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ACCEPTED MANUSCRIPT is 52.3 %. A more straightforward solution consisting of a standard, re–heat steam cycle condensing at 30 ◦C followed by a n-butane cycle vaporizing at 20 ◦C and condensing at -50 ◦C according to the same computing program would exhibit a slightly better overall efficiency (53.7 %) at the cost of a complex vacuum section and of a second steam superheating (42.3 % steam, 19.7 % n-butane cycle efficiency). 2.2 Brayton cycle system The successfull more than decennial experience of closed cycle gas turbines ([13, 14]) represents a sound basis for the extension of this concept to cryo- genic temperatures. A detailed solution for one such plant serving an LNG terminal is reported in [3]. Nitrogen with a very small oxygen addition is be- lieved to be the best working fluid. Top temperatures are limited to 700–800 ◦C owing to material problems in the primary heater. The cooling charac- teristics of LNG which must be heated from -160 ◦C to ambient temperature suggest the adoption of a simple, non–intercooled, regenerative cycle. The overall maximum to minimum temperature ratio (τ = Tmax/Tmin) which was around 3.4 in historical plants [13] in the peculiar LNG application rises to about 7 ∗ with a strong reduction in compressor work and a substantial gain in efficiency (from historical values of about 30 % to well above 50 %). The ∗In the case of an open combined cycle with an LNG heat sink τ exceeds 11.0. 10 peer-00573462, version 1 - 4 Mar 2011PDF Image | Class Action Information Notice Ormat Technologies
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