natgillin/translations-raw huggingface dataset:
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).
Upravljavec vključi vsaj naslednje možne vire emisij CO2: kotle, procesne grelnike/naprave za toplotno obdelavo/turbine, katalitične in toplotne oksidante, 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).
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.
Spremljanje dejavnosti rafiniranja mineralnega olja se izvaja v skladu z oddelkom 1 te priloge za emisije iz izgorevanja, vključno s čiščenjem dimnih plinov.
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.
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.
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.
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.
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.
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.
All CO in the flue gas shall be accounted for as CO2, applying the mass relation: t CO2 = t CO * 1,571.
Celoten CO v dimnem plinu se šteje kot CO2, pri čemer se uporabi masno razmerje: t CO2 = t CO * 1,571.
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.
Analiza vnosa zraka in dimnih plinov ter izbira stopenj sta v skladu z določbami členov 32 do 35.
The specific calculation methodology shall be approved by the competent authority.
Posebno metodologijo izračuna odobri pristojni organ.
By way of derogation from Article 24, emissions from hydrogen production shall be calculated as activity data (expressed as tonnes of hydrocarbon feed) multiplied by the emission factor (expressed as t CO2/t feed).
Ne glede na člen 24 se emisije iz proizvodnje vodika izračunajo kot podatki o dejavnosti (izraženi v tonah polnitve ogljikovodika), pomnoženi s faktorjem emisije (izražen kot t CO2/t polnitve).
The following tiers are defined for the emission factor:
Naslednji stopnji sta opredeljeni za faktorje emisij:
Tier 1 The operator shall use a reference value of 2,9 t CO2 per tonne feed processed, conservatively based on ethane.
Stopnja 1 upravljavec uporabi referenčno vrednost 2,9 t CO2 na tono polnitve, predelane na podlagi etana.
Tier 2 The operator shall use an activity-specific emission factor calculated from the carbon content of the feed gas determined in accordance with Articles 32 to 35.
Stopnja 2 upravljavec uporabi faktor emisije, specifičen za dejavnost, izračunan iz vsebnosti ogljika v dovedenem plinu, določene v skladu s členi 32 do 35.
Production of coke as listed in Annex I to Directive 2003/87/EC
Proizvodnja koksa 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 (vključno s premogom ali petrolkoksom), konvencionalna goriva (vključno z zemeljskim plinom), procesne pline (vključno s plavžnim plinom), 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 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.
Metal ore roasting and sintering as listed in Annex I to Directive 2003/87/EC
Praženje in sintranje kovinskih rud 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 (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.
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 koksarniškim 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.
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 and 4 of Annex II.
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 oddelkoma 2 in 4 Priloge II.
Production of pig iron and steel 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 (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 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 (koksarniški 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 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 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.
By way of derogation from section 3.1 of Annex II, tier 3 for the carbon content is defined as follows:
Z odstopanjem od oddelka 3.1 Priloge II se stopnja 3 za vsebnost ogljika opredeli na naslednji način:
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.
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.
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.
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 or processing of ferrous and non-ferrous metals 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 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 ne uporablja določb iz tega oddelka za spremljanje emisij CO2 iz proizvodnje surovega železa in jekla ter primarnega aluminija in 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 upošteva vsaj naslednje možne vire emisij CO2: konvencionalna goriva, alternativna goriva, vključno z granuliranim plastičnim materialom iz naprav za obdelavo ostankov iz drobilnikov, reducente, vključno s koksom in grafitnimi elektrodami, surovine, vključno z apnencem in dolomitom, ogljik, ki vsebuje kovinske rude in koncentrate, ter sekundarne polnitvene materiale.
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.
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.
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.
V nasprotnem primeru upravljavec izračuna emisije iz izgorevanja in emisije iz proizvodnih postopkov ločeno s standardno metodologijo v skladu s členom 24 ter oddelkoma 2 in 4 Priloge II.
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.
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.
Emissions from production or processing of primary aluminium 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 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.
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 poročanje o njih.
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 upošteva 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.
The associated emissions of perfluorocarbons — PFCs, resulting from anode effects, including fugitive emissions, shall be monitored in accordance with section 8 of this Annex.
S tem povezane emisije perfluoriranih ogljikovodikov, ki izhajajo iz anodnih učinkov, vključno z ubežnimi emisijami, se spremljajo v skladu z oddelkom 8 te priloge.
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 določi emisije CO2 na podlagi proizvodnje ali predelave primarnega aluminija z uporabo metodologije masne bilance v skladu s členom 25.
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.
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.
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.
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.
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.
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.
PFC emissions from production or processing of primary aluminium as listed in Annex I to Directive 2003/87/EC
Emisije perfluoriranih ogljikovodikov (PFC) iz proizvodnje ali predelave primarnega aluminija iz Priloge I k Direktivi 2003/87/ES
The operator shall apply the following for emissions of perfluorocarbons (PFCs) resulting from anode effects including fugitive emissions of PFCs.
Upravljavec uporabi naslednje za emisije perfluoriranih ogljikovodikov (PFC), ki izhajajo iz anodnih učinkov, vključno z ubežnimi emisijami PFC.
For associated CO2 emissions, including emissions from electrode production, the operator shall apply section 7 of this Annex.
Upravljavec za emisije CO2, povezane s tem, vključno z emisijami iz proizvodnje elektrod, uporabi oddelek 7 te priloge.
B. Determination of PFC emissions
B. Določanje emisij PFC
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:
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 (total) = PFC emissions (duct)/collection efficiency
emisije PFC (skupaj) = emisije PFC (vod)/zbiralna učinkovitost.
The collection efficiency shall be measured when the installation-specific emission factors are determined.
Zbiralna učinkovitost se izmeri, ko se določijo faktorji emisije, specifični za napravo.
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.
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 calculate emissions of CF4 and C2F6 emitted through a duct or stack using one of the following methods:
Upravljavec izračuna emisije CF4 in C2F6, izpuščene iz voda ali odvodnika, na podlagi ene od naslednjih metod:
Method A where the anode effect minutes per cell-day are recorded;
metode A, če so zabeleženi anodni učinki na celico dnevno;
Method B where the anode effect overvoltage is recorded.
metode B, če je zabeležena prenapetost anodnih učinkov.
Calculation Method A —
Metoda izračuna A –
Slope Method
metoda smernega koeficienta
The operator shall use the following equations for determining PFC emissions:
Upravljavec za določanje emisij PFC uporabi naslednji enačbi:
emissions [t] = AEM × (SEFCF4/1000) × PrAl
emisij [t] = AEM × (SEFCF4/1000) × PrAl,
C2F6 emissions [t] = CF4 emissions * FC2F6
C2F6 emisij [t] = CF4 emisij * FC2F6,
AEM Anode effect minutes/cell-day;
AEM minute anodnih učinkov/celico dnevno;
Slope emission factor [(kg CF4/t Al produced)/(anode effect minutes/cell-day)].
faktor naraščanja emisij [(kg CF4/t proizvedenega Al)/(minute anodnih učinkov/celico dnevno)].
Where different cell-types are used, different SEF may be applied as appropriate;
Če se uporabijo različne vrste celic, se lahko ustrezno uporabijo različni faktorji SEF;
Annual production of primary Aluminium [t];
letna proizvodnja primarnega aluminija [t];
Weight fraction of C2F6 (t C2F6/t CF4).
masni delež C2F6 (t C2F6/t CF4).
The anode effect minutes per cell-day shall express the frequency of anode effects (number anode effects/cell-day) multiplied by the average duration of anode effects (anode effect minutes/occurrence):
Minute anodnih učinkov na celico dnevno izražajo frekvenco anodnih učinkov (število anodnih učinkov/celico dnevno), pomnoženo s povprečnim trajanjem anodnih učinkov (minute anodnih učinkov/pojav):
AEM = frequency × average duration
AEM = frekvenca × povprečno trajanje.
Emission factor The emission factor for CF4 (slope emission factor, SEFCF4) expresses the amount [kg] of CF4 emitted per tonne of aluminium produced per anode effect minute/cell-day.
Faktor emisije faktor emisije za CF4 (faktor naraščanja emisij, SEFCF4) izraža količino [kg] izpuščenega CF4 na tono proizvedenega aluminija na minute anodnih učinkov/celico dnevno.
The emission factor (weight fraction FC2F6) of C2F6 expresses the amount [t] of C2F6 emitted proportionate to the amount [t] of CF4 emitted.
Faktor emisije (masni delež FC2F6) C2F6 izraža količino [t] izpuščenega C2F6, sorazmernega s količino [t] izpuščenega CF4.
Tier 1 The operator shall use technology-specific emission factors from Table 1 of this section of Annex IV.
Stopnja 1 upravljavec uporabi faktorje emisije, specifične za tehnologije, iz preglednice 1 tega oddelka Priloge IV.
Tier 2 The operator shall use installation-specific emission factors for CF4 and C2F6 established through continuous or intermittent field measurements.
Stopnja 2 upravljavec uporabi faktorje emisije za CF4 in C2F6, specifične za napravo in določene z neprekinjenimi ali prekinjenimi meritvami na terenu.
For the determination of those emission factors the operator shall use the most recent version of the guidance mentioned under tier 3 of section 4.4.2.4 of the 2006 IPCC Guidelines [1].
Upravljavec za določitev teh faktorjev emisije uporabi najnovejšo različico navodil, navedenih v Stopnji 3 oddelka 4.4.2.4 Smernic IPCC iz leta 2006 [1].
The operator shall determine each emission factor with a maximum uncertainty of ± 15 %.
Upravljavec določi vsak faktor emisije z največjo možno negotovostjo ± 15 %.
The operator shall determine the emission factors at least every three years or earlier where necessary due to relevant changes at the installation.
Upravljavec določi faktorje emisije vsaj vsaka tri leta ali pogosteje, če je to potrebno zaradi ustreznih sprememb v napravi.
Relevant changes shall include a change in the distribution of anode effect duration, or a change in the control algorithm affecting the mix of the types of anode effects or the nature of the anode effect termination routine.
Ustrezne spremembe vključujejo spremembo v porazdelitvi trajanja anodnih učinkov ali spremembo v nadzornem algoritmu, ki vpliva na vrste anodnih učinkov ali naravo strategije za izničevanje anodnih učinkov.
Table 1: Technology-specific emission factors related to activity data for the slope method
Preglednica 1: Faktorji emisije, specifični za tehnologije, ki so povezani s podatki o dejavnosti za metodo smernega koeficienta
Emission factor for CF4 (SEFCF4)
Faktor emisije za CF4 (SEFCF4)
[(kg CF4/t Al)/(AE-Mins/cell-day)]
[(kg CF4/t Al)/(anodni učinki – min/celico dnevno)]
Emission factor for C2F6 (FC2F6)
Faktor emisije za C2F6 (FC2F6)
Calculation Method B —
Metoda izračuna B –
Overvoltage Method
prenapetostna metoda
Where the anode effect overvoltage is measured, the operator shall use the following equations for the determination of PFC emissions:
Če se izmeri prenapetost anodnega učinka, upravljavec za določitev emisij PFC uporabi naslednji enačbi:
emissions [t] = OVC × (AEO/CE) × PrAl × 0,001
emisij [t] = OVC × (AEO/CE)× PrAl × 0,001,
C2F6 emissions [t] = CF4 emissions × FC2F6
C2F6 emisij [t] = CF4 emisij × FC2F6,
OVC Overvoltage coefficient (‘emission factor’) expressed as kg CF4 per tonne of aluminium produced per mV overvoltage;
OVC koeficient prenapetosti („faktor emisije“), izražen v kg CF4 na tono proizvedenega aluminija na mV prenapetosti;
AEO Anode effect overvoltage per cell [mV] determined as the integral of (time × voltage above the target voltage) divided by the time (duration) of data collection;
AEO prenapetost anodnih učinkov na celico [mV], določena kot integral časa × napetosti nad ciljno napetostjo, deljen s časom (trajanjem) zbiranja podatkov;
CE Average current efficiency of aluminium production [%];
CE povprečna trenutna učinkovitost proizvodnje aluminija [%];
Weight fraction of C2F6 (t C2F6/t CF4);
masni delež C2F6 (t C2F6/t CF4).
Emission factor The emission factor for CF4 (‘overvoltage coefficient’ OVC) shall express the amount [kg] of CF4 emitted per tonne of aluminium produced per millivolt overvoltage [mV].
Faktor emisije faktor emisije za CF4 („koeficient prenapetosti“ OVC) izraža količino [kg] izpuščenega CF4 na tono proizvedenega aluminija na milivolt prenapetosti [mV].
The emission factor of C2F6 (weight fraction FC2F6) shall express the amount [t] of C2F6 emitted proportionate to the amount [t] of CF4 emitted.
Faktor emisije C2F6 (masni delež FC2F6) izraža količino [t] izpuščenega C2F6, sorazmernega s količino [t] izpuščenega CF4.