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160 table 3.11. Continued. Study Assumptions and Results Reference Plant (without capture) Plant products (primary/secondary) Production process or type Feedstock Feedstock cost, LHV (US$ GJ−1) IPCC Special Report on Carbon dioxide Capture and Storage mitretek 2003 * F-T liquids + electricity Unspecified O2-blown gasifier, unspecified synthesis reactor Range min max config, config, Coal Coal 1.00 1.00 1.00 1.09 Larson/Ren 2003 MeOH +electricity Texaco quench, Liquid phase reactor, Larson/Ren 2003 MeOH +electricity Texaco quench, Liquid phase reactor, LiQuiD FuEL AND ELECtRiCity PRODuCtS Larson/Ren 2003 DME +electricity Texaco quench, Liquid phase reactor, Larson/Ren 2003 DME +electricity Texaco quench, Liquid phase reactor, Celik et al. 2005 DME + electricity Texaco quench, Liquid phase reactor, Celik et al. 2005 DME + electricity Texaco quench, Liquid phase reactor, Celik et al. 2005 DME + electricity Texaco quench, Liquid phase reactor, Celik et al. 2005 DME + electricity Texaco quench, Liquid phase reactor, Once-through Once-through Once-through Once-through Once-through Once-through Once-through Once-through config, Coal Coal 1,09 1.00 config, config, Coal Coal 1.00 1.00 9893 8690 2254 2160 625 552 45.5 47.7 85 85 5.646 4.895 0.317 0.334 203 198 config, Coal 1.00 8690 2160 552 47.7 85 4.895 0.334 198 CO2 H2S co-capture. Selexol Coal config, Coal 1.00 7931 2161 490 49.5 80 4.077 0.274 185 CO2 H2S co-capture. Rectisol 7931 2161 469 config, Coal 1.00 7931 2161 Ref. plant input capacity, LHV (GJ h−1) Ref plant output capacity, LHV: Fuels (GJ h−1) Electricity (MW) 16136 9893 7161 2254 697 625 59.9 45.5 90 85 8.067 5.646 1.190 0.317 163 203 Amine Selexol scrubber 16136 9893 7242 2254 7931 7931 2161 2161 7931 16136 2160 7161 490 49.5 490 490 490 697 Net plant efficiency, LHV (%) Plant capacity factor (%) CO2 emitted (MtCO2 yr−1) Carbon exported in fuels (MtC yr−1) 49.5 49.5 80 80 80 80 90 45.5 59.9 4.077 4.077 4.077 4.08 8.07 0.274 0.274 0.274 0.27 1.19 Total carbon released (kgCO2 GJ−1 products) Capture Plant Design CO2 capture/separation technology CO2 H2S Selexol co-capture. 185 CO2 H2S co-capture. Rectisol 7931 2160 367 43.9 89 185 CO2 H2S co-capture. Rectisol 7931 2160 365 43.8 92 185 CO2 H2S co-capture. Rectisol 7931 2160 163 203 7931 16136 2160 7242 Capture plant input capacity, LHV (GJ h−1) Capture plant output capacity LHV: Fuels (GJ h−1) Electricity (MW) Selexol 9893 8690 510 582 56.3 44.0 91 58 0.733 2.377 2254 2160 577 531 43.8 46.9 2160 527 353 582 43 56 97 32 97 Net plant efficiency, LHV (%) CO2 capture efficiency (%)** CO2 emitted (MtCO2 yr−1)*** Carbon exported in fuels (MtC yr−1) 48.5 63 32 37 36 353 43.2 Total carbon released (kgCO2 GJ−1 products) CO2 captured (MtCO2 yr−1) CO2 product pressure (MPa) CCS energy requirement. (% more input/GJ plant output) CO2 reduction/unit product (%) 71.7 109.2 7.260 3.269 13.8 15 6.5 3.6 56 46 12.7 15.0 2160 1351 2243 1385 3.8 2.6 35.6 42.9 53.6 42.9 50.5 0.0 5.58 9.12 5.43 10.36 -0.15 1.24 -5.7 13.6 12.3 13.2 3.547 1.574 1.819 1.479 15 15 15 15 57 53 43 43 145 3.692 3.790 4.021 1.48 7.26 1.2 0.317 2.099 3.320 3.076 2.598 0.317 0.294 0.294 0.274 101.0 144.9 137.4 134 4.0 1.9 50 27 31 15.0 15.0 1351 1215 1220 1237 -9.7 1.8 42.9 42.9 42.9 42.9 0.0 0.0 9.12 8.68 8.42 9.37 -0.70 0.69 -7.7 7.9 -6.4 13.3 -6.9 13.0 0.390 0.288 0.028 0.03 3.32 0.274 0.274 0.274 0.274 1.200 15 15 2.0 12.8 13.0 15 14 15 14.5 1.9 14.5 Cost year basis (constant dollars) Fixed charge rate (%) Reference plant TCR (million US$)**** 15.0 15.0 15.0 15.0 12.7 15.0 1161 1161 2160 27 56 Cost Results 2003 2003 2003 2003 15.0 1215 1161 1161 1161 Capture plant TCR (million US$)**** % increase in capital cost (%) Ref. plant electricity price (US$ MWh−1) 1090 1066 1128 1164 -10.3 -8.1 -2.8 0.2 42.9 44.1 44.1 44.1 42.9 58.0 58.0 58.0 0.0 31.5 31.5 31.5 8.68 7.41 7.41 7.41 7.57 6.73 7.18 7.65 -1.11 -0.68 -0.23 0.24 1172 1066 2243 0.9 -10.3 3.8 Capture plant electricity price (US$ MWh−1) % increase in assumed elec. price 44.1 35.6 44.1 58.0 42.9 58.0 31.5 0.0 50.5 7.41 5.6 9.1 8.09 5.4 10.4 0.68 -1.1 1.2 Ref. plant fuel product cost, LHv (uS$ GJ−1) Capture plant fuel product cost, LHv (uS$ GJ−1) increase in fuel product cost (uS$ GJ−1) -12.8 -9.2 -18.4 -12.4 -18.3 -13.3 -3.1 3.2 9.2 -12.8 13.6 -1.5 1.5 4.1 -18.4 13.3 -1.8 1.8 4.8 -18.3 13.2 % increase in fuel product cost Cost of CO2 captured (US$/tCO2) Cost of CO2 avoided (US$/tCO2) Confidence level (see Table 3.6) moderate moderate 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, 0.846 for hydrogen, and 0.93 for F-T liquids. ** 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. moderate low to moderatePDF Image | CARBON DIOXIDE CAPTURE AND STORAGE
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