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Table 20: Summary of Case Study Results Cases Gross Output (MW) Net Plant Efficiency (%) Capital Cost ($/kW -net) Revenue Required ($/MWh) PC Supercritical PC Supercritical + CCS PC Subcritical PC Subcritical + CCS IECM 580.2 663.3 583.2 681.3 NETL IECM 580.2 39.1% 663.4 27.1% 583.3 36.8% 679.9 24.8% NETL IECM NETL IECM NETL 39.1% 1601 1575 60.4 63.3 27.2% 2857 2870 108.4 114.8 36.8% 1541 1549 60.1 64.0 24.9% 2935 2895 112.5 118.8 5.2.5 Cost Sensitivity A cost sensitivity analysis was done for different steam cycles (Subcritical, Supercritical, and Ultra Supercritical), for different coal types (Appalachian Medium Sulfur, Illinois #6, and Wyoming Powder River Basin), and for plants with and without CO2 capture across a range of net plant sizes (250MW to 750MW). In each of these sensitivity studies, the defaults for the IECM were used with an SCR, ESP, and FGD system, and with an Advanced Amine CO2 Capture System for the case with CO2 capture. The results are presented below. Cost Sensitivity to Steam Cycle Type In the sensitivity analysis for the steam cycle, an IECM default plant was built with an SCR, ESP, and FGD system, but without a CO2 capture system, and the coal used was Illinois #6. The net plant size was varied between 250 and 750 MW. The plant efficiencies were approximately constant through this range of plant sizes, with the Subcritical plant having an efficiency of 36.4%, the Supercritical plant having an efficiency of 38.7%, and the Ultra Supercritical plant having an efficiency of 42.7% (all HHV). The results from the sensitivity studies for Capital Cost and Revenue Required are shown in Figure 9 and Figure 10 below. Integrated Environmental Control Model - Technical Documentation • 54PDF Image | Amine Based CO2 Capture
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