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Chapter7 EnergyConversionSystems–OptionsandIssues The actual performance data for the MIT-COGEN plant were obtained from the plant engineers (Cooper, 2005). Table 7.12 shows the minimum, maximum, and average monthly demands for electricity, chiller cooling, and steam. Table 7.13 gives the annual amounts for these quantities, and Table 7.14 converts these values to instantaneous power requirements based on monthly averages. Table 7.10 Electrical demand and supply at MIT – November 18, 2005. Table 7.11 Steam demand and supply at MIT – November 18, 2005. Demand load, kWe Cogen power, kWe NSTAR power, kWe 24,087 22,100 2,060 Demand load, lbm/h HRSG output, lbm/h Demand load, kg/s HRSG output, kg/s 135,059 135,059 17.017 17.017 MIT COGENERATION SYSTEM Cambridge Steam (Not In Service) ENERGY FLOW DIAGRAM Main St. @ RR Cooling Tower Water East Gate Campus NW14 Conversion Plant No. 6 Oil Gas No. 2 Oil BOILER 3/4 80 KPPH Ea. Combustion Turbine 20.4 MW (ISO) BOILER 5 100 KPPH HRSG BOILER 6 G BOILER 7/8 60 KPPH Ea. 102,000 PPH Unfired 168,000 PPH Fired 200 PSI Steam Superheated Refrigeration 2x50 KPPH HT Water to NW30, W79 Steam Turbine Driven Chillers 1-2 Chiller 3 Chiller 4 Chillers 5-6 1500 TONS Ea. 3500 TONS 4000 TONS 5000 TONS Ea. 42o Chilled Water Cooling Tower Water 68-E17-E18-E19 East Campus M Electric Driven Chillers 1-2-3 1000 TONS Ea. @ E40 ECCWP NSTAR 13.8 KV Chillers 7-8 2000 TONS Ea. @ N16A CUP 42o Chilled Water 43.8 MVA normal continuous - 4 cables 37.4 MVA 12 hr emergency - 3 cables 13.8 KV & 2.4 KV Distributed to Campus NOTE: Nameplate capacities shown. Actual capability depends on equipment and ambient conditions, etc. 7-24 Figure 7.17 Energy-flow diagram for MIT-COGEN system.PDF Image | The Future of Geothermal Energy
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