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156 IPCC Special Report on Carbon dioxide Capture and Storage table 3.10 CO2 capture costs: new IGCC power plants using current technology. Study Assumptions and Results et al. et al. et al. Reference Plant without capture) PLANtS WitH BitumiNOuS COAL FEEDStOCK Gasifier name or type * Shell, O2 blown, CGCU Illinois #6 413 85 47.4 1.03 0.682 * E-gas, O2 blown, CGUC Illinois #6 401 85 46.7 1.03 0.692 * Texaco quench, O2 blown Illinois #6 571 65 39.1 1.28 0.846 * E-gas, O2 blown Texaco quench, O2 blown bit, 1% S 521 80 44.6 0.98 0.725 * Texaco syngas cooler, O2 blown bit Texaco quench, O2 blown Texaco quench, O2 blown Shell, O2 blown Texaco quench, O2 blown Texaco quench, O2 blown Fuel type (bit, subbit, lig; other) and %S Reference plant size (MW) Plant capacity factor (%) Net plant efficiency, LHV (%) bit, 2.5% S 425 65 44.8 1.29 0.718 bit, 1%S 827 85 38.0 1.50 0.833 bit, 1%S 827 85 38.0 1.50 0.833 bit, 1%S 776 85 43.1 1.50 0.763 bit, 2.1%S 527 75 39.1 1.25 0.817 bit, 2.1%S 527 401 827 Fuel cost, LHV (US$ GJ-1) Reference plant emission rate (tCO2 MWh-1) 80 1.23 65 65 85 39.1 38 47 1.25 0.98 1.50 0.817 0.68 0.85 Capture Plant Design Selexol 359 40.1 87.0 0.105 Selexol 457 31.3 89.0 0.116 Selexol 404 38.5 91.0 0.073 Selexol 455 39.0 91.2 0.065 Selexol 31.5 0.104 Selexol 730 31.5 Selexol. NS 742 32.0 Selexol 676 34.5 Selexol 492 33.8 Selexol 492 351 742 CO2 capture technology Net plant size, with capture (MW) Net plant efficiency, LHV (%) CO2 capture system efficiency (%) CO2 emission rate after capture (t MWh-1) CO2 captured (Mt/yr) CO2 product pressure (MPa) CCS energy requirement (% more input MWh-1) CO2 reduction per kWh (%) Selexol 351 40.1 89.2 0.087 33.8 31 40 85 85 85 90 90 85 91 Cost Results 87 85 86 90 91 82 82 81 88 88 81 91 Cost year basis (constant dollars) Fixed charge factor (%) Reference plant TCR (US$ kW-1) Capture plant TCR (US$ kW-1) Incremental TCR for capture (US$ kW-1) Reference plant COE (uS$ mWh-1) Capture plant COE (uS$ mWh-1) incremental COE for capture 2002 14.8 1370 2270 900 40.6 62.9 22.3 2002 14.8 1374 1897 523 40.9 54.4 13.5 2002 15.0 1169 1549 380 43.4 59.9 16.5 2000 13.8 1251 1844 593 47.7 65.8 18.1 2000 13.0 1486 2067 581 2002 2002 11.0 11.0 1187 1187 1495 1414 308 227 45.0 45.0 56.0 54.0 11 9 2002 2001 2001 (uS$ mWh-1) 43.0 53.0 57.7 71.5 14.7 18.5 15 14.3 % increase in capital cost (over ref. plant) 66 55 32 37 38 33 19 23 33 38 18 23 47 39 38 34 30 21 28 22 39 26 19 36 33 31 30 19 17 24 20 33 19 66 30 20 55 21 11 32 25 13 37 % increase in COE (over ref. plant) 35 24 20 Cost of CO2 captured (US$/tCO2) Cost of CO2 avoided (US$/tCO2) Capture cost confidence level (see Table 3.6) 23 moderate 13 11 16 13 NEtL NEtL NEtL Parsons Simbeck Nsakala, iEA GHG iEA GHG iEA GHG Rubin Rubin Range 2002 2002 2002 2002b 2002 2003 2003 2003 2003 2005 2005 min max 1.803 14.5 18 1.870 14.5 16 2.368 8.3 25 1.379 8.3 16 2.151 4.682 4.728 11.0 11.0 21 19 4.050 2.749 11.0 13.7 25 16 13.7 8 14 16 14 25 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. ** Reported capital costs increased by 8% to include interest during construction. **Reported capital costs increased by 15% to estimate interest during construction and other owners’ costs. 14 1565 2179 614 11.0 14.8 1371 1311 1860 1748 489 437 48.0 48.3 63.0 62.6 17.3 11 17 1311 1169 1565 1748 1414 2270 437 227 900 61 41 61 79 54 79 18.2 9 22 0.152 0.151 0.142 0.097 0.097 0.07 0.15 2.383 1.38 4.73 ** ** **PDF Image | CARBON DIOXIDE CAPTURE AND STORAGE
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