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 possible explanation for the elevated water concentrations would be to maintain a lower operating temperature in order to prolong the life of the refractory or minimize damage to the slurry injector. 4.3.5 GE Reactor One of the largest coal IGCC plants is the TECO plant in Tampa Florida. Using a high temperature entrained flow reactor, the plant gasifies 2500 tons of coal per day (McDaniel 2002). This model maintains an operational range from 1300 - 1500 Celsius and five to eight megapascal (McDaniel 2002). Figure 41: GE Reactor In order to produce a net power output of 550 megawatts, two entrained flow reactors are needed in the design for the New Mexico plant. The two reactors will operate with an average cold gas efficiency ranging from 70 – 75%, supplying a synthesis gas capable of 1000 megawatts. This will also use the radiant synthesis gas cooler over the water quench systems which is typically used in the ammonia industry (Liu 2009). Radiant synthesis gas coolers are reported to have excellent performance and recover 10% of the fuels heating value in the form of pressurized steam (McDaniel 2002) 4.3.6 Oxygen and Water Supply A key to successful gasification is optimizing uses of partial oxidation and steam reformation in such a way that the synthesis gas achieves a high level of heating value within the limitations of the reactors design. Without diligent management of the oxygen and water streams, much of the carbon and hydrogen present in the coal will either form carbon dioxide and water or pass though unreacted with the slag. The New Mexico plant will require an average 4000 tons of oxygen per day. This amount should be raised or lowered to maintain a suitable temperature above the coal‘s ash fusion temperature. For this reason the operating equivalence ratio will be lower than the optimal ratios which hold higher cold gas efficiencies. Penn State University | 4.3 Gasifier 66

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