natgillin/translations-raw huggingface dataset:
For emissions from make-up chemicals, the following tier definitions for the emission factor shall apply:
Za emisije iz pripravkov kemikalij se uporabita naslednji opredelitvi stopenj za faktor emisije:
The purity of relevant input materials shall be determined by means of best industry practice.
Čistost zadevnih vhodnih materialov se določi na podlagi najboljše industrijske prakse.
The derived values shall be adjusted in accordance with the moisture and gangue content of the applied carbonate materials.
Dobljene vrednosti se prilagodijo v skladu z vlago in vsebnostjo jalovine v uporabljenih karbonatnih materialih.
Production of carbon black as listed in Annex I to Directive 2003/87/EC
Proizvodnja saj iz Priloge I k Direktivi 2003/87/ES
The operator shall include at least all fuels for combustion and all fuels used as process material as sources for CO2 emissions.
Upravljavec kot vire emisij CO2 vključi vsaj vsa goriva za izgorevanje in vsa goriva, ki se uporabljajo kot material v proizvodnem procesu.
The monitoring of emissions from carbon black production may be monitored either as a combustion process, including flue gas scrubbing, in accordance with section 1 of this Annex or using a mass balance in accordance with Article 25 and section 3 of Annex II.
Emisije iz proizvodnje saj se lahko spremljajo kot proces izgorevanja, vključno s čiščenjem dimnih plinov, v skladu z oddelkom 1 te priloge ali z uporabo masne bilance v skladu s členom 25 in oddelkom 3 Priloge II.
Determination of nitrous oxide (N2O) emissions from nitric acid, adipic acid, caprolactam, glyoxal and glyoxylic acid production as listed in Annex I to Directive 2003/87/EC
Določanje emisij dušikovega oksida (N2O) pri proizvodnji dušikove kisline, adipinske kisline, kaprolaktama, glioksala in glioksilne kisline iz Priloge I k Direktivi 2003/87/ES
Each operator shall consider for each activity from which N2O emissions result, all sources emitting N2O from production processes, including where N2O emissions from production are channelled through any abatement equipment.
Vsak upravljavec za vsako dejavnost, pri kateri nastajajo emisije N2O, upošteva vse vire emisij N2O v proizvodnih procesih, vključno s tistimi, pri katerih se emisije N2O usmerijo skozi opremo za zmanjševanje emisij.
This includes any of the following:
Med te spada kar koli od naslednjega:
nitric acid production N2O emissions from the catalytic oxidation of ammonia and/or from the NOx/N2O abatement units;
proizvodnja dušikove kisline emisije N2O pri katalitski oksidaciji amoniaka in/ali iz naprav za zmanjševanje emisij NOx/N2O
adipic acid production N2O emissions including from the oxidation reaction, any direct process venting and/or any emissions control equipment;
proizvodnja adipinske kisline emisije N2O, vključno z oksidacijskimi reakcijami, vsakim neposrednim izpustom med postopkom in/ali iz opreme za omejevanje emisij;
glyoxal and glyoxylic acid production N2O emissions including from the process reactions, any direct process venting and/or any emissions control equipment;
proizvodnja glioksala in glioksilne kisline emisije N2O, vključno s procesnimi reakcijami, vsakim neposrednim izpustom med postopkom in/ali iz opreme za omejevanje emisij;
caprolactam production N2O emissions including from the process reactions, any direct process venting and/or any emissions control equipment.
proizvodnja kaprolaktama emisije N2O, vključno s procesnimi reakcijami, vsakim neposrednim izpustom med postopkom in/ali iz opreme za omejevanje emisij.
These provisions shall not apply to any N2O emissions from the combustion of fuels.
Te določbe se ne uporabljajo za emisije N2O, ki nastajajo pri izgorevanju goriva.
B. Determination of N2O emissions
B. Določanje emisij N2O
Annual N2O emissions
B.1 Letne emisije N2O
The operator shall monitor emissions of N2O from nitric acid production using continuous emissions measurement.
Upravljavec spremlja emisije N2O pri proizvodnji dušikove kisline z neprekinjenim merjenjem emisij.
The operator shall monitor emissions of N2O from adipic acid, caprolactam, glyoxal and glyoxylic acid production using a measurement-based methodology for abated emissions and a calculation-based method (based on a mass balance methodology) for temporary occurrences of unabated emissions.
Upravljavec spremlja emisije N2O, ki nastanejo pri proizvodnji adipinske kisline, kaprolaktama, glioksala in glioksilne kisline, z metodologijo na podlagi meritev za zmanjšane emisije in metodo na podlagi izračuna (na podlagi metodologije masne bilance), kadar emisije začasno ostajajo nezmanjšane.
For each emission source where continuous emissions measurement is applied, the operator shall consider the total annual emissions to be the sum of all hourly emissions using the following formula:
Za vsak vir emisije, pri katerem se uporablja neprekinjeno merjenje emisij, upravljavec šteje, da so skupne letne emisije enake vsoti vseh urnih emisij, izračunani z naslednjo enačbo:
total annual emissions of N2O from the emission source in tonnes N2O
skupne letne emisije N2O iz zadevnega vira emisije v tonah N2O;
hourly concentrations of N2O in mg/Nm3 in the flue gas flow measured during operation
urne koncentracije N2O v mg/Nm3 v pretoku dimnega plina, izmerjene med delovanjem naprave;
Flue gas flow flue gas flow determined in Nm3/h for each hourly concentration
pretok dimnega plina pretok dimnega plina, določen v Nm3/h za vsako urno koncentracijo.
Hourly N2O emissions
B.2 Urne emisije N2O
The operator shall calculate annual average hourly N2O emissions for each source where continuous emission measurement is applied using the following equation:
Upravljavec letne povprečne urne emisije N2O za vsak vir, pri katerem se uporablja neprekinjeno merjenje emisije, izračuna z naslednjo enačbo:
annual average hourly N2O emissions in kg/h from the source;
letno povprečje urnih emisij N2O v kg/h iz vira;
hourly concentrations of N2O in mg/Nm3 in the flue gas flow measured during operation;
urne koncentracije N2O v mg/Nm3 v pretoku dimnega plina, izmerjene med delovanjem naprave;
Flue gas flow flue gas flow determined in Nm3/h for each hourly concentration.
pret. dim. plina pretok dimnega plina, določen v Nm3/h za vsako urno koncentracijo.
The operator shall determine hourly N2O concentrations [mg/Nm3] in the flue gas from each emission source using a measurement-based methodology at a representative point, after the NOx/N2O abatement equipment, where abatement is used.
Upravljavec določi urne koncentracije N2O [mg/Nm3] v dimnem plinu iz vsakega vira emisije z metodologijo na podlagi meritev na reprezentativni točki po izhodu iz opreme za zmanjševanje emisij NOx/N2O, kadar se ta uporablja.
The operator shall apply techniques capable of measuring N2O concentrations of all emission sources during both abated and unabated conditions.
Upravljavec uporabi tehnike, s katerimi je mogoče izmeriti koncentracije N2O vseh virov emisij v pogojih z zmanjšanimi emisijami in v pogojih z nezmanjšanimi emisijami.
Where uncertainties increase during such periods, the operator shall take them into account in the uncertainty assessment.
Če se med takšnimi obdobji negotovost poveča, upravljavec to upošteva v oceni negotovosti.
The operator shall adjust all measurements to a dry gas basis where required and report them consistently.
Upravljavec po potrebi vse meritve prilagodi glede na suhi plin in jih dosledno sporoča.
Determination of flue gas flow
B.3 Določanje pretoka dimnega plina
The operator shall use the methods for monitoring flue gas flow set out in Article 43(5) of this Regulation for measuring the flue gas flow for N2O emissions monitoring.
Upravljavec pri spremljanju emisij N2O za merjenje pretoka dimnega plina uporabi metode spremljanja pretoka dimnega plina iz člena 43(5) te uredbe.
For nitric acid production, the operator shall apply the method in accordance with point (a) of Article 43(5) unless it is technically not feasible.
Pri proizvodnji dušikove kisline upravljavec uporabi metodo v skladu s členom 43(5)(a), razen če ta tehnično ni izvedljiva.
In that case and upon approval by the competent authority, the operator shall apply an alternative method, including by a mass balance methodology based on significant parameters such as ammonia input load, or determination of flow by continuous emissions flow measurement.
V tem primeru in po odobritvi pristojnega organa upravljavec uporabi nadomestno metodo, vključno z metodologijo masne bilance, ki temelji na bistvenih parametrih, kot je vnos amoniaka ali določanje pretoka z neprekinjenim merjenjem pretoka emisij.
Total input air flow in Nm3/h at standard conditions;
skupni vnos pretoka zraka v Nm3/h pri standardnih pogojih;
Volume fraction of O2 in dry air [= 0,2095];
prostorninski delež O2 v suhem zraku [= 0,2095];
Volume fraction of O2 in the flue gas.
prostorninski delež O2 v dimnem plinu.
The operator shall apply the following formula, unless stated otherwise in its monitoring plan:
Če upravljavec v svojem načrtu za spremljanje ne navede drugače, uporablja naslednjo enačbo:
Primary input air flow in Nm3/h at standard conditions;
primarni vnos pretoka zraka v Nm3/h pri standardnih pogojih;
Secondary input air flow in Nm3/h at standard conditions;
sekundarni vnos pretoka zraka v Nm3/h pri standardnih pogojih;
Seal input air flow in Nm3/h at standard conditions.
zaporni vnos pretoka zraka v Nm3/h pri standardnih pogojih.
The operator shall determine Vprim by continuous flow measurement before the mixing with ammonia takes place.
Upravljavec določi Vprim z neprekinjenim merjenjem pretoka, preden se zrak pomeša z amoniakom.
The operator shall determine Vsec by continuous flow measurement, including where the measurement is before the heat recovery unit.
Upravljavec določi Vsek z neprekinjenim merjenjem pretoka, vključno z merjenjem pred enoto za rekuperacijo toplote.
For Vseal the operator shall consider the purged airflow within the nitric acid production process.
Pri Vzap upravljavec upošteva prečiščeni pretok zraka v postopku proizvodnje dušikove kisline.
For input air streams accounting for cumulatively less than 2,5 % of the total air flow, the competent authority may accept estimation methods for the determination of that air flow rate proposed by the operator based on industry best practices.
Za dovajani tok zraka, katerega skupni delež znaša manj kot 2,5 % celotnega pretoka zraka, lahko pristojni organ za določanje te stopnje zračnega pretoka sprejme metode ocenjevanja, ki jih upravljavec predlaga na podlagi najboljših industrijskih praks.
The operator shall provide evidence through measurements under normal operating conditions that the flue gas flow measured is sufficiently homogeneous to allow for the proposed measurement method.
Upravljavec na podlagi meritev v normalnih pogojih dokaže, da je izmerjeni pretok dimnega plina dovolj homogen, da omogoča uporabo predlagane merilne metode.
Where non-homogeneous flow is confirmed through these measurements, the operator shall take that into account when determining appropriate monitoring methods and when calculating the uncertainty in the N2O emissions.
Če te meritve pokažejo, da je pretok nehomogen, upravljavec to upošteva pri določanju ustreznih metod spremljanja in pri izračunu negotovosti emisij N2O.
The operator shall adjust all measurements to a dry gas basis and report them consistently.
Upravljavec vse meritve prilagodi glede na suhi plin in jih dosledno sporoča.
Oxygen (O2) concentrations
B.4 Koncentracije kisika (O2)
The operator shall measure the oxygen concentrations in the flue gas where necessary for calculating the flue gas flow in accordance with subsection B.3 of this section of Annex IV.
Upravljavec meri koncentracije kisika v dimnem plinu, kadar je to potrebno za izračun pretoka dimnega plina v skladu s pododdelkom B.3 tega oddelka Priloge IV.
In doing so, the operator shall comply with the requirements for concentration measurements within Article 41(1) and (2).
Pri tem upravljavec upošteva zahteve za meritve koncentracije iz člena 41(1) in (2).
In determining the uncertainty of N2O emissions, the operator shall take the uncertainty of O2 concentration measurements into account.
Pri določanju negotovosti emisij N2O upravljavec upošteva negotovost meritev koncentracij O2.
Calculation of N2O emissions
B.5 Izračun emisij N2O
For specific periods of unabated emissions of N2O from adipic acid, caprolactam, glyoxal and glyoxylic acid production, including unabated emissions from venting for safety reasons and when abatement plant fails, and where continuous emissions monitoring of N2O is technically not feasible, the operator shall subject to the approval of the specific methodology by the competent authority calculate N2O emissions using a mass balance methodology.
Kadar v določenih obdobjih emisije N2O, ki nastajajo pri proizvodnji adipinske kisline, kaprolaktama, glioksala in glioksilne kisline, ostajajo nezmanjšane, vključno z nezmanjšanimi emisijami zaradi zračenja iz varnostnih razlogov in v primeru izpada naprav za zmanjševanje emisij, ter kadar neprekinjeno spremljanje emisij N2O tehnično ni izvedljivo, upravljavec po tem, ko pristojni organ odobri določeno metodologijo, izračuna emisije N2O z uporabo metodologije masne bilance.
For this purpose the overall uncertainty shall be similar to the result of applying the tier requirements of Article 41(1) and (2).
Zato je splošna negotovost podobna rezultatu uporabe zahtev v zvezi s stopnjami iz člena 41(1) in (2).
The operator shall base the calculation method on the maximum potential emission rate of N2O from the chemical reaction taking place at the time and the period of the emission.
Metoda izračuna upravljavca temelji na največji možni stopnji emisij N2O pri kemični reakciji, ki poteka med nastajanjem emisije.
The operator shall take the uncertainty in any calculated emissions for a specific emission source into account in determining the annual average hourly uncertainty for the emission source.
Upravljavec pri določanju letne povprečne urne negotovosti vira emisije upošteva negotovost vseh emisij, izračunanih za posebni vir emisije.
Determination of activity production rates
B.6 Določanje stopenj proizvodnje, povezanih z dejavnostjo
Sampling rates
B.7 Stopnje vzorčenja
Valid hourly averages or averages for shorter reference periods shall be calculated in accordance with Article 44 for:
Veljavne urne povprečne vrednosti ali povprečne vrednosti za krajša referenčna obdobja se izračunajo v skladu s členom 44 za:
concentration of N2O in the flue gas;
koncentracijo N2O v dimnem plinu;
total flue gas flow where this is measured directly and where required;
skupni pretok dimnega plina, kadar se ta meri neposredno in se to zahteva;
C. Determination of annual CO2 equivalent — CO2(e)
C. Določanje letnega ekvivalenta CO2 – CO2(e)
The operator shall convert the total annual N2O emissions from all emissions sources, measured in tonnes to three decimal places, to annual CO2(e) in rounded tonnes, using the following formula and the GWP values in Annex VI, section 3:
Upravljavec pretvori skupne letne emisije N2O iz vseh virov emisij, izmerjene v tonah na tri decimalna mesta natančno, v letne emisije CO2(e), zaokroženo na tone, z naslednjo enačbo in vrednostmi potenciala globalnega segrevanja (GWP) iz oddelka 3 Priloge VI:
= N2Oannual[t] * GWPN2O
= N2Oletno[t] * GWPN2O
The total annual CO2(e) generated by all emission sources and any direct CO2 emissions from other emission sources included under the greenhouse gas permit shall be added to the total annual CO2 emissions generated by the installation and shall be used for reporting and surrendering allowances.
Skupna letna vrednost CO2(e) iz vseh virov emisij in morebitne neposredne emisije CO2 iz drugih virov emisij, vključene v dovoljenje za emisije toplogrednih plinov, se dodajo skupnim letnim emisijam CO2, ki nastajajo v napravi, ter se uporabijo pri poročanju in predaji pravic.
Total annual emissions of N2O shall be reported in tonnes to three decimal places and as CO2(e) in rounded tonnes.
Skupne letne emisije N2O so v poročilu navedene v tonah in zaokrožene na tri decimalna mesta natančno ter kot CO2(e), zaokroženo na tone.
Production of ammonia as listed in Annex I to Directive 2003/87/EC
Proizvodnja amoniaka iz Priloge I k Direktivi 2003/87/ES
The operator shall include at least the following potential emission sources for CO2 emissions: 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 including for the purpose of producing hot water or steam.
Upravljavec vključi vsaj naslednje možne vire emisij CO2: izgorevanje goriv za pridobivanje toplote za preoblikovanje ali delno oksidacijo, goriva, ki se uporabljajo kot vhodni material pri proizvodnem postopku amoniaka (preoblikovanje ali delna oksidacija) in goriva, ki se uporabljajo pri drugih procesih izgorevanja, vključno z namenom proizvodnje tople vode ali pare.
For monitoring of emissions from combustion processes and from fuels used as process inputs, the standard methodology in accordance with Article 24 and section 1 of this Annex shall be applied.
Za spremljanje emisij pri procesih izgorevanja in pri gorivih, ki se uporabljajo kot vhodni materiali pri proizvodnem postopku, se uporablja standardna metodologija v skladu s členom 24 in oddelkom 1 te priloge.
Where CO2 from ammonia production is used as feedstock for the production of urea or other chemicals, or transferred out of the installation for any use not covered by Article 49(1), the related amount of CO2 shall be considered as emitted by the installation producing the CO2.
Kadar se CO2, ki nastane pri proizvodnji amoniaka, uporablja kot surovina za proizvodnjo sečnine ali drugih kemikalij ali prenese iz naprave za uporabo, ki ni zajeta v členu 49(1), se ta količina CO2 šteje kot emisija naprave za proizvodnjo CO2.
Production of bulk organic chemicals as listed in Annex I to Directive 2003/87/EC
Proizvodnja osnovnih organskih kemikalij iz Priloge I k Direktivi 2003/87/ES
The operator shall take into account at least the following sources of CO2 emissions: 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, and the burning of fuel in other combustion processes.
Upravljavec upošteva vsaj naslednje vire emisij CO2: kreking (katalitski in nekatalitski), preoblikovanje, delno ali popolno oksidacijo, podobne procese, ki povzročajo emisije CO2 iz ogljika, vsebovanega v surovinah, ki temeljijo na ogljikovodikih, izgorevanje odpadnih plinov in sežig ter druge procese izgorevanja goriv.
Where the production of bulk organic chemicals is technically integrated in a mineral oil refinery, the operator of that installation shall apply the relevant provisions of section 2 of this Annex.
Kadar je proizvodnja osnovnih organskih kemikalij tehnično vključena v rafinerije mineralnih olj, upravljavec te naprave uporabi ustrezne določbe iz oddelka 2 te priloge.
Notwithstanding the first subparagraph, the operator shall monitor emissions from combustion processes where the fuels used do not take part in or stem from chemical reactions for the production of bulk organic chemicals using the standard methodology in accordance with Article 24 and section 1 of this Annex.
Ne glede na prvi pododstavek, upravljavec spremlja emisije pri postopkih izgorevanja, kadar uporabljena goriva niso del ali ne izhajajo iz kemijskih reakcij za proizvodnjo osnovnih organskih kemikalij z uporabo standardne metodologije v skladu s členom 24 in oddelkom 1 te priloge.
In all other cases, the operator may choose to monitor the emissions from bulk organic chemicals production by mass balance methodology in accordance with Article 25 or the standard methodology in accordance with Article 24.
V vseh drugih primerih se lahko upravljavec odloči za spremljanje emisij pri proizvodnji osnovnih organskih kemikalij z metodologijo masne bilance v skladu s členom 25 ali standardno metodologijo v skladu s členom 24.
Where using the standard methodology, the operator shall provide evidence to the competent authority that the chosen methodology covers all relevant emissions that would also be covered by a mass-balance methodology.
Kadar upravljavec uporablja standardno metodologijo, pristojnemu organu predloži dokaze, da izbrana metodologija vključuje vse ustrezne emisije, ki bi jih vključevala tudi metodologija masne bilance.
For the determination of the carbon content under Tier 1, the reference emission factors as listed in Table 5 in Annex VI shall be applied.
Za določanje vsebnosti ogljika v skladu s stopnjo 1 se uporabijo referenčni faktorji emisije iz preglednice 5 Priloge VI.
For substances not listed in Table 5 of Annex VI or other provisions of this Regulation, the operator shall 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.
Upravljavec za snovi, ki niso navedene v preglednici 5 Priloge VI ali drugih določbah te uredbe, izračuna vsebnost ogljika iz stehiometrične vsebnosti ogljika v čisti snovi in koncentracije snovi v vhodnem ali izhodnem toku.
Production of hydrogen and synthesis gas as listed in Annex I to Directive 2003/87/EC
Proizvodnja vodika in sinteznega plina iz Priloge I k Direktivi 2003/87/ES
The operator shall include at least the following potential emission sources for CO2 emissions: fuels used in the hydrogen or synthesis gas production process (reforming or partial oxidation), and fuels used for other combustion processes including for the purpose of producing hot water or steam.
Upravljavec vključi vsaj naslednje možne vire emisij CO2: goriva, ki se uporabljajo v proizvodnem procesu vodika ali sinteznega plina (preoblikovanje ali delna oksidacija) in goriva, ki se uporabljajo pri drugih procesih izgorevanja, tudi za pridobivanje tople vode ali pare.
Synthesis gas produced shall be considered as source stream under the mass balance methodology.
Proizvedeni sintezni plin se upošteva kot tok vira v skladu z metodologijo masne bilance.
For monitoring of emissions from combustion processes and from fuels used as process inputs in hydrogen production, the standard methodology in accordance with Article 24 and section 1 of this Annex shall be used.
Za spremljanje emisij pri procesih izgorevanja in pri gorivih, ki se uporabljajo kot vhodni materiali pri proizvodnji vodika, se uporablja standardna metodologija v skladu s členom 24 in oddelkom 1 te priloge.
For the monitoring of emissions from the production of synthesis gas, a mass balance in accordance with Article 25 shall be used.
Za spremljanje emisij pri proizvodnji sinteznega plina se uporablja masna bilanca v skladu s členom 25.
For emissions from separate combustion processes, the operator may choose to include them in the mass balance or to use the standard methodology in accordance with Article 24 at least for a part of the source streams, avoiding any gaps or double counting of emissions.
Upravljavec se lahko odloči, da emisije iz ločenih procesov izgorevanja goriv vključi v masno bilanco ali da zanje uporabi standardno metodologijo v skladu s členom 24 vsaj za del tokov vira, pri čemer se preprečijo vrzeli in dvojno štetje v zvezi z emisijami.
Where hydrogen and synthesis gas are produced at the same installation, the operator shall calculate CO2 emissions using either separate methodologies for hydrogen and for synthesis gas as outlined in the first two paragraphs of this subsection, or using one common mass balance.
Kadar proizvodnja vodika in sinteznega plina poteka v isti napravi, upravljavec izračuna emisije CO2 z uporabo ločenih metodologij za vodik in za sintezni plin, kot je navedeno v prvih dveh odstavkih tega pododdelka, ali z uporabo ene skupne masne bilance.
Production of soda ash and sodium bicarbonate as listed in Annex I to Directive 2003/87/EC
Proizvodnja natrijevega karbonata in natrijevega bikarbonata iz Priloge I k Direktivi 2003/87/ES