SCHEDULE 1
TABLE 1
FUEL COMBUSTION EMISSION FACTORS
STATIONARY SOURCE CATEGORY
[Table 1 amended by section 98 of Act 34 of 2019]
|
FUEL TYPE |
CO2(KGCO2/TJ) |
CH4(KGCH4/TJ) |
N2O (KGN2O/TJ) |
DEFAULT NET CALORIFIC VALUE (TJ/TONNE) |
||
|
NET CALORIFIC VALUE |
LOWER LIMIT OF THE 95% CONFIDENCE INTERVAL |
UPPER LIMIT OF THE 95% CONFIDENCE INTERVAL |
||||
|
ANTHRACITE |
98 300 |
1 |
1.5 |
0.0267 |
0.0216 |
0.0322 |
|
AVIATION GASOLINE |
70 000 |
3 |
0.6 |
0.0443 |
0.0425 |
0.0448 |
|
BIODIESEL |
0 |
3 |
0.6 |
0.027 |
0.0136 |
0.054 |
|
BIOGASOLINE |
0 |
3 |
0.6 |
0.027 |
0.0136 |
0.054 |
|
BITUMEN |
80 700 |
3 |
0.6 |
0.0402 |
0.0335 |
0.0412 |
|
BLAST FURNACE GAS |
260 000 |
1 |
0.1 |
0.00247 |
0.0012 |
0.005 |
|
DIESEL |
74 100 |
3 |
0.6 |
0.043 |
0.0414 |
0.0433 |
|
BROWN COAL BRIQUETTES |
97 500 |
1 |
1.5 |
0.0207 |
0.0151 |
0.032 |
|
CHARCOAL |
0 |
200 |
4 |
0.0295 |
0.0149 |
0.058 |
|
COAL TAR |
80 700 |
1 |
1.5 |
0.028 |
0.0141 |
0.055 |
|
COKE OVEN COKE AND LIGNITE COKE |
107 000 |
1 |
1.5 |
0.0282 |
0.0251 |
0.0302 |
|
COKE OVEN GAS |
44 400 |
1 |
0.1 |
0.0387 |
0.0196 |
0.077 |
|
COKING COAL |
94 600 |
1 |
1.5 |
0.0282 |
0.024 |
0.031 |
|
CRUDE OIL |
73 300 |
3 |
0.6 |
0.0438 |
0.0401 |
0.0448 |
|
DIESEL |
74 100 |
3 |
0.6 |
0.0381 |
0 |
0 |
|
ETHANE |
61 600 |
1 |
0.1 |
0.0464 |
0.0449 |
0.0488 |
|
GAS COKE |
107 000 |
1 |
0.1 |
0.0173 |
0.0251 |
0.0302 |
|
GAS WORKS GAS |
44 400 |
1 |
0.1 |
0.0387 |
0.0196 |
0.077 |
|
INDUSTRIAL WASTES |
143 000 |
30 |
4 |
N/A |
N/A |
N/A |
|
JET GASOLINE |
70 000 |
3 |
0.6 |
0.0443 |
0.0425 |
0.0448 |
|
JET KEROSENE |
71 500 |
3 |
0.6 |
0.0441 |
0.042 |
0.045 |
|
LANDFILL GAS |
0 |
1 |
0.1 |
0.0504 |
0.0254 |
0.1 |
|
LIGNITE |
101 000 |
1 |
1.5 |
0.0119 |
0.0055 |
0.0216 |
|
LIQUEFIED PETROLEUM GASES |
63 100 |
1 |
0.1 |
0.0473 |
0.0448 |
0.0522 |
|
LUBRICANTS |
73 300 |
3 |
0.6 |
0.0402 |
0.0335 |
0.0423 |
|
MUNICIPAL WASTES (BIOMASS FRACTION) |
0 |
30 |
4 |
0.0116 |
0.0068 |
0.018 |
|
MUNICIPAL WASTES (NON BIOMASS FRACTION) |
91 700 |
30 |
4 |
0.01 |
0.007 |
0.018 |
|
NAPHTHA |
73 700 |
3 |
0.6 |
0.0445 |
0.0418 |
0.0465 |
|
NATURAL GAS |
56 100 |
1 |
0.1 |
0.048 |
0.0465 |
0.0504 |
|
NATURAL GAS LIQUIDS |
64 200 |
3 |
0.6 |
0.041 |
0.0409 |
0.0469 |
|
OIL SHALE AND TAR SANDS |
107 000 |
1 |
1.5 |
0.0089 |
0.0071 |
0.0111 |
|
ORIMULSION |
77 000 |
3 |
0.6 |
0.0275 |
0.0275 |
0.0283 |
|
OTHER BIOGAS |
0 |
1 |
0.1 |
0.0504 |
0.0254 |
0.1 |
|
OTHER BITUMINOUS COAL |
94 600 |
1 |
1.5 |
0.0243 |
0.0199 |
0.0305 |
|
OTHER KEROSENE |
71 900 |
3 |
0.6 |
0.037 |
0 |
0 |
|
OTHER LIQUID BIOFUELS |
0 |
3 |
0.6 |
0.0274 |
0.0138 |
0.054 |
|
OTHER PETROLEUM PRODUCTS |
73 300 |
3 |
0.6 |
0.0402 |
0.0337 |
0.0482 |
|
OTHER PRIMARY SOLID BIOMASS |
0 |
30 |
4 |
0.0116 |
0.0059 |
0.023 |
|
OXYGEN STEEL FURNACE GAS |
182 000 |
1 |
0.1 |
0.00706 |
0.0038 |
0.015 |
|
PARAFFIN |
71 900 |
3 |
0.6 |
0.0438 |
0.0424 |
0.0452 |
|
PARAFFIN WAXES |
73 300 |
3 |
0.6 |
0.0402 |
0.0337 |
0.0482 |
|
PATENT FUEL |
97 500 |
1 |
1.5 |
0.0207 |
0.0151 |
0.032 |
|
PEAT |
0 |
1 |
1.5 |
0.00976 |
0.0078 |
0.0125 |
|
PETROL |
69 300 |
3 |
0.6 |
0.0443 |
0.0425 |
0.0448 |
|
PETROLEUM COKE |
97 500 |
3 |
0.6 |
0.0325 |
0.0297 |
0.0419 |
|
REFINERY FEEDSTOCK |
73 300 |
3 |
0.6 |
0.043 |
0.0363 |
0.0464 |
|
REFINERY GAS |
57 600 |
1 |
0.1 |
0.0495 |
0.0475 |
0.0506 |
|
RESIDUAL FUEL OIL (HEAVY FUEL OIL) |
77 400 |
3 |
0.6 |
0.0404 |
0.0398 |
0.0417 |
|
SHALE OIL |
73 300 |
3 |
0.6 |
0.0381 |
0.0321 |
0.0452 |
|
SLUDGE GAS |
0 |
1 |
0.1 |
0.0504 |
0.0254 |
0.1 |
|
SUB-BITUMINOUS COAL |
96 100 |
1 |
1.5 |
0.0192 |
0.0115 |
0.026 |
|
SULPHITE LYES (BLACK LIQUOR) |
0 |
3 |
2 |
0.0118 |
0.0059 |
0.023 |
|
WASTE OILS |
73 300 |
30 |
4 |
0.0402 |
0.0203 |
0.08 |
|
WHITE SPIRIT AND SBP |
73 300 |
3 |
0.6 |
0.0402 |
0.0337 |
0.0482 |
|
WOOD/WOOD WASTE |
0 |
30 |
4 |
0.0156 |
0.0079 |
0.031 |
NON-STATIONARY/MOBILE SOURCE CATEGORY ACTIVITY
|
FUEL TYPE |
CO2(KGCO2/TJ) |
CH4(KGCH4/TJ) |
N2O (KGN2O/TJ) |
DEFAULT NET CALORIFIC VALUE (TJ/TONNE) |
||
|
NET CALORIFIC VALUE |
LOWER LIMIT OF THE 95% CONFIDENCE INTERVAL |
UPPER LIMIT OF THE 95% CONFIDENCE INTERVAL |
||||
|
AVIATION GASOLINE |
70 000 |
3 |
0.6 |
0.0443 |
0.0425 |
0.0448 |
|
COMPRESSED NATURAL GAS |
56 100 |
92 |
3 |
N/A |
N/A |
N/A |
|
DIESEL |
74 100 |
4.15 |
28.6 |
0.0381 |
0 |
0 |
|
DIESEL — (OCEAN-GOING SHIPS) |
74 100 |
7 |
2 |
0.0381 |
0 |
0 |
|
DIESEL — RAIL |
74 100 |
4.5 |
28.6 |
0.0381 |
0 |
0 |
|
JET KEROSENE |
71 500 |
0.5 |
2 |
0.0441 |
0.042 |
0.045 |
|
KEROSENE |
71 500 |
3 |
0.6 |
0.037 |
0 |
0 |
|
LIQUIFIED NATURAL GASES |
56 100 |
92 |
3 |
N/A |
N/A |
N/A |
|
LIQUEFIED PETROLEUM GASES |
63 100 |
62 |
0.2 |
0.0473 |
0.0448 |
0.0522 |
|
LUBRICANTS |
73 300 |
3 |
0.6 |
0.0402 |
0.0335 |
0.0423 |
|
NATURAL GAS |
56 100 |
92 |
3 |
0.048 |
0.0465 |
0.0504 |
|
(PARAFFIN) OTHER KEROSENE |
71 900 |
3 |
0.6 |
0.0438 |
0.0424 |
0.0452 |
|
OTHER PETROLEUM PRODUCTS |
73 300 |
3 |
0.6 |
0.0402 |
0.0337 |
0.0482 |
|
PARAFFIN WAXES |
73 300 |
3 |
0.6 |
0.0402 |
0.0337 |
0.0482 |
|
PETROL |
69 300 |
3.5 |
5.7 |
0.0443 |
0.0425 |
0.0448 |
|
REFINERY GAS |
57 600 |
1 |
0.1 |
0.0495 |
0.0475 |
0.0506 |
|
RESIDUAL FUEL OIL— (HEAVY FUEL OIL) |
77 400 |
7 |
2 |
0.0404 |
0.0398 |
0.0417 |
|
SUB-BITUMINOUS COAL |
96 100 |
2 |
1.5 |
0.0192 |
0.0115 |
0.026 |
|
WHITE SPIRIT AND SBP |
73 300 |
3 |
0.6 |
0.0402 |
0.0337 |
0.0482 |
SCHEDULE 1
TABLE 2
FUGITIVE EMMISSION FACTORS
[Table 2 substituted by section 67(1) of Act 17 of 2023 deemed effective on 1 June, 2019]
|
IPCC Code |
SOURCE CATEGORY ACTIVITY |
CO2 |
CH4 |
N2O |
|
1B1 |
SOLID FUELS (M3 /TONNE) |
|||
|
1B1a |
COAL MINING AND HANDLING |
|||
|
1B1ai |
UNDERGROUND COAL MINING |
0.000077 |
0.00077 |
|
|
UNDERGROUND POST-MINING (HANDLING & TRANSPORT) |
0.000018 |
0.00018 |
||
|
1B1aii |
SURFACE COAL MINING |
N/A |
0 |
|
|
SURFACE POST-MINING (STORAGE AND TRANSPORT) |
N/A |
0 |
||
|
1B1c2 |
Charcoal production (Fuel wood input)(kgCH4/TJ) |
N/A |
0.300 |
|
|
Charcoal production (Charcoal produced)(kgCH4/TJ) |
N/A |
1.000 |
||
|
1B2 |
OIL AND NATURAL GAS (Gg/103M3 TOTAL OIL PRODUCTION) |
|||
|
1B2b |
NATURAL GAS |
|||
|
1B2b |
FLARING AND VENTING |
|||
|
1.B.2.b.ii |
WELL DRILLING |
0.0000001 |
0.000000033 |
ND |
|
1.B.2.b.ii |
WELL TESTING |
0.000009 |
0.000000051 |
0.000000000068 |
|
1.B.2.b.ii |
WELL SERVICING |
0.0000000019 |
0.00000011 |
ND |
|
1B2b |
GAS PRODUCTION (Gg/106M3 TOTAL OIL PRODUCTION) |
|||
|
1.B.2.b.iii.2 |
FUGITIVES |
1.40E-05 to 8.20E-05 |
3.80E-04 to 2.30E-03 |
N/A |
|
1.B.2.b.ii |
FLARING |
0.0012 |
0.00000076 |
0.000000021 |
|
GAS PROCESSING (Gg/106M3 RAW GAS FEED) |
||||
|
1.B.2.b.iii.3 |
SWEET GAS PLANTS—FUGITIVES |
1.50E-04 to 3.20E-04 |
4.80E-04 to 1.03E-03 |
N/A |
|
1.B.2.b.ii |
SWEET GAS PLANTS—FLARING |
0.0018 |
0.0000012 |
0.000000025 |
|
1.B.2.b.iii.3 |
SOUR GAS PLANTS—FUGITIVES |
0.0000079 |
0.000097 |
N/A |
|
1.B.2.b.ii |
SOUR GAS PLANTS—FLARING |
0.0036 |
0.0000024 |
0.000000054 |
|
1.B.2.b.i |
SOUR GAS PLANTS—RAW CO2 VENTING |
0.063 |
N/A |
N/A |
|
1.B.2.b.iii.3 |
DEEP CUT EXTRACTION—FUGITIVES |
0.0000016 |
0.000011 |
N/A |
|
1.B.2.b.ii |
DEEP CUT EXTRACTION—FLARING |
0.00011 |
0.000000072 |
0.000000012 |
|
1.B.2.b.iii.3 |
DEFAULT—FUGITIVES |
1.20E-05 to 3.20E-04 |
1.50E-04 to 1.03E-03 |
N/A |
|
1.B.2.b.ii |
DEFAULT—FLARING |
0.003 |
0.000002 |
0.000000033 |
|
1.B.2.b.i |
DEFAULT—RAW CO2 VENTING |
0.04 |
N/A |
N/A |
|
1B2b |
GAS TRANSMISSION & STORAGE (Gg-CO2/year/km |
|||
|
1.B.2.b.iii.4 |
TRANSMISSION—FUGITIVES |
0.000000016 |
0.0000025 |
N/A |
|
1.B.2.b.i |
TRANSMISSION—VENTING |
0.0000000085 |
0.0000010 |
N/A |
|
1.B.2.b.iii.4 |
STORAGE (Gg-CO2/year/M3) |
2.32E-12 |
ND |
|
|
1B2b |
GAS DISTRIBUTION (Gg/106M3 OF UTILITY SALES) |
|||
|
1.B.2.b.iii.5 |
ALL |
0.000051 |
0.0011 |
ND |
|
1B2b |
NATURAL GAS LIQUIDS TRANSPORT (Gg/ 103M3 CONDENSATE AND PENTANES PLUS) |
|||
|
1.B.2.a.iii.3 |
CONDENSATE |
0.0000000072 |
0.00000011 |
|
|
1.B.2.a.iii.3 |
LIQUEFIED PETROLEUM GAS (Gg/103M3 LPG) |
0.00000043 |
N/A |
2.2 0E-12 |
|
1.B.2.a.iii.3 |
LIQUEFIED NATURAL GAS (Gg/106M3 MARKETABLE GAS) |
ND |
ND |
ND |
|
1B2a |
OIL |
|||
|
1B2a |
OIL PRODUCTION (Gg/ 103M3 CONVENTIONAL OIL PRODUCTION) |
|||
|
1.B.2.a.iii.2 |
CONVENTIONAL OIL—FUGITIVES (ONSHORE) |
1.10E-10 to 2.60E-07 |
1.50E-09 to 3.60E-06 |
N/A |
|
1.B.2.a.iii.2 |
CONVENTIONAL OIL—FUGITIVES (OFFSHORE) |
0.000000000043 |
0.00000000059 |
N/A |
|
1.B.2.a.i |
CONVENTIONAL OIL—VENTING |
0.000000095 |
0.00000072 |
N/A |
|
1.B.2.a.ii |
CONVENTIONAL OIL—FLARING |
0.000041 |
0.000000025 |
0.00000000064 |
|
1B2a |
OIL PRODUCTION (Gg/ 103M3 HEAVY OIL PRODUCTION) |
|||
|
1.B.2.a.iii.2 |
HEAVY OIL/COLD BITUMEN—FUGITIVES |
0.00000054 |
0.0000079 |
N/A |
|
1.B.2.a.i |
HEAVY OIL/COLD BITUMEN—VENTING |
0.0000053 |
0.000017 |
N/A |
|
1.B.2.a.ii |
HEAVY OIL/COLD BITUMEN—FLARING |
0.000022 |
0.00000014 |
0.00000000046 |
|
1B2a |
OIL PRODUCTION (Gg/ 103M3 THERMAL BITUMEN PRODUCTION) |
|||
|
1.B.2.a.iii.2 |
THERMAL OIL PRODUCTION—FUGITIVES |
0.000000029 |
0.00000018 |
N/A |
|
1.B.2.a.i |
THERMAL OIL PRODUCTION—VENTING |
0.00000022 |
0.0000035 |
N/A |
|
1.B.2.a.ii |
THERMAL OIL PRODUCTION—FLARING |
0.000027 |
0.000000016 |
0.00000000024 |
|
1B2a |
OIL PRODUCTION (Gg/103M3 SYNTHETIC CRUDE PRODUCTION FROM OILSANDS) |
|||
|
1.B.2.a.iii.2 |
SYNTHETIC CRUDE (FROM OILSANDS) |
ND |
0.0000023 |
ND |
|
1.B.2.a.iii.2 |
SYNTHETIC CRUDE (OIL SHALE) |
ND |
ND |
ND |
|
1B2a |
OIL PRODUCTION (Gg/103M3 TOTAL OIL PRODUCTION) |
|||
|
1.B.2.a.iii.2 |
DEFAULT TOTAL—FUGITIVES |
0.00000028 |
0.0000022 |
N/A |
|
1.B.2.a.i |
DEFAULT TOTAL—VENTING |
0.0000018 |
0.0000087 |
N/A |
|
1.B.2.a.ii |
DEFAULT TOTAL—FLARING |
0.000034 |
0.000000021 |
0.00000000054 |
|
1B2a |
OIL UPGRADING (Gg/103M3 OIL UPGRADED) |
|||
|
1.B.2.a.iii.2 |
ALL |
ND |
ND |
ND |
|
1B2a |
OIL TRANSPORT (Gg/103M3 OIL TRANSPORTED BY PIPELINE) |
|||
|
1.B.2.a.iii.3 |
PIPELINES |
0.00000000049 |
0.0000000054 |
N/A |
|
1B2a |
OIL TRANSPORT (Gg/103M3 OIL TRANSPORTED BY TANKER TRUCK) |
|||
|
1.B.2.a.i |
TANKER TRUCKS AND RAIL CARS—VENTING |
0.0000000023 |
0.000000025 |
N/A |
|
OIL TRANSPORT (Gg/ 103M3 OIL TRANSPORTED BY TANKER SHIPS) |
||||
|
1.B.2.a.i |
LOADING OFF-SHORE PRODUCTION ON TANKER SHIPS—VENTING |
ND |
ND |
ND |
|
1B2a |
OIL REFINING (Gg/ 103M3 OIL REFINED) |
|||
|
1.B.2.a.iii.4 |
ALL |
2.60E-09 to 4.10E-08 |
ND |
SCHEDULE 1
TABLE 3
INDUSTRIAL PROCESSES AND PRODUCT USE (IPPU) EMISSION FACTORS
|
IPCC Code |
SOURCE CATEGORY ACTIVITY / RAW MATERIAL / PRODUCT |
TONNE |
TONNE CH4/ tonne product |
TONNE N2O/ tonne product |
TONNE C2F6/ tonne product |
TONNE CF4/ tonne product |
TONNE SF6/ tonne product |
|
2A1 |
CEMENT PRODUCTION (PER TONNE OF CLINKER) |
||||||
|
CEMENT |
0.52 |
||||||
|
2A2 |
LIME PRODUCTION (PER TONNE OF LIME) |
||||||
|
QUICKLIME/HIGH CALCIUM LIME |
0.75 |
||||||
|
DOLOMITIC LIME |
0.77 |
||||||
|
HYDRATED LIME |
0.59 |
||||||
|
2A3 |
GLASS PRODUCTION (PER TONNE GLASS) |
||||||
|
GLASS PRODUCTION |
0.2 |
||||||
|
2A4 |
Other Process Uses of Carbonates |
||||||
|
2A4a |
CERAMICS (PER TONNE CARBONATE) |
||||||
|
CALCITE/ARAGONITE (CaCO3) |
0.43971 |
||||||
|
MAGNESITE (MgCO3) |
0.52197 |
||||||
|
DOLOMITE (CaMg(CO3)2)) |
0.47732 |
||||||
|
SIDERITE (FeCO3) |
0.37987 |
||||||
|
ANKERITE (Ca(Fe,Mg,Mn)(CO3)2)) |
0.40822 to 0.47572 |
||||||
|
RHODOCHROSITE (MnCO3) |
0.38286 |
||||||
|
SODIUM CARBONATE/SODA ASH (Na2CO3) |
0.41492 |
||||||
|
2A4b |
OTHER USES OF SODA ASH (PER TONNE CARBONATE) |
||||||
|
CALCITE/ARAGONITE (CaCO3) |
0.43971 |
||||||
|
MAGNESITE (MgCO3) |
0.52197 |
||||||
|
DOLOMITE (CaMg(CO3)2)) |
0.47732 |
||||||
|
SIDERITE (FeCO3) |
0.37987 |
||||||
|
ANKERITE (Ca(Fe,Mg,Mn)(CO3)2)) |
0.40822 to 0.47572 |
||||||
|
RHODOCHROSITE (MnCO3) |
0.38286 |
||||||
|
SODIUM CARBONATE/SODA ASH (Na2CO3) |
0.41492 |
||||||
|
2A4c |
NON METALLURGICAL MAGNESIA PRODUCTION (PER TONNE CARBONATE) |
||||||
|
CALCITE/ARAGONITE (CaCO3) |
0.43971 |
||||||
|
MAGNESITE (MgCO3) |
0.52197 |
||||||
|
DOLOMITE (CaMg(CO3)2)) |
0.47732 |
||||||
|
SIDERITE (FeCO3) |
0.37987 |
||||||
|
ANKERITE (Ca(Fe,Mg,Mn)(CO3)2)) |
0.40822 to 0.47572 |
||||||
|
RHODOCHROSITE (MnCO3) |
0.38286 |
||||||
|
SODIUM CARBONATE/SODA ASH (Na2CO3) |
0.41492 |
||||||
|
2A5 |
OTHER (PER TONNE CARBONATE) |
||||||
|
CALCITE/ARAGONITE (CaCO3) |
0.43971 |
||||||
|
MAGNESITE (MgCO3) |
0.52197 |
||||||
|
DOLOMITE (CaMg(CO3)2)) |
0.47732 |
||||||
|
SIDERITE (FeCO3) |
0.37987 |
||||||
|
ANKERITE (Ca(Fe,Mg,Mn)(CO3)2)) |
0.40822 to 0.47572 |
||||||
|
RHODOCHROSITE (MnCO3) |
0.38286 |
||||||
|
SODIUM CARBONATE/SODA ASH (Na2CO3) |
0.41492 |
||||||
|
2B1 |
AMMONIA PRODUCTION (PER TONNE NH3) |
||||||
|
MODERN PLANTS-CONVENTIONAL REFORMING (NATURAL GAS) |
1.694 |
||||||
|
EXCESS AIR REFORMING (NATURAL GAS) |
1.666 |
||||||
|
AUTOTHERMAL REFORMING (NATURAL GAS) |
1.694 |
||||||
|
PARTIAL OXIDATION |
2.772 |
||||||
|
AVERAGE VALUE NATURAL GAS (MIXTURE OF MODERN & OLD) |
2.104 |
||||||
|
AVERAGE VALUE (PARTIAL OXIDATION) |
3.273 |
||||||
|
2B2 |
NITRIC ACID PRODUCTION (PER TONNE NITRIC ACID) |
||||||
|
PLANTS WITH NSCR (ALL PROCESSES) |
0.002 |
||||||
|
PLANTS WITH PROCESS (INTEGRATED OR TAIL GAS NO2 DESTRUCTION) |
0.0025 |
||||||
|
ATMOSPHERIC PRESSURE PLANTS (LOW PRESSURE PLANTS) |
0.005 |
||||||
|
MEDIUM PRESSURE COMBUSTION PLANTS (MEDIUM PRESSURE) |
0.007 |
||||||
|
HIGH PRESSURE PLANTS (HIGH PRESSURE) |
0.009 |
||||||
|
2B3 |
ADIPIC ACID PRODUCTION (PER TONNE ADIPIC ACID UNCONTROLLED) |
||||||
|
NITRIC ACID OXIDATION (ADIPIC ACID) |
0.3 |
||||||
|
2B4 |
CAPROLACTAM, GLYOXAL AND GLYOXYLIC ACID PRODUCTION (PER TONNE PRODUCED) |
||||||
|
CAPROLACTAM PRODUCTION (RASCHIG) |
0.009 |
||||||
|
GLYOXAL PRODUCTION |
0.1 |
||||||
|
GLYOXYLIC ACID PRODUCTION |
0.02 |
||||||
|
2B5 |
CARBIDE PRODUCTION (PER TONNE RAW MATERIAL USED) |
||||||
|
SILICON CARBIDE PRODUCTION |
2.3 |
0.0102 |
|||||
|
PETROLEUM COKE USE |
1.7 |
||||||
|
2B5 |
CARBIDE PRODUCTION (PER TONNE CARBIDE PRODUCED) |
||||||
|
SILICON CARBIDE PRODUCTION (CARBIDE PRODUCED) |
2.62 |
0.0116 |
|||||
|
PETROLEUM COKE USE |
1.09 |
||||||
|
USE OF PRODUCT |
1.1 |
||||||
|
2B6 |
TITANIUM DIOXIDE PRODUCTION (PER TONNE PRODUCT) |
||||||
|
TITANIUM SLAG |
NOT AVAILABLE |
||||||
|
SYNTHETIC RUTILE |
1.43 |
||||||
|
RUTILE TITANIUM DIOXIDE (CHLORIDE ROUTE) |
1.34 |
||||||
|
2B7 |
SODA ASH PRODUCTION (PER TONNE OF SODA ASH OR TRONA) |
||||||
|
NATURAL SODA ASH OUTPUT |
0.138 |
||||||
|
NATURAL SODA ASH (TRONA USED) |
0.097 |
||||||
|
2B8 |
PETROCHEMICAL AND CARBON BLACK PRODUCTION |
||||||
|
2B8a |
METHANOL PRODUCTION (PER TONNE METHANOL PRODUCED) |
||||||
|
CONVENTIONAL STEAM REFORMING WITHOUT PRIMARY REFORMER (NATURAL GAS FEEDSTOCK) |
0.67 |
0.0023 |
|||||
|
CONVENTIONAL STEAM REFORMING WITH PRIMARY REFORMER (NATURAL GAS FEEDSTOCK) |
0.497 |
0.0023 |
|||||
|
CONVENTIONAL STEAM REFORMING LURGI CONVENTIONAL PROCESS (NATURAL GAS FEEDSTOCK) |
0.385 |
0.0023 |
|||||
|
CONVENTIONAL STEAM REFORMING LURGI CONVENTIONAL PROCESS (NATURAL GAS+CO2 FEEDSTOCK) |
0.267 |
0.0023 |
|||||
|
CONVENTIONAL STEAM REFORMING LURGI LOW PRESSURE PROCESS (NATURAL GAS FEEDSTOCK) |
0.267 |
0.0023 |
|||||
|
CONVENTIONAL STEAM REFORMING LURGI COMBINED PROCESS (NATURAL GAS FEEDSTOCK) |
0.396 |
0.0023 |
|||||
|
CONVENTIONAL STEAM REFORMING LURGI MEGA METHANOL PROCESS (NATURAL GAS FEEDSTOCK) |
0.31 |
0.0023 |
|||||
|
PARTIAL OXIDATION PROCESS (OIL FEEDSTOCK) |
1.376 |
0.0023 |
|||||
|
PARTIAL OXIDATION PROCESS (COAL FEEDSTOCK) |
5.285 |
0.0023 |
|||||
|
PARTIAL OXIDATION PROCESS (LIGNITE FEEDSTOCK) |
5.02 |
0.0023 |
|||||
|
CONVENTIONAL STEAM REFORMING WITH INTEGRATED AMMONIA PRODUCTION (NATURAL GAS FEEDSTOCK) |
1.02 |
0.0023 |
|||||
|
2B8b |
STEAM CRACKING ETHYLENE PRODUCTION (PER TONNE ETHYLENE PRODUCED) |
||||||
|
ETHYLENE (TOTAL PROCESS & ENERGY FEEDSTOCK USE)—NAPTHA |
1.73 |
0.003 |
|||||
|
ETHYLENE (TOTAL PROCESS & ENERGY FEEDSTOCK USE)—GAS OIL |
2.29 |
0.003 |
|||||
|
ETHYLENE (TOTAL PROCESS & ENERGY FEEDSTOCK USE)—ETHANE |
0.95 |
0.006 |
|||||
|
ETHYLENE (TOTAL PROCESS & ENERGY FEEDSTOCK USE)—PROPANE |
1.04 |
0.003 |
|||||
|
ETHYLENE (TOTAL PROCESS & ENERGY FEEDSTOCK USE)—BUTANE |
1.07 |
0.003 |
|||||
|
ETHYLENE (TOTAL PROCESS & ENERGY FEEDSTOCK USE)—OTHER |
1.73 |
0.003 |
|||||
|
ETHYLENE ( PROCESS FEEDSTOCK USE)— NAPHTHA |
1.73 |
0.003 |
|||||
|
ETHYLENE ( PROCESS FEEDSTOCK USE)—GAS OIL |
2.17 |
0.003 |
|||||
|
ETHYLENE ( PROCESS FEEDSTOCK USE)—ETHANE |
0.76 |
0.006 |
|||||
|
ETHYLENE ( PROCESS FEEDSTOCK USE)— PROPANE |
1.04 |
0.003 |
|||||
|
ETHYLENE ( PROCESS FEEDSTOCK USE)—BUTANE |
1.07 |
0.003 |
|||||
|
ETHYLENE ( PROCESS FEEDSTOCK USE)—OTHER |
1.73 |
0.003 |
|||||
|
ETHYLENE ( SUPPLEMENTAL FUEL-ENERGY FEEDSTOCK) USE—GAS OIL |
0.12 |
0.003 |
|||||
|
ETHYLENE ( SUPPLEMENTAL FUEL-ENERGY FEEDSTOCK) USE—ETHANE |
0.19 |
0.006 |
|||||
|
2B8c |
ETHYLENE DICHLORIDE AND VINYL CHLORIDE MONOMER (PER TONNE EDC PRODUCED OR TONNE VCM PRODUCT PRODUCED) |
||||||
|
DIRECT CHLORINATION PROCESS (EDC) |
0.191 |
0.0000226 |
|||||
|
OXYCHLORINATION PROCESS (EDC) |
0.202 |
0.0000226 |
|||||
|
BALANCED PROCESS (DEFAULT)—EDC |
0.196 |
0.0000226 |
|||||
|
2B8c |
ETHYLENE DICHLORIDE AND VINYL CHLORIDE MONOMER (PER TONNE VCM PRODUCED OR TONNE VCM PRODUCT PRODUCED) |
||||||
|
DIRECT CHLORINATION PROCESS (EDC) |
0.191 |
0.0000226 |
|||||
|
OXYCHLORINATION PROCESS (VCM) |
0.302 |
0.0000226 |
|||||
|
BALANCED PROCESS (DEFAULT) -VCM |
0.294 |
0.0000226 |
|||||
|
2B8d |
ETHYLENE OXIDE (PER TONNE ETHYLENE OXIDE PRODUCED) |
||||||
|
AIR PROCESS (DEFAULT)— CATALYST DEFAULT (70) |
0.863 |
0.00179 |
|||||
|
AIR PROCESS (DEFAULT)— CATALYST (75) |
0.663 |
0.00179 |
|||||
|
AIR PROCESS (DEFAULT)— CATALYST (80) |
0.5 |
0.00179 |
|||||
|
OXYGEN PROCESS (DEFAULT)—CATALYST DEFAULT (75) |
0.663 |
0.00179 |
|||||
|
OXYGEN PROCESS— CATALYST (80) |
0.5 |
0.00179 |
|||||
|
OXYGEN PROCESS— CATALYST (85) |
0.35 |
0.00179 |
|||||
|
ALL ETHYLENE OXIDE PROCESSES—THERMAL TREATMENT |
N/A |
0.00079 |
|||||
|
2B8e |
ACRYLONITRILE (PER TONNE ACRYLONITRILE PRODUCED) |
||||||
|
DIRECT AMMOXIDATION WITH SECONDARY PRODUCTS BURNED FOR ENERGY RECOVERY OR FLARED (DEFAULT) |
1 |
0.00018 |
|||||
|
DIRECT AMMOXIDATION WITH ACETONITRILE BURNED FOR ENERGY RECOVERY OR FLARED |
0.83 |
0.00018 |
|||||
|
DIRECT AMMOXIDATION WITH ACETONITRILE & HYDROGEN CYANIDE RECOVERED AS PRODUCT |
0.79 |
0.00018 |
|||||
|
2B8f |
CARBON BLACK PRODUCTION (PER TONNE CARBON BLACK PRODUCED) |
||||||
|
FURNACE BLACK PROCESS (DEFAULT)—Primary Feedstock |
1.96 |
0.00006 |
|||||
|
THERMAL BLACK PROCESS—PRIMARY FEEDSTOCK |
4.59 |
0.00006 |
|||||
|
ACETYLENE BLACK PROCESS—PRIMARY FEEDSTOCK |
0.12 |
0.00006 |
|||||
|
FURNACE BLACK PROCESS (DEFAULT)—SECONDARY FEEDSTOCK |
0.66 |
0.00006 |
|||||
|
THERMAL BLACK PROCESS—SECONDARY FEEDSTOCK |
0.66 |
0.00006 |
|||||
|
ACETYLENE BLACK PROCESS—SECONDARY FEEDSTOCK |
0.66 |
0.00006 |
|||||
|
FURNACE BLACK PROCESS (DEFAULT)—TOTAL FEEDSTOCK |
2.62 |
0.00006 |
|||||
|
THERMAL BLACK PROCESS—TOTAL FEEDSTOCK |
5.25 |
0.00 006 |
|||||
|
ACETYLENE BLACK PROCESS—TOTAL FEEDSTOCK |
0.78 |
0.00006 |
|||||
|
ALL CARBON BLACK PROCESSES (NO THERMAL TREATMENT) |
N/A |
0.0287 |
|||||
|
2C1 |
IRON AND STEEL PRODUCTION (PER TONNE PRODUCT PRODUCED) |
||||||
|
SINTER PRODUCTION |
0.2 |
0.00007 |
|||||
|
COKE OVEN |
0.56 |
0.0000001 |
|||||
|
PIG IRON PRODUCTION |
1.35 |
||||||
|
DIRECT REDUCED IRON (DRI) PRODUCTION |
0.7 |
0.001/TJ (NG) |
|||||
|
PELLET PRODUCTION |
0.03 |
||||||
|
BASIC OXYGEN FURNACE |
1.46 |
||||||
|
ELECTRIC ARC FURNACE |
0.08 |
||||||
|
OPEN HEARTH FURNACE |
1.72 |
||||||
|
GLOBAL AVERAGE |
1.06 |
||||||
|
2C2 |
FERROALLOYS PRODUCTION (PER TONNE PRODUCTION) |
||||||
|
FERROSILICON (45%) SI |
2.5 |
||||||
|
FERROSILICON (65%) SI |
3.6 |
0.001 |
|||||
|
FERROSILICON (75%) SI |
4 |
0.001 |
|||||
|
FERROSILICON (90%) SI |
4.8 |
0.0011 |
|||||
|
FERROMANGANESE (7% C) |
1.3 |
||||||
|
FERROMANGANESE (1% C) |
1.5 |
||||||
|
SILICOMANGANESE |
1.4 |
||||||
|
SILICON METAL |
5 |
0.0012 |
|||||
|
FERROCHROMIUM (STAND ALONE) |
1.3 |
||||||
|
FERROCHROMIUM (WITH SINTER PLANT) |
1.6 |
||||||
|
2C3 |
ALUMINIUM PRODUCTION (PER TONNE ALUMINIUM PRODUCED) |
||||||
|
PREBAKE |
1.6 |
||||||
|
SODERBERG |
1.7 |
||||||
|
CWPB |
0.00004 |
0.0004 |
|||||
|
SWPB |
0.0004 |
0.0016 |
|||||
|
VSS |
0.00004 |
0.0008 |
|||||
|
HSS |
0.00003 |
0.0004 |
|||||
|
2C4 |
MAGNESIUM PRODUCTION (PER TONNE MAGNESIUM PRODUCED) |
||||||
|
DOLOMITE |
5.13 |
0.001 |
|||||
|
MAGNESITE |
2.83 |
0.001 |
|||||
|
2C5 |
LEAD PRODUCTION (PER TONNE PRODUCT) |
||||||
|
IMPERIAL SMELT FURNACE (ISF) PRODUCTION |
0.59 |
||||||
|
DIRECT SMELTING PRODUCTION |
0.25 |
||||||
|
TREATMENT OF SECONDARY RAW MATERIALS |
0.2 |
||||||
|
DEFAULT EF |
0.52 |
||||||
|
2C6 |
ZINC PRODUCTION (PER TONNE PRODUCT) |
||||||
|
WAELZ KILN |
3.66 |
||||||
|
PYROMETALLURGICAL |
0.43 |
||||||
|
DEFAULT EF |
1.72 |