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Energy Conversion Systems

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Energy Conversion Systems ( energy-conversion-systems )

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Chapter 7 turbine eff = 0.80 g Energy Conversion Systems – Options and Issues 14-1 in underground HXer 3 8s89 6 1214 5 turbine eff = 0.80 4 T = 400°C 1 1 2s 2 turbine eff = 0.80 quality @ 2 = 0.9 13 7 11 pump eff = 0.80 3 T = 50°C 10s 10 P =0.123b Figure 7.12 Processes for triple­expansion power plant (see Figure 7.11 for location of state points). Entropy P1 7­18 2 Temperature P Table 7.6 Results of triple­expansion analysis for an inlet temperature of 400°C. P1 P2 T2 �w �w wnet qIN η TP th MPa MPa °C kJ/kg 3 kJ/kg kW/(kg/s) kW/(kg/s) % 25 14.6 340.0 759.1 31.8 727.3 2301.3 31.6 27 19.05 361.6 699.3 34.3 665.0 2149.0 30.9 The results for the triple­expansion system are shown in Tables 7.6 and 7.7. It is evident that this is a very efficient means of generating electricity. The utilization efficiency is about 67%, and the thermal efficiency is about 31%. Given the high specific net power, it would take only about 15 kg/s of EGS fluid flow to produce 10 MW in either case. Such flow rates have already been demonstrated at EGS reservoirs in Europe. For inlet pressures above 27 MPa, there are no solutions that satisfy our constraints with the triple­expansion system. Even the solution at 27 MPa requires the cyclone separator to operate close to the critical point, thereby diminishing its effectiveness. The density difference between the liquid and vapor phases is not as pronounced as at separator conditions found in a typical geothermal flash plant: Here, the liquid­to­vapor density ratio is only 3.5 as compared with 172.5 in a 1 MPa separator.

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