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 At this time a complete cost analysis for the brayton cycle turbine and associated heat exchanger proposed for this project cannot be completed because the turbine is not yet commercially available. Through up scaling of the documented turbine at SNL it is possible to arrive at a projected 15MW of power production for 1000kg/s of scCO2. This will result in approximately 5.26x107 KWh of production. In addition to this value there will be an additional 153MW from the heat exchanger associated with the brayton cycle turbine which will result in approximately 5.4x108 KWh of production. These are rough numbers that will need to be further constrained via further reservoir simulation and efficiency data for the turbine at the proposed conditions. However, these values are promising. Table 15: Double Flash Cost and Production Estimations Working Fluid Water Water Water Water Water Water Water Water Water Flow Energy rate Rate Effective Plant Energy Rate Cost Eff(0.50) [MW] $/kw Operational Cost T_in T_out [C] [C] 210 15 210 15 210 15 210 15 210 15 210 15 210 15 210 15 210 15 This analysis is Cost]. By varying the flow rates of produced water and the resulting KWH calculations the economic feasibility of the double flash geothermal power plant can be determined independent of simulated production rates. KWH [292 days] 29,240 73,103 146,207 219,311 292,415 438,623 584,831 731,039 877,247 [kg/s] [MW] 10 8 4 1881 Plant Cost $ cents/kwh 25 20 50 41 75 63 100 83 150 125 200 166 10 1838 21 1771 31 1707 41 1649 63 1541 83 1446 7,847,250 19,175,700 36,948,300 53,448,000 68,794,000 96,453,800 120,698,000 142,172,500 161,417,500 2 1.925 1.85 1.775 1.7 1.625 1.55 1.475 1.4 250 300 208 104 1363 250 125 1289 based upon calculations from MIT (2006) [Plant Cost] and Sanyal (2004) [O&M Penn State University | 9.4 Gravity Separation- scCO2-Double Flash Conversion System 109

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