Abstract:We have conducted comprehensive exergy analyses of three integrated gasification combined cycle with carbon capture and storage (IGCC-CCS) power plant configurations: (1) a baseline model using Selexol™ for H 2 S/CO 2 removal; (2) a modified version that adds a H 2 -selective membrane before the Selexol™ acid gas removal system; and (3) a modified baseline version that uses a CO 2 -selective membrane before the Selexol™ acid gas removal system. While holding the coal input flow rate and the CO 2 captured flow rates constant, it was determined that the H 2 -selective membrane case had a higher net power output (584 MW) compared to the baseline (564 MW) and compared to the CO 2 -selective membrane case (550 MW). Interestingly, the CO 2 -selective membrane case destroyed the least amount of exergy within the power plant (967 MW), compared with the Baseline case (999 MW) and the H 2 -membrane case (972 MW). The main problem with the CO 2 -selective membrane case was the large amount of H 2 (48 MW worth of H 2 chemical exergy) remaining within the supercritical CO 2 that exits the power plant. Regardless of the CO 2 capture process used, the majority of the exergy destruction occurred in the gasifier (305 MW) and gas turbine (~380 MW) subsystems, suggesting that these two areas should be key areas of focus of future improvements.