GREAT NECK WATER POLLUTION CONTROL DISTRICT NASSAU COUNTY, NEW YORK MICROTURBINE INSTALLATION FEASIBILITY STUDY

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GREAT NECK WATER POLLUTION CONTROL DISTRICT NASSAU COUNTY, NEW YORK MICROTURBINE INSTALLATION FEASIBILITY STUDY ( great-neck-water-pollution-control-district-nassau-county-ne )

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Supercritical Carbon Dioxide Circulated EGS Combined with IGCC in New Mexico One important difference in the effects of water concentration on hydrogen species verses carbon species is the water‘s effect on heating value. Unlike Figure 38, every addition of water lowers the equilibrium heating value that is available from carbon species. Though this is often done intentionally in later stages such as the water gas shift reactor, excess concentrations of water have the potential to be counterproductive. Endothermic reactions, like the water gas shift, in excess can slow down the coal gasification kinetics which may decrease the overall percent of carbon conversion. 4.3.4 Coal Water Slurry Preparation To accomplish the required power output, the system will gasify an average of 5500 pound tons of coal per day. Using local railways, the necessary coal can be procured from upstate coal mines and avoid costly transportation methods. Likewise, the coal handling facilities will need coal storage, crushing and slurry prep stations that can accommodate this magnitude of coal. One distinct advantage to the Texaco design is its ability to gasify all ranks of coal (Jeffrey, NETL Reference Shelf). This means the plant will have more flexibility in relation to fuel supplies in the coming decades. However, any given coal feed dictates the reactors operational parameters and limits the power output. For this reason, the plant will place preference on local bituminous coal. This coal type is successfully used in the Tampa Florida IGCC plant with high efficiency results (McDaniel 2002). The coal water slurry concentration will maintain the ratio of 63% solids. This is the recommended parameters to balance the lifespan of the reactors lining with a profitable power output (McDaniel 2002). This goes past the optimal ratio if governed solely by thermodynamics as shown in Figure 40 Figure 40: Initial Mole Fraction of water vs. KJ/mole of Synthesis gas Penn State University | 4.3 Gasifier 65

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