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Chapter 7 Energy Conversion Systems – Options and Issues Table 7.10 Electrical demand and supply at MIT – November 18, 2005. Demand load, kWe Cogen power, kWe NSTAR power, kWe 24,087 22,100 2,060 Table 7.11 Steam demand and supply at MIT – November 18, 2005. Demand load, lbm/h HRSG output, lbm/h Demand load, kg/s HRSG output, kg/s 135,059 135,059 17.017 17.017 The actual performance data for the MITCOGEN 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. MIT COGENERATION SYSTEM 724 ENERGY FLOW DIAGRAM No. 6 Oil G Cambridge Steam (Not In Service) 200 PSI Steam Superheated Main St. @ RR East Gate BOILER BOILER BOILER 3/4 5 7/8 Refrigeration Cooling Tower Campus Gas 80 KPPH 100 KPPH 60 KPPH Water Ea. Ea. 2x50 KPPH No. 2 Oil HT Water Steam Turbine Driven to HRSG BOILER 102,000 PPH Unfired M Chillers 1-2 1500 TONS Ea. NW30, W79 Chiller 3 3500 TONS NW14 Combustion 6 168,000 PPH Fired Chiller 4 4000 TONS Conversion Plant Chillers 5-6 5000 TONS Ea. 42o Chilled Water Figure 7.17 Energyflow diagram for MITCOGEN system. Cooling Tower NSTAR 13.8 KV Electric Driven 68-E17-E18-E19 Chillers 1-2-3 1000 TONS Ea. @ E40 ECCWP Chillers 7-8 2000 TONS Ea. @ N16A CUP Turbine 20.4 MW (ISO) 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 42o Chilled Water East Campus NOTE: Nameplate capacities shown. Actual capability depends on equipment and ambient conditions, etc.PDF Image | Energy Conversion Systems
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