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Chapter 3: Capture of CO2 167 table 3.14 CO2 capture costs: Multi-product plants using advanced technology. NRC 2004 Parsons mitretek mitretek mitretek Range min max Study Assumptions and Results Simbeck 2005 * H2 NRC 2004 2002a 2003 2003 2003 Capture Plant Design * * * * Plant products (primary/secondary) Production process or type H2 H2 H2+electricity H2+electricity H2+electricity H2+electricity Feedstock Feedstock cost, LHV (US$ GJ−1) Plant capacity factor (%) CO2 capture/separation technology Capture plant input capacity, LHV (GJ h−1) Capture plant output capacity, LHV: Fuels (GJ h−1) Natural gas 5.26 90 Oxy-fuel 9527 7504 −13 78.3 95 0.086 0 1.46 4.074 13.7 Natural gas 4.73 90 Coal 1.20 90 Pgh #8 Coal 0.89 80 Oxy-fuel 2794 1956 7 70.9 94 0.117 0 8.45 1.855 13.4 Coal 1.03 85 Oxy-fuel 3020 1904 25 66.0 100 0.000 0 0.00 1.918 20 Coal 1.03 85 Oxy-fuel 6051 1844 416 55.2 100 0.000 0 0.00 3.846 20 Coal 1.03 85 Oxy-fuel 6051 1808 519 60.7 95 0.191 0 6.96 3.652 20 1 5 80 90 Net plant efficiency, LHV (%) CO2 capture efficiency (%)** CO2 emitted (MtCO2 yr−1)*** Carbon exported in fuels (MtC yr−1) Total carbon released (kgCO2 GJ−1 products) CO2 captured (MtCO2 yr−1) CO2 product pressure (MPa) Cost Results Cost year basis (constant dollars) Fixed charge rate (%) Capture plant TCR (million US$)**** Capture plant electricity price (US$ MWh−1) Capture plant fuel product cost, LHv (uS$ GJ−1) Capture cost confidence level (see Table 3.6) 2003 20 725 50.0 9.84 low 2000 16 441 45.0 8.53 low 2000 16 921 45.0 6.39 low 2000 14.3 398 30.8 5.79 2000 2000 Electricity (MW) 7697 6004 −66 74.9 90 0.505 0 11.10 3.119 13.7 8121 6004 −88 70.0 90 0.873 0 19.45 5.853 13.7 2794 9527 1808 7504 -88 519 55 78 90 100 0.000 0.873 0 0 0.0 19.5 1.9 5.9 13.4 20.0 Autothermal reforming with O2 provided by ITM 78% efficient ATR/SMR, adv CO2 compressor Gasifier LHV= High-pressure E-gas, HGCU, HTMR, H2SO4 co-product Advanced E-gas, HGCU, HTMR Advanced E-gas, HGCU, HTMR, large elec. co- product Advanced E-gas, HGCU, HTMR, SOFC, large elec. co-product 75-->80%, Adv ASU, membrane sep, adv CO2 compressor Notes: All costs in this table are for capture only and do not include the costs of CO2 transport and storage; see Chapter 8 for total CCS costs. * Reported HHV values converted to LHV assuming LHV/ HHV = 0.96 for coal and 0.846 for hydrogen. **CO2 capture efficiency = (C in CO2 captured)/(C in fossil fuel input to plant - C in carbonaceous fuel products of plant) x100; C associated with imported electricity is not included. ***Includes CO2 emitted in the production of electricity imported by the plant. ****Reported total plant investment values increased by 3.5% to estimate total capital requirement. 2000 12.7 12.7 12.7 441 950 1023 53.6 53.6 53.6 31 54 6.24 3.27 1.13 1.13 9.84 low to very low very low 12.7 20.0 398 1023PDF Image | CARBON DIOXIDE CAPTURE AND STORAGE
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