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ACCEPTED MANUSCRIPT preheat the high pressure gas from point 15 to point 16 in the condensation cycle and from point 2 to point 4 in the gas cycle. As a consequence of this de-coupling optimum top pressures fall to about 100 bar for the condensation cycle and to about 40 bar for the gas cycle which implies obvious structural benefits and a simplified design for the compressor and the turbine of the gas cycle. Figure 11 reports cycle efficiency as a func- tion of compressor discharge pressure. At 600 ◦C top temperature optimum efficiency of the low pressure compound cycle is 55.3 % at 100 bar pump, 40 bar compressor discharge pressure which compares with 53.3 % of the high pressure compound cycle. At 700 ◦C top temperature efficiency reaches a remarkable 59.0 %. 5 Conclusions The thermodynamic analysis reported in the previous sections, with reference to Figure 12 too, suggests the following conclusions: 1. conventional power cycles, both Rankine and Brayton, can be adapted to the exploitation of the LNG thermal exergy with conversion effi- ciencies in the range 50 to 54 %. Rankine cycles must have a binary (steam–organic fluid) configuration. Nitrogen Brayton cycle, although less efficient than Rankine cycle at a fixed top temperature, has the 18 peer-00573462, version 1 - 4 Mar 2011PDF Image | Class Action Information Notice Ormat Technologies
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