natgillin/translations-raw huggingface dataset:
The operator shall include at least the following emission sources: boilers, burners, turbines, heaters, furnaces, incinerators, calciners, kilns, ovens, dryers, engines, fuel cells, chemical looping combustion units, flares, thermal or catalytic post-combustion units, and scrubbers (process emissions) and any other equipment or machinery that uses fuel, excluding equipment or machinery with combustion engines that are used for transportation purposes.
Procesi izgorevanja, ki potekajo v terminalih za predelavo plinov, se lahko spremljajo z masno bilanco v skladu s členom 25.
B. Specific monitoring rules
C. Čiščenje dimnih plinov
The emissions from combustion processes shall be calculated in accordance with Article 24(1), unless the fuels are included in a mass balance in accordance with Article 25.
Razžveplanje
The tiers defined in section 2 of Annex II shall apply.
Emisije iz proizvodnih procesov CO2 iz uporabe karbonata za čiščenje kislega plina po postopku iz toka dimnega plina se izračunajo v skladu s členom 24(2) na podlagi porabljenih karbonatov (metoda A v nadaljevanju) ali proizvedene sadre (metoda B v nadaljevanju).
In addition, process emissions from flue gas scrubbing shall be monitored using the provisions laid down in subsection C.
Z odstopanjem od oddelka 4 Priloge II velja:
For emissions from flares special requirements shall apply, as laid down in subsection D of this section.
Metoda A: Faktor emisije
Combustion processes taking place in gas processing terminals may be monitored using a mass balance in accordance with Article 25.
Stopnja 1: faktor emisije se določi na podlagi stehiometričnih razmerij, kot so opredeljena v oddelku 2 Priloge VI.
C. Flue gas scrubbing
Količine CaCO3 in MgCO3 ali drugih karbonatov v ustreznem vhodnem materialu se določijo na podlagi smernic za najboljšo industrijsko prakso.
Desulphurisation
Metoda B: Faktor emisije
Process CO2 emissions from the use of carbonate for acid gas scrubbing from the flue gas stream shall be calculated in accordance with Article 24(2) on the basis of carbonate consumed, Method A as follows, or gypsum produced, Method B as follows.
Stopnja 1: faktor emisije je stehiometrično razmerje suhe sadre (CaSO4 × 2H2O) in sproščenega CO2: 0,2558 t CO2/t sadre.
The following applies by way of derogation from section 4 of Annex II.
Faktor pretvorbe:
Method A: Emission factor
Z odstopanjem od oddelka 5 Priloge II se emisije CO2 iz proizvodnih procesov iz uporabe sečnine za čiščenje dimnih plinov po mokrem postopku izračunajo v skladu s členom 24(2) z uporabo stopenj, navedenih v nadaljevanju.
Tier 1: The emission factor shall be determined from stoichiometric ratios as laid down in section 2 of Annex VI.
Faktor emisije:
The determination of the amount of CaCO3 and MgCO3 or other carbonates in the relevant input material shall be carried out using industry best practice guidelines.
Stopnja 1: količine sečnine v ustreznem vhodnem materialu se določijo na podlagi smernic za najboljšo industrijsko prakso.
Method B: Emission factor
Faktor emisije se določi s stehiometričnim razmerjem 0,7328 t CO2/t sečnine.
Tier 1: The emission factor shall be the stoichiometric ratio of dry gypsum (CaSO4 × 2H2O) to CO2 emitted: 0,2558 t CO2/t gypsum.
Uporablja se samo stopnja 1.
Conversion Factor:
D. Naprave za sežiganje plinov
By way of derogation from section 5 of Annex II, process CO2 emissions from the use of urea for scrubbing of the flue gas stream shall be calculated in accordance with Article 24(2) applying the following tiers.
Upravljavec v izračun emisij iz sežiganja plinov vključi rutinsko in obratovalno sežiganje (izvrtine, zagon in zaustavitev ter tudi izredne posege).
Emission factor:
Upravljavec vključi tudi vsebovani CO2 v skladu s členom 48.
Tier 1: The determination of the amount of urea in the relevant input material shall be carried out using industry best practice guidelines.
Ne glede na oddelek 2.1 Priloge II se uporabita naslednji opredelitvi stopenj 1 in 2b za faktor emisije:
The emission factor shall be determined using a stoichiometric ratio of 0,7328 t CO2/t urea.
Stopnja 1: upravljavec uporabi referenčni faktor emisije 0,00393 t CO2/Nm3, izračunan iz izgorevanja čistega etana, uporabljen kot ohranitveni približek za sežgane pline.
Only tier 1 shall be applicable.
Stopnja 2b: faktorji emisije, specifični za napravo, se izpeljejo iz ocene molekulske mase toka sežiganja plinov s postopkom modeliranja, ki temelji na industrijsko standardiziranih modelih.
D. Flares
Ob upoštevanju sorazmernih deležev in molekularnih tež vsakega od prispevajočih tokov se za molekulsko maso sežganega plina izpelje tehtana letna povprečna vrednost.
When calculating emissions from flares the operator shall include routine flaring and operational flaring (trips, start-up and shutdown as well as emergency relieves).
Ne glede na oddelek 2.3 Priloge II se za faktor oksidacije za naprave za sežiganje plinov uporabita le stopnji 1 in 2.
The operator shall also include inherent CO2 in accordance with Article 48.
RAFINIRANJE MINERALNEGA OLJA IZ PRILOGE I K DIREKTIVI 2003/87/ES
By way of derogation from section 2.1 of Annex II, tiers 1 and 2b for the emission factor shall be defined as follows:
Upravljavec spremlja vse emisije CO2 iz procesov izgorevanja in proizvodnje, ki nastajajo v rafinerijah, ter poroča o njih.
Tier 1: The operator shall use a reference emission factor of 0,00393 t CO2/Nm3 derived from the combustion of pure ethane used as a conservative proxy for flare gases.
Upravljavec vključi vsaj naslednje možne vire emisij CO2: kotle, procesne grelnike/naprave za toplotno obdelavo/turbine, katalitične in toplotne oksidatorje, apnene peči za žganje koksa, gasilske črpalke, generatorje v sili/v pripravljenosti, naprave za sežiganje plinov, sežigalne naprave, naprave za kreking, enote za proizvodnjo vodika, procesne enote Claus, katalitsko regeneracijo (iz kreking procesov in drugih katalitskih procesov) in koksarne (fleksi koksanje, podaljšano koksanje).
Tier 2b: Installation-specific emission factors shall be derived from an estimate of the molecular weight of the flare stream, using process modelling based on industry standard models.
Spremljanje dejavnosti rafiniranja mineralnega olja se izvaja v skladu z oddelkom 1 te priloge za emisije iz izgorevanja, vključno s čiščenjem dimnih plinov.
By considering the relative proportions and the molecular weights of each of the contributing streams, a weighted annual average figure shall be derived for the molecular weight of the flare gas.
Upravljavec se lahko odloči, da za celotno rafinerijo ali posamezne procesne enote, kot so naprave za uplinjanje težkega olja ali naprave za sežiganje, uporabi metodologijo masne bilance v skladu s členom 25.
By way of derogation from section 2.3 of Annex II, only tiers 1 and 2 shall be applied for the oxidation factor in the case of flares.
Če se uporabljajo kombinacije standardne metodologije in masne bilance, upravljavec pristojnemu organu predloži dokaze, da so zadevne emisije popolne in da ni prišlo do dvojnega štetja emisij.
REFINING OF MINERAL OIL AS LISTED IN ANNEX I TO DIRECTIVE 2003/87/EC
Emisije iz posebnih enot za proizvodnjo vodika se spremljajo v skladu z oddelkom 19 te priloge.
The operator shall monitor and report all CO2 emissions from combustion and production processes as occurring in refineries.
Ne glede na člena 24 in 25 se emisije iz regeneracije katalizatorjev iz kreking procesov, drugih katalitskih regeneracij in fleksi koksarn spremljajo z masno bilanco, pri čemer se upošteva stanje vnosa zraka in dimnega plina.
The operator shall include at least the following potential sources of CO2 emissions: boilers, process heaters/treaters, internal combustion engines/turbines, catalytic and thermal oxidisers, coke calcining kilns, firewater pumps, emergency/standby generators, flares, incinerators, crackers, hydrogen production units, Claus process units, catalyst regeneration (from catalytic cracking and other catalytic processes) and cokers (flexi-coking, delayed coking).
Celoten CO v dimnem plinu se šteje kot CO2, pri čemer se uporabi masno razmerje: t CO2 = t CO * 1,571.
The monitoring of mineral oil refining activities shall be carried out in accordance with section 1 of this Annex for combustion emissions including flue gas scrubbing.
Analiza vnosa zraka in dimnih plinov ter izbira stopenj sta v skladu z določbami členov 32 do 35.
The operator may choose to use the mass balance methodology in accordance with Article 25 for the whole refinery or individual process units such as heavy oil gasification or calcinations plants.
Posebno metodologijo izračuna odobri pristojni organ.
Where combinations of standard methodology and mass balance are used, the operator shall provide evidence to the competent authority demonstrating the completeness of emissions covered, and that no double counting of emissions occurs.
PROIZVODNJA KOKSA IZ PRILOGE I K DIREKTIVI 2003/87/ES
Emissions from dedicated hydrogen production units shall be monitored in accordance with section 19 of this Annex.
Upravljavec vključi vsaj naslednje možne vire emisij CO2: surovine (vključno s premogom ali naftnim koksom), konvencionalna goriva (vključno z zemeljskim plinom), procesne pline (vključno s plavžnim plinom), druga goriva in čiščenje odpadnih plinov po mokrem postopku.
By way of derogation from Article 24 and 25, emissions from catalytic cracker regeneration, other catalyst regeneration and flexi-cokers shall be monitored using a mass balance, taking into account the state of the input air and the flue gas.
Upravljavec se lahko odloči, da za spremljanje emisij iz proizvodnje koksa uporabi masno bilanco v skladu s členom 25 in oddelkom 3 Priloge II ali standardno metodologijo v skladu s členom 24 ter oddelkoma 2 in 4 Priloge II.
All CO in the flue gas shall be accounted for as CO2, applying the mass relation: t CO2 = t CO * 1,571.
PRAŽENJE IN SINTRANJE KOVINSKIH RUD IZ PRILOGE I K DIREKTIVI 2003/87/ES
The analysis of input air and flue gases and the choice of tiers shall be in accordance with the provisions of Articles 32 to 35.
Upravljavec vključi vsaj naslednje možne vire emisij CO2: surovine (žganje apnenca, dolomita in karbonatnih železovih rud, vključno s FeCO3), konvencionalna goriva (vključno z zemeljskim plinom in koksom/koksovo žlindro), procesne pline (vključno s koksnim plinom in plavžnim plinom), procesne ostanke, uporabljene kot vhodni material, vključno s filtriranim prahom iz naprave za sintranje, konverterja in plavžne peči, druga goriva in čiščenje dimnih plinov.
The specific calculation methodology shall be approved by the competent authority.
Upravljavec se lahko odloči, da za spremljanje emisij iz praženja, sintranja ali peletiranja kovinskih rud uporabi masno bilanco v skladu s členom 25 in oddelkom 3 Priloge II ali standardno metodologijo v skladu s členom 24 ter oddelki 2, 4 in 5 Priloge II.
PRODUCTION OF COKE AS LISTED IN ANNEX I TO DIRECTIVE 2003/87/EC
PROIZVODNJA SUROVEGA ŽELEZA IN JEKLA IZ PRILOGE I K DIREKTIVI 2003/87/ES
The operator shall include at least the following potential sources of CO2 emissions: raw materials (including coal or petroleum coke), conventional fuels (including natural gas), process gases (including blast furnace gas – BFG), other fuels and waste gas scrubbing.
Upravljavec vključi vsaj naslednje možne vire emisij CO2: surovine (žganje apnenca, dolomita in karbonatnih železovih rud, vključno s FeCO3), konvencionalna goriva (zemeljski plin, premog in koks), reducente (vključno s koksom, premogom in plastiko), procesne pline (koksni plin, plavžni plin in plin v martinovki), porabo grafitnih elektrod, druga goriva in čiščenje odpadnih plinov po mokrem postopku.
For the monitoring of emissions from the production of coke, the operator may choose to use a mass balance in accordance with Article 25 and section 3 of Annex II, or the standard methodology in accordance with Article 24 and sections 2 and 4 of Annex II.
Upravljavec se lahko odloči, da za spremljanje emisij iz proizvodnje surovega železa in jekla uporabi masno bilanco v skladu s členom 25 in oddelkom 3 Priloge II ali standardno metodologijo v skladu s členom 24 ter oddelkoma 2 in 4 Priloge II, vsaj za del tokov vira, pri čemer se preprečijo vrzeli in dvojno štetje emisij.
METAL ORE ROASTING AND SINTERING AS LISTED IN ANNEX I TO DIRECTIVE 2003/87/EC
Z odstopanjem od oddelka 3.1 Priloge II se stopnja 3 za vsebnost ogljika opredeli na naslednji način:
The operator shall include at least the following potential sources of CO2 emissions: raw materials (calcination of limestone, dolomite and carbonatic iron ores, including FeCO3), conventional fuels (including natural gas and coke/coke breeze), process gases (including coke oven gas – COG, and blast furnace gas – BFG), process residues used as input material including filtered dust from the sintering plant, the converter and the blast furnace, other fuels and flue gas scrubbing.
Stopnja 3: upravljavec izračuna vsebnost ogljika vhodnega ali izhodnega toka v skladu s členi 32 do 35 glede na reprezentativno vzorčenje goriv, proizvodov in stranskih proizvodov, določanje njihove vsebnosti ogljika ter frakcije biomase.
For the monitoring of emissions from metal ore roasting, sintering or pelletisation, the operator may choose to use a mass balance in accordance with Article 25 and section 3 of Annex II or the standard methodology in accordance with Article 24 and sections 2, 4 and 5 of Annex II.
Upravljavec določi vsebnost ogljika v proizvodih ali polproizvodih na podlagi letnih analiz v skladu s členi 32 do 35 ali jo izračuna iz srednjeročnih vrednosti sestave, ki jih določajo ustrezni mednarodni ali nacionalni standardi.
PRODUCTION OF PIG IRON AND STEEL AS LISTED IN ANNEX I TO DIRECTIVE 2003/87/EC
PROIZVODNJA ALI PREDELAVA ŽELEZA IN JEKLA TER BARVNIH KOVIN IZ PRILOGE I K DIREKTIVI 2003/87/ES
The operator shall include at least the following potential sources of CO2 emissions: raw materials (calcination of limestone, dolomite and carbonatic iron ores, including FeCO3), conventional fuels (natural gas, coal and coke), reducing agents (including coke, coal and plastics), process gases (coke oven gas – COG, blast furnace gas – BFG and basic oxygen furnace gas – BOFG), consumption of graphite electrodes, other fuels and waste gas scrubbing.
Upravljavec ne uporablja določb iz tega oddelka za spremljanje emisij CO2 iz proizvodnje surovega železa in jekla ter primarnega aluminija in poročanje o njih.
For the monitoring of emissions from production of pig iron and steel, the operator may choose to use a mass balance in accordance with Article 25 and section 3 of Annex II, or the standard methodology in accordance with Article 24 and sections 2 and 4 of Annex II, at least for a part of the source streams, avoiding any gaps or double counting of emissions.
Upravljavec vključi vsaj naslednje možne vire emisij CO2: konvencionalna goriva; alternativna goriva, vključno z granuliranim plastičnim materialom iz naprav za obdelavo ostankov iz drobilnikov; reducenti, vključno s koksom, grafitne elektrode; surovine, vključno z apnencem in dolomitom; kovinske rude in koncentrate, ki vsebujejo ogljik, ter sekundarne polnitvene materiale.
By way of derogation from section 3.1 of Annex II, tier 3 for the carbon content is defined as follows:
Če ogljik iz goriv ali vhodnih materialov, ki se uporabljajo v tej napravi, ostane v proizvodih ali drugih izhodnih materialih pri proizvodnji, upravljavec uporabi masno bilanco v skladu s členom 25 in oddelkom 3 Priloge II.
Tier 3: The operator shall derive the carbon content of input or output stream following Articles 32 to 35 in respect to the representative sampling of fuels, products and by-products, the determination of their carbon contents and biomass fraction.
V nasprotnem primeru upravljavec izračuna emisije iz izgorevanja in emisije iz proizvodnih procesov ločeno s standardno metodologijo v skladu s členom 24 ter oddelkoma 2 in 4 Priloge II
The operator shall base the carbon content of products or semi-finished products on annual analyses following Articles 32 to 35 or derive the carbon content from mid-range composition values as specified by relevant international or national standards.
Če se uporabi masna bilanca, se lahko upravljavec odloči, da vključi emisije iz procesov izgorevanja v masni bilanci ali uporabi standardno metodologijo v skladu s členom 24 in oddelkom 1 te priloge za del tokov vira, pri čemer se preprečijo vrzeli in dvojno štetje emisij.
PRODUCTION OR PROCESSING OF FERROUS AND NON-FERROUS METALS AS LISTED IN ANNEX I TO DIRECTIVE 2003/87/EC
EMISIJE CO2 IZ PROIZVODNJE ALI PREDELAVE PRIMARNEGA ALUMINIJA IZ PRILOGE I K DIREKTIVI 2003/87/ES
The operator shall not apply the provisions in this section for the monitoring and reporting of CO2 emissions from the production of pig iron and steel and primary aluminium.
Upravljavec uporabi določbe iz tega oddelka za spremljanje emisij CO2 iz proizvodnje elektrod za taljenje primarnega aluminija, vključno s samostojnimi napravami za proizvodnjo takšnih elektrod, in porabo elektrod med elektrolizo ter poročanje o njih.
The operator shall consider at least the following potential emission sources for CO2 emissions: conventional fuels; alternative fuels including plastics granulated material from post shredder plants; reducing agents including coke, graphite electrodes; raw materials including limestone and dolomite; carbon containing metal ores and concentrates; and secondary feed materials.
Upravljavec vključi vsaj naslednje možne vire emisij CO2: goriva za proizvodnjo toplote ali pare, proizvodnjo elektrod, zmanjšanje Al2O3 med elektrolizo, ki je povezana s porabo elektrod, in uporabo natrijevega karbonata ali drugih karbonatov za čiščenje odpadnih plinov po mokrem postopku.
Where carbon stemming from fuels or input materials used at this installation remains in the products or other outputs of the production, the operator shall use a mass balance in accordance with Article 25 and section 3 of Annex II.
S tem povezane emisije perfluoriranih ogljikovodikov, ki izhajajo iz anodnih učinkov, vključno z ubežnimi emisijami, se spremljajo v skladu z oddelkom 8 te priloge.
Where this is not the case the operator shall calculate combustion and process emission separately using the standard methodology in accordance with Article 24 and sections 2 and 4 of Annex II.
Upravljavec določi emisije CO2 na podlagi proizvodnje ali predelave primarnega aluminija z uporabo metodologije masne bilance v skladu s členom 25.
Where a mass balance is used, the operator may choose to include emissions from combustion processes in the mass balance or to use the standard methodology in accordance with Article 24 and section 1 of this Annex for a part of the source streams, avoiding any gaps or double counting of emissions.
Pri metodologiji masne bilance se upošteva celoten ogljik v vhodnih materialih, zalogah, proizvodih ter ostalem izvozu iz mešanja, oblikovanja, žganja in recikliranja elektrod ter iz porabe elektrod pri elektrolizi.
EMISSIONS FROM PRODUCTION OR PROCESSING OF PRIMARY ALUMINIUM AS LISTED IN ANNEX I TO DIRECTIVE 2003/87/EC
Kadar se uporabijo predhodno žgane anode, se lahko uporabita masni bilanci za proizvodnjo posebej in porabo posebej ali ena skupna masna bilanca, pri kateri se upoštevata proizvodnja in poraba elektrod.
The operator shall apply the provisions of this section to the monitoring and reporting of CO2 emissions from the production of electrodes for primary aluminium smelting, including stand-alone plants for the production of such electrodes, and the consumption of electrodes during electrolysis.
Pri Søderbergovih obratih s celično tehnologijo upravljavec uporabi eno samo skupno masno bilanco.
The operator shall consider at least the following potential sources for CO2 emissions: fuels for the production of heat or steam, electrode production, reduction of Al2O3 during electrolysis which is related to electrode consumption, and use of soda ash or other carbonates for waste gas scrubbing.
Upravljavec se lahko odloči, da emisije iz procesov izgorevanja goriv vključi v masno bilanco ali da zanje uporabi standardno metodologijo v skladu s členom 24 in oddelkom 1 te priloge vsaj za del tokov vira, pri čemer se preprečijo vrzeli in dvojno štetje emisij.
The associated emissions of perfluorocarbons – PFCs, resulting from anode effects, including fugitive emissions, shall be monitored in accordance with section 8 of this Annex.
EMISIJE PERFLUORIRANIH OGLJIKOVODIKOV (PFC) IZ PROIZVODNJE ALI PREDELAVE PRIMARNEGA ALUMINIJA IZ PRILOGE I K DIREKTIVI 2003/87/ES
The operator shall determine CO2 emissions from the production or processing of primary aluminium using the mass balance methodology in accordance with Article 25.
Upravljavec uporabi naslednje za emisije perfluoriranih ogljikovodikov (PFC), ki izhajajo iz anodnih učinkov, vključno z ubežnimi emisijami PFC.
The mass balance methodology shall consider all carbon in inputs, stocks, products and other exports from the mixing, forming, baking and recycling of electrodes as well as from electrode consumption in electrolysis.
Upravljavec za emisije CO2, povezane s tem, vključno z emisijami iz proizvodnje elektrod, uporabi oddelek 7 te priloge.
Where pre-baked anodes are used, either separate mass balances for production and consumption may be applied, or one common mass balance taking into account both production and consumption of electrodes.
Upravljavec izračuna tudi emisije, ki niso povezane z anodnimi učinki, na podlagi metod ocenjevanja v skladu z najboljšo industrijsko prakso ter smernicami, ki jih v ta namen objavi Komisija.
In the case of Søderberg cells, the operator shall use one common mass balance.
B. Določanje emisij PFC
For emissions from combustion processes the operator may choose to include them in the mass balance or to use the standard methodology in accordance with Article 24 and section 1 of this Annex at least for a part of the source streams, avoiding any gaps or double counting of emissions.
Emisije PFC se izračunajo iz emisij, ki se lahko izmerijo v vodu ali odvodniku („emisije točkovnega vira“), in iz ubežnih emisij, pri čemer se uporabi zbiralna učinkovitost voda:
PFC EMISSIONS FROM PRODUCTION OR PROCESSING OF PRIMARY ALUMINIUM AS LISTED IN ANNEX I TO DIRECTIVE 2003/87/EC
emisije PFC (skupaj) = emisije PFC (vod)/zbiralna učinkovitost.
The operator shall apply the following for emissions of perfluorocarbons (PFCs) resulting from anode effects including fugitive emissions of PFCs.
Zbiralna učinkovitost se izmeri, ko se določijo faktorji emisije, specifični za napravo.
For associated CO2 emissions, including emissions from electrode production, the operator shall apply section 7 of this Annex.
Za njeno določitev se uporabi najnovejša različica navodil, navedenih v Stopnji 3 oddelka 4.4.2.4 Smernic IPCC iz leta 2006.
The operator shall furthermore calculate PFC emissions not related to anode effects based on estimation methods in accordance with industry best practice, and any guidelines published by the Commission for this purpose.
Upravljavec izračuna emisije CF4 in C2F6, izpuščene iz voda ali odvodnika, na podlagi ene od naslednjih metod:
B. Determination of PFC emissions
metode A, če so zabeleženi anodni učinki na celico dnevno;
PFC emissions shall be calculated from the emissions measurable in a duct or stack (‘point source emissions’) as well as fugitive emissions using the collection efficiency of the duct:
metode B, če je zabeležena prenapetost anodnih učinkov.
PFC emissions (total) = PFC emissions (duct) / collection efficiency
Metoda izračuna A – Metoda smernega koeficienta („Slope method“)
The collection efficiency shall be measured when the installation-specific emission factors are determined.
Upravljavec za določanje emisij PFC uporabi naslednji enačbi:
For its determination the most recent version of the guidance mentioned under Tier 3 of section 4.4.2.4 of the 2006 IPCC Guidelines shall be used.
emisije CF4 [t] = AEM × (SEFCF4/1000) × PrAl
The operator shall calculate emissions of CF4 and C2F6 emitted through a duct or stack using one of the following methods:
emisije C2F6 [t] = emisije CF4 * FC2F6
Method A where the anode effect minutes per cell-day are recorded;
pri čemer je:
Method B where the anode effect overvoltage is recorded.
AEM = minute anodnih učinkov/celico dnevno;