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Supercritical Carbon Dioxide Circulated EGS Combined with IGCC in New Mexico Assuming the H2S input stream is at least 20-50% H2S, a sulfur recovery of 94 to 96% will be achieved (Klara, 2007). 4.4.6 Methods To ensure that the IGCC plant maintained the highest possible efficiency and maximum heat recovery a comprehensive literature review was performed. Variations of each component were considered, including experimental design and operational procedures for the water gas shift and acid gas removal. In particular, the AGR was placed downstream of the WGS so that there would be a consistent step down in temperature instead of reheating the raw synthesis gas to be passed through the WGS. Figures 43 and 44 graphically show the difference in the upstream and downstream placement of the AGR. Figure 43: Upstream AGR Placement Temperature Profile 10000 1000 100 10 Gasifier Radiative Cooler Quencher WGS Mercury AGR Removal Figure 44: Down Stream AGR Placement Temperature Profile Figure 44 represents the chosen design path to minimize heat loss and maximize heat recovery through the IGCC process. Since no reheat is required for the WGS, any heat that is Penn State University | 4.4 Gas Cleaning Unit 71 Temperature ( C) Log scalePDF Image | GREAT NECK WATER POLLUTION CONTROL DISTRICT NASSAU COUNTY, NEW YORK MICROTURBINE INSTALLATION FEASIBILITY STUDY
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