production of hydrogen or synthesis gas, CO2 emissions result from the following emission sources and source streams:
—
fuels used in the hydrogen or synthesis gas production process (reforming or partial oxidation),
—
fuels used for other combustion processes, e.g. with the purpose of producing hot water or steam.
2.1. CALCULATION OF CO2 EMISSIONS
2.1.1. COMBUSTION EMISSIONS
Emissions from combustion of fuels not used as process input for the production of hydrogen or synthesis gas production, but for other combustion processes shall be monitored and reported in accordance with Annex II.
2.1.2. EMISSIONS FROM FUEL USED AS PROCESS INPUT
Emissions from fuels used as process input in hydrogen production shall be calculated using the input-related methodology laid down under Section 2.1.2.1. For synthesis gas production a mass balance as under Section 2.1.2.2 shall be used. Where hydrogen and synthesis gas are produced at the same installation, the operator may choose to calculate the respective emissions from both production processes using one mass balance according to Section 2.1.2.2. 2.1.2.1. HYDROGEN PRODUCTION
Emissions from fuel used as process input shall be calculated using the formula
CO2 emissions = activity data * emission factor
where
—
activity data is expressed as the net energy content of the fuel used as process input [TJ] or, when a mass or volume related emission factor is used, as the amount of fuel used as process input [t or Nm3],
—
emission factor is expressed as tonnes CO2/TJ or as tonnes CO2/t or as tonnes CO2/Nm3 of fuel used as process input.
The following tier requirements shall be applied:
(a)
Activity data
Activity data are generally expressed as the net energy content of the fuel used [TJ] during the reporting period. The energy content of the fuel used shall be calculated by means of the following formula:
Energy content of fuel used [TJ] = fuel used [t or Nm3] * net calorific value of fuel [TJ/t or TJ/Nm3]
In case a mass or volume related emission factor [t CO2/t or t CO2/Nm3] is used, activity data are expressed as the amount of fuel used [t or Nm3].
With:
(a1) Fuel used
Tier 1
Amount of fuel used as process input [t or Nm3] processed during the reporting period, derived with a maximum uncertainty of ± 7,5 %.
Tier 2
Amount of fuel used as process input [t or Nm3] processed during the reporting period, derived with a maximum uncertainty of ± 5,0 %.
Tier 3
Amount of fuel used as process input [t or Nm3] processed during the reporting period, derived with a maximum uncertainty of ± 2,5 %.
Tier 4
Amount of fuel used as process input [t or Nm3] processed during the reporting period, derived with a maximum uncertainty of ± 1,5 %.
(a2) Net calorific value
Tier 1
Reference values for each fuel are used as specified in Section 11 of Annex I.
Tier 2a
The operator applies country-specific net calorific values for the respective fuel as reported by the respective Member State in its latest national inventory submitted to the Secretariat of the United Nations Framework Convention on Climate Change.
Tier 2b
For commercially traded fuels the net calorific value as derived from the purchasing records for the respective fuel provided by the fuel supplier is used, provided it has been derived based on accepted national or international standards.
Tier 3
The net calorific value representative for the fuel in an installation is measured by the operator, a contracted laboratory or the fuel supplier in accordance with the provisions of Section 13 of Annex I.
(b)
Emission factor
Tier 1
The reference values listed in Section 11 of Annex I to these guidelines are used.
Tier 2a
The operator applies country specific emission factors for the respective fuel as reported by the respective Member State in its latest national inventory submitted to the Secretariat of the United Nations Framework Convention on Climate Change.
Tier 2b
The operator derives emission factors for the fuel based on one of the following established proxies:
—
density measurement of specific oils or gases common e.g. to the refinery or steel industry, and
—
net calorific value for specific coal types,
in combination with an empirical correlation as determined at least once per year according to the provisions of Section 13 of Annex I. The operator shall ensure that the correlation satisfies the requirements of good engineering practice and that it is applied only to values of the proxy which fall into the range for which it was established.
Tier 3
Use of an activity-specific emission factor [CO2/TJ or CO2/t or CO2/Nm3 feed] calculated from the carbon content of the fuel used, determined according to Section 13 of Annex I.
2.1.2.2. PRODUCTION OF SYNTHESIS GAS
As part of the carbon in the fuels used as process input is contained in the produced synthesis gas, a mass balance approach is to be used for the calculation of greenhouse gas emissions.
The mass-balance approach shall consider all carbon in inputs, stocks, products and other exports from the installation to determine the level of emissions of greenhouse gases over the reporting period, except for emission sources monitored in accordance with Section 2.1.1 and 2.1.2.1 of this Annex. The following equation shall be used:
CO2 emissions [t CO2] = (input – products – export – stock changes) * conversion factor CO2/C
With:
— input [t C]: all carbon entering the boundaries of the installation,
— products [t C]: all carbon in products and materials, including by-products, leaving the boundaries of the installation,
— export [t C]: carbon exported from the boundaries of the installation, e.g. discharged to sewer, deposited into landfill or through losses. Export does not include the release of greenhouse gases or carbon monoxide into the atmosphere,
— stock changes [t C]: stock increases of carbon within the boundaries of the mass balance.
The calculation shall then be as follows:
CO2 emissions [t CO2] = (Σ (activity datainput * carbon contentinput) – Σ (activity dataproducts * carbon contentproducts) – Σ (activity dataexport * carbon contentexport) – Σ (activity datastock changes * carbon contentstock changes)) * 3,664
With:
(a)
activity data
The operator shall analyse and report the mass flows into and from the installation and respective stock changes for all relevant fuels and materials separately. Where the carbon content of a mass flow is usually related to energy content (fuels), the operator may determine and use the carbon content related to the energy content [t C/TJ] of the respective mass flow for the calculation of the mass balance.
Tier 1
Activity data over the reporting period are determined with a maximum uncertainty of less than ± 7,5 %.
Tier 2
Activity data over the reporting period are determined with a maximum uncertainty of less than ± 5 %.
Tier 3
Activity data over the reporting period are determined with a maximum uncertainty of less than ± 2,5 %.
Tier 4
Activity data over the reporting period are determined with a maximum uncertainty of less than ± 1,5 %.
(b)
carbon content
Tier 1
The carbon content of input or output streams is derived from reference emission factors for fuels or materials named in Section 11 of Annex I or in other activity-specific Annexes to these Guidelines. The carbon content is derived as follows:
C content [t/t or TJ] = Emission factor [t CO2/t or TJ]/3,664 [t CO2/t C]
Tier 2
The operator applies country-specific carbon contents for the respective fuel or material as reported by the respective Member State in its latest national inventory submitted to the Secretariat of the United Nations Framework Convention on Climate Change.
Tier 3
The carbon content of input or output stream shall be derived following the provisions of Section 13 of Annex I in respect to representative sampling of fuels, products and by-products, the determination of their carbon contents and biomass fraction.
2.2. MEASUREMENT OF CO2 EMISSIONS
The measurement guidelines contained in Annexes I and XII shall be applied.’

‘ANNEX XXII
Activity-specific guidelines for the production of bulk organic chemicals as listed in Annex I to Directive 2003/87/EC 1. BOUNDARIES AND COMPLETENESS
The activity-specific guidelines contained in this Annex shall be used to monitor emissions from the production of bulk organic chemicals as listed in Annex I to Directive 2003/87/EC. Where such production is technically integrated in a mineral oil refinery, the operator of such installation shall use the relevant provisions of Annex III instead, especially for emissions from catalytic crackers.
Installations for the production of bulk organic chemicals can be part of integrated installations in the chemical or refinery industry causing an intensive energy and material exchange. CO2 emissions may occur from combustion of fuels as well as from fuels or materials used as process input. 2. DETERMINATION OF CO2 EMISSIONS
Potential emission sources for CO2 include fuels and input materials of the following processes:
—
cracking (catalytic and non-catalytic),
—
reforming,
—
partial or full oxidation,
—
similar processes which lead to CO2 emissions from carbon contained in hydrocarbon-based feedstock,
—
combustion of waste gases and flaring,
—
other combustion of fuel for supply of heat to the abovementioned processes.
2.1. CALCULATION OF CO2 EMISSIONS
In case of combustion processes where the fuels used do not take part in or stem from chemical reactions for the production of bulk organic chemicals, e.g. for generating process heat or electricity, the emissions shall be monitored and reported pursuant to Section 2.1.1. In all other cases the emissions from bulk organic chemicals production shall be calculated using a mass-balance approach laid down in Section 2.1.2. All CO in the flue gas shall be accounted for as CO2. Based on the approval of the competent authority, an input-based approach such as presented in Annex II, taking into account industry best practice can be used instead of a mass-balance approach if the operator can show that this is more cost-efficient and leads to a comparable accuracy level.
2.1.1. COMBUSTION EMISSIONS
Emissions from combustion processes shall be monitored and reported in accordance with Annex II. If waste gas scrubbing is carried out at the installation and the resulting emissions are not calculated using the mass balance pursuant to Section 2.1.2, they shall be calculated in accordance with Annex II.
2.1.2. MASS-BALANCE APPROACH
The mass-balance approach shall consider all carbon in inputs, stocks, products and other exports from the installation to account for the emissions of greenhouse gases, except for emission sources monitored in accordance with Section 2.1.1 of this Annex. The following equation shall be used:
Emissions [t CO2] = (input – products – export – stock changes) * conversion factor CO2/C
With:
— input [t C]: all carbon entering the boundaries of the installation,
— products [t C]: all carbon in products and materials, including by-products, leaving the boundaries of the installation,
— export [t C]: carbon exported from the boundaries of the installation, e.g. discharged to sewer, deposited into landfill or through losses. Export does not include the release of greenhouse gases or carbon monoxide into the atmosphere,
— stock changes [t C]: stock increases of carbon within the boundaries of the installation.
The calculation shall then be as follows:
CO2 emissions [t CO2] = (Σ (activity datainput * carbon contentinput) – Σ (activity dataproducts * carbon contentproducts) – Σ (activity dataexport * carbon contentexport) – Σ (activity datastock changes * carbon contentstock changes)) * 3,664
With:
(a)
Activity data
The operator shall analyse and report the mass flows into and from the installation and respective stock changes for all relevant fuels and materials separately. Where the carbon content of a mass flow is usually related to energy content (fuels), the operator may determine and use the carbon content related to the energy content [t C/TJ] of the respective mass flow for the calculation of the mass balance.
Tier 1
Activity data over the reporting period are determined with a maximum uncertainty of less than ± 7,5 %.
Tier 2
Activity data over the reporting period are determined with a maximum uncertainty of less than ± 5,0 %.
Tier 3
Activity data over the reporting period are determined with a maximum uncertainty of less than ± 2,5 %.
Tier 4
Activity data over the reporting period are determined with a maximum uncertainty of less than ± 1,5 %.
(b)
carbon content
Tier 1
The carbon content of input or output streams shall be derived from reference emission factors for fuels or materials listed in Section 11 of Annex I, in the Table below or in other activity-specific Annexes to these Guidelines. The carbon content is derived as follows:
C content [t/t or TJ] = Emission factor [t CO2/t or TJ]/3,664 [t CO2/t C]
For substances not listed in Section 11 of Annex I or in other activity-specific Annexes to these Guidelines, operators may calculate the carbon content from the stoichiometric carbon content in the pure substance and the concentration of the substance in the input or output stream.
Table
Reference Emission Factors
(1) Substance
Carbon content (t C/t feedstock or t C/t product)
Acetonitril
0,5852 t C/t
Acrylonitrile
0,6664 t C/t
Butadiene
0,888 t C/t
Carbon Black
0,97 t C/t
Ethylene
0,856 t C/t
Ethylene dichloride
0,245 t C/t
Ethylene glycol
0,387 t C/t
Ethylene oxide
0,545 t C/t
Hydrogen cyanide
0,4444 t C/t
Methanol
0,375 t C/t
Methane
0,749 t C/t
Propane
0,817 t C/t
Propylene
0,8563 t C/t
Vinyl chloride monomer
0,384 t C/t
Tier 2
The operator applies country-specific carbon content for the respective fuel or material as reported by the respective Member State in its latest national inventory submitted to the Secretariat of the United Nations Framework Convention on Climate Change.
Tier 3
The carbon content of input or output stream shall be derived following the provisions of Section 13 of Annex I in respect to representative sampling of fuels, products and by-products, the determination of their carbon contents and biomass fraction.
2.2. MEASUREMENT OF CO2 EMISSIONS
The measurement guidelines contained in Annexes I and XII shall be applied.’