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ACCEPTED MANUSCRIPT terminal of 8 Gm3/year gaseous methane capacity (which could feed at least 5000 MWe combined cycle plant) has the potential of generating about 150 MWe in a high efficiency cycle using the LNG as heat sink. It is not surprising that most existing energy recovery plants employ an organic fluid Rankine cycle since, besides direct expansion, this is a practical, straightforward way of exploiting the LNG thermal exergy. Owing to the cryogenic temperatures envisaged the direct use of steam is banned. With reference to condensing cryogenic cycles both hydrocarbons and refrigerants exhibit a limited thermal stability besides some technical and environmental drawback. Carbon dioxide, on the contrary, while lending itself to the implementation of a condensing cycles, is stable up to very high temperatures, is non flammable, non toxic, non corrosive, inexpensive and was used extensively in the past, for decades, by the power industry in the Advanced Gas Cooled Reactors (AGR) at a top temperature of 650 ◦C. In principle it could represent an ideal option for low temperature uses as water it is at ambient temperatures. A limit of CO2 as a working fluid is its triple point at -57 ◦C which, in general, prevents its use at even lower temperatures. Carbon dioxide power cycles were extensively investigated in the past for applications where the final cooling of the working medium in a condenser takes place just below the critical temperature of the substance (31 ◦C, ref. [4, 5, 6, 7]). In these conditions waste heat rejection takes place near the 6 peer-00573462, version 1 - 4 Mar 2011PDF Image | Class Action Information Notice Ormat Technologies
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