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Supercritical Carbon Dioxide Circulated EGS Combined with IGCC in New Mexico Figure 42: Physical Solvent AGR Process Flow The dual stage Selexol process removes 99.7% of the H2S from the synthesis gas stream which is then sent to the Claus Plant for further processing (Black, 2010). 90.3% of the CO2 is stripped and removed for the acid gas stream then sent to the Enhanced Geothermal System (EGS) plant. The CO2 stream sent to the EGS is composed of 99.48% CO2 (Black, 2010). The H2-rich synthesis gas stream contains 91.4% hydrogen and is sent to the gas turbine to be utilized for electricity generation (Black, 2010). 4.4.5 Claus Plant The Claus process converts H2S to elemental sulfur. The elemental sulfur can be sold to the chemical industry to generate further income for the overall IGCC plant. The following reactions occur in the conversion of H2S: 4.8 4.9 Equation 4.8 shows the stoichiometry for the combustion of H2S to form SO2 which is required for the 2nd reaction (Equation 4.9). The reaction shown by equation is an equilibrium reaction thus it follows L‘Chatlier‘s Principle. The Claus process works in many stages including a catalytic stage which consists of gas preheat a catalytic reactor, and a sulfur condenser (Black, 2010). Oxygen is required from the Air Separation Unit (ASU) for the first part of the H2S combustion inside the furnace (Black, 2010). Temperatures typically range from 1100 to 1400°C in the furnace but higher conversions are achieved at higher temperatures (Klara, 2007). Penn State University | 4.4 Gas Cleaning Unit 70PDF Image | GREAT NECK WATER POLLUTION CONTROL DISTRICT NASSAU COUNTY, NEW YORK MICROTURBINE INSTALLATION FEASIBILITY STUDY
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