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Supercritical Carbon Dioxide Circulated EGS Combined with IGCC in New Mexico recovered is utilized by the HRSG to produce steam either for electricity production or used for the shift process portion of the WGS. Since the AGR is placed downstream of the WGS, a sulfur resistant catalyst was required for the shift reactions. The sulfur resistant catalyst serves a dual purpose as it also hydrolyzes COS to H2S, thus negating the need for a separate COS hydrolysis reactor. Due to the large capacity of the plant, multiple units are required to perform the given operations. The WGS is a system of two reactors (one high temperature and one low temperature) in series in parallel with another two reactors. There are also two mercury absorber fixed bed reactors. 4.4.7 Results: The system design of components in the IGCC allows for the consistent decrease in temperature through its operations. The energy (heat) saved by not reheating certain components is utilized as useful energy through the heat recovery steam generation (HRSG) unit. The combination of WGS, mercury removal, AGR, and Claus process permits the high production of hydrogen through the IGCC process. Figure 45 depicts the composition of the synthesis gas stream as it passes through water gas shift (WGS) reactor and the acid gas removal (AGR) reactor. Penn State University | 4.4 Gas Cleaning Unit 72PDF Image | GREAT NECK WATER POLLUTION CONTROL DISTRICT NASSAU COUNTY, NEW YORK MICROTURBINE INSTALLATION FEASIBILITY STUDY
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