Carbon Tax Act, 2019 (Act No. 15 of 2019)SchedulesSchedule 1Table 3 : Industrial Processes and Product Use (IPPU) Emission Factors |
Table 3
Industrial Processes and Product Use (IPPU) Emission Factors
IPCC Code |
SOURCE CATEGORY ACTIVITY / RAW MATERIAL PRODUCT |
TONNE CO2/ tonne product |
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 |
0.02 |
||||||
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) - NAPTHA |
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 CHORINATION 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 CHORINATION PROCESS (VCM) |
0.286 |
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 |
0.00006 |
|||||
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 MATERIAL |
0.2 |
||||||
DEFAULT EF |
0.52 |
||||||
2C6 |
ZINC PRODUCTION (PER TONNE PRODUCT) |
||||||
WAELZ KILN |
3.66 |
||||||
PYROMETALLURGICAL |
0.43 |
||||||
DEFAULT EF |
0.72 |