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Modeling and optimization of natural gas liquefaction process for reducing energy consumption

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dc.contributor.authorJeon, G.-
dc.contributor.authorSong, Kiwook-
dc.contributor.authorLee, Chul-Jin-
dc.contributor.authorLim, Youngsub-
dc.contributor.authorHan, Chonghun-
dc.date.accessioned2021-09-29T04:40:16Z-
dc.date.available2021-09-29T04:40:16Z-
dc.date.issued2011-
dc.identifier.urihttps://scholarworks.bwise.kr/cau/handle/2019.sw.cau/50037-
dc.description.abstractBecause of limited fuel reserves, increasing prices of oil and growing concerns about the environment, natural gases are receiving attention as low-carbon, eco-friendly fuels. Natural gases have very large gas-to-liquid volume ratio, so the liquefaction process is essential to reduce volume of natural gases. Through the liquefaction process, natural gas becomes liquefied natural gas (LNG). LNG has a comparative advantage in terms of transport and safety. There are several kinds of natural gas liquefaction process. Among the liquefaction processes, propane pre-cooled mixed refrigerant (C3MR) process is the most widely used natural gas liquefaction process to date. In this study, a steady-state simulation of the C3MR process was performed using ASPEN HYSYS™ and it was optimized to reduce energy consumption. Optimization formulation is developed to minimize operating cost of the process. Optimization variables are temperature, pressure, and flow-rate of refrigerant and composition of the mixed refrigerant.-
dc.language영어-
dc.language.isoENG-
dc.titleModeling and optimization of natural gas liquefaction process for reducing energy consumption-
dc.typeArticle-
dc.identifier.bibliographicCitation11AIChE - 2011 AIChE Annual Meeting, Conference Proceedings-
dc.description.isOpenAccessN-
dc.identifier.scopusid2-s2.0-84863178478-
dc.citation.title11AIChE - 2011 AIChE Annual Meeting, Conference Proceedings-
dc.type.docTypeConference Paper-
dc.description.journalRegisteredClassscopus-
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