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Supercritical Carbon Dioxide Circulated EGS Combined with IGCC in New Mexico Figure 45: Composition of synthesis gas through WGS and AGR The clean synthesis gas being sent to the gas turbine is roughly 91.4% H2 and approximately 5% CO2. The stream that is to be sent to the EGS is comprised of 99.5% CO2. Because of the purity of this stream, the effluent requires no further processing or modification before it is pumped underground for heat recovery. 4.4.8 Conclusion The design of the IGCC plant with the acid gas removal downstream of the water gas shift reactors is essential to minimizing irreversible heat loss through the system. The utilization of the sulfur-resistant Co/Mo catalyst is also vital for the system as it allows the CO in the sour synthesis gas to be shifted to CO2 thus freeing H2 from water. This Co/Mo catalyst also serves to hydrolyze COS, thus removing a prior necessary reactor should a sweet synthesis gas shift take place. The large cost of the plant‘s components is offset by the generation of electricity through the gas turbine and steam turbines. An economic benefit is also associated with the production of elemental sulfur. To maximize efficiency of the plant, any recoverable heat is sent to the heat recovery steam generation unit Penn State University | 4.4 Gas Cleaning Unit 73PDF Image | GREAT NECK WATER POLLUTION CONTROL DISTRICT NASSAU COUNTY, NEW YORK MICROTURBINE INSTALLATION FEASIBILITY STUDY
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