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ACCEPTED MANUSCRIPT 1 Introduction All over the world natural gas transportation is increasingly relying on lique- faction and conveyance by specialized tankers. For structural reasons LNG is shipped basically at atmospheric pressure at a temperature of about -160 ◦C. At the receiving terminal a large amount of cryogenic cold is available which, in general, is lost since LNG is directly vaporized using sea water as heat source. Sometimes, mainly in Japan, LNG physical exergy is used for technolog- ical (air separation, CO2 liquefaction, ...) or for power uses. In the latter case a propane or a refrigerant Rankine cycle using sea water as heat source and LNG as heat sink generates electricity without any fuel consumption. All existing power plants of this kind (around fifteen) employ a small frac- tion of the overall LNG cooling capability available at the site (net outputs limited to a maximum of 9400 kW). Often the net power obtained from the thermodynamic cycle is supplemented by an additional contribution due to the direct expansion of methane which is heated at a pressure greater than that requested by the final user and eventually expanded [1, 2]. Envisaging the use of a high temperature conversion cycle (for example a closed nitrogen Brayton cycle, ref. [3]) the amount of power which can be generated increases greatly. As a first approximation a typical LNG import 5 peer-00573462, version 1 - 4 Mar 2011PDF Image | Class Action Information Notice Ormat Technologies
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