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Supercritical Carbon Dioxide Circulated EGS Combined with IGCC in New Mexico molecular hydrogen and carbon monoxide. This is due to the heat of combustion possible from both species. Therefore, the formation of these two molecules holds high priority.CO and H2 formation from coal is a combination of exothermic and endothermic reactions with oxygen and water. The most pertinent of these are listed below. 4.1 4.2 4.3 4.4 4.5 4.6 Both oxygen and water streams must be carefully adjusted to ensure that the formation of hydrogen gas and carbon monoxide is thermodynamically favored. Using relevant reactions listed in the GRI mechanism, a series of calculations were performed to test the theoretical effects of oxygen and water inputs on the thermodynamic equilibrium concentrations. Synthesis gas composition depends on the internal reactor conditions and the concentrations of the reactants. One aspect that sets the entrained flow reactor apart is the elevated operating temperature. This is a result of operating above the coal‘s ash fusion temperature. A combination of this dramatic increase in operating temperature and a highly pressurized reactor will greatly increases the coal‘s chemical reaction rates (Liu 2009). Therefore, the assumption that gas-phase equilibrium is reached will be implemented when testing the reactors sensitivity to select parameters. Since coal is a complex heterogeneous solid, the fuel input needed to be simplified to conduct reasonable calculations. Therefore the molecule CH was used to represent the coal feed. The oxidizing stream consisted entirely of oxygen accomplished with an air separation unit. Actual reactor conditions and synthesis gas composition was collected from the final technical report on the Tampa Florida IGCC plant owned by TECO electric. The typical reactor conditions of the TECO plant were mimicked in the following cases studies with an initial reactor temperature of 1300 Celsius and five megapascals (Mc Daniel 2002). In each case, both the mole fractions of oxygen or water were varied over a select range and equilibrium concentrations were then calculated. The estimates on mass and energy flows through the theoretical system were calculated to estimate the quantities of reactants and theoretical efficiencies of the New Mexico gasifiers. Coal composition Illinois No. 6(Herrin) is used as a basis for calculations and synthesis gas Penn State University | 4.3 Gasifier 61PDF Image | GREAT NECK WATER POLLUTION CONTROL DISTRICT NASSAU COUNTY, NEW YORK MICROTURBINE INSTALLATION FEASIBILITY STUDY
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