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dc.contributor.authorTaejong, Yu
dc.contributor.authorKim, Donghoi
dc.contributor.authorGundersen, Truls
dc.contributor.authorLim, Youngsub
dc.date.accessioned2023-03-16T09:54:53Z
dc.date.available2023-03-16T09:54:53Z
dc.date.created2022-09-12T15:20:30Z
dc.date.issued2022
dc.identifier.citationComputer-aided chemical engineering. 2022, 49 1081-1086.en_US
dc.identifier.issn1570-7946
dc.identifier.urihttps://hdl.handle.net/11250/3058682
dc.description.abstractAs regulation of ship emission established, using liquefied natural gas (LNG) as ship fuel is one of the method to reduce ship emission. For LNG carrier, boil-off gas (BOG) generated from the storage tank can be used as fuel and it is economical to adopt BOG re-liquefaction system on the vessel. In this study, we investigate the feasibility of hydro- fluoroolefins (HFO) refrigerants in the BOG re-liquefaction system. We simulate BOG re-liquefaction system and optimize it to minimize energy consumption. Then, the global warming potential(GWP) generation during lifecycle of the ship is estimated. As the results, HFO refrigerants has similar performance in BOG re-liquefaction system in terms of energy consumption compared to hydrocarbon refrigerants. In case using HFO refrigerants, the specific power consumption (SPC) of re-liquefaction process is 0.479 kWh/kg and in case using hydrocarbon refrigerants it is 0.471 kWh/kg. However, although HFO refrigerants has lower GWP than hydrocarbons, the total GWP generation is larger than when using hydrocarbons due to GWP generation caused by CO2 emission. © 2022 Elsevier B.V.en_US
dc.description.abstractThe study on feasibility of HFO refrigerants in BOG re-liquefaction processen_US
dc.language.isoengen_US
dc.publisherElsevieren_US
dc.titleThe study on feasibility of HFO refrigerants in BOG re-liquefaction processen_US
dc.title.alternativeThe study on feasibility of HFO refrigerants in BOG re-liquefaction processen_US
dc.typePeer revieweden_US
dc.typeJournal articleen_US
dc.description.versionpublishedVersionen_US
dc.rights.holderThis version will not be available due to the publisher's copyright.en_US
dc.source.pagenumber1081-1086en_US
dc.source.volume49en_US
dc.source.journalComputer-aided chemical engineeringen_US
dc.identifier.doi10.1016/B978-0-323-85159-6.50180-9
dc.identifier.cristin2050912
cristin.ispublishedtrue
cristin.fulltextpostprint
cristin.qualitycode1


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