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dc.contributor.authorKim, Donghoi
dc.contributor.authorGiametta, Roxane Edith Helene
dc.contributor.authorGundersen, Truls
dc.date.accessioned2020-03-25T11:00:31Z
dc.date.available2020-03-25T11:00:31Z
dc.date.created2019-01-22T15:40:35Z
dc.date.issued2018
dc.identifier.citationIndustrial & Engineering Chemistry Research. 2018, 57 (17), 5914-5923.en_US
dc.identifier.issn0888-5885
dc.identifier.urihttps://hdl.handle.net/11250/2648546
dc.description.abstractOne of the solutions to utilizing liquefied natural gas (LNG) cold energy at import terminals is supplying it to an air separation unit (ASU), replacing an external refrigeration process and reducing the power consumption. Thus, two different options for the integration of a novel single column ASU process with LNG vaporization have been developed to achieve optimal use of the cold energy. After optimization of the heat integration part, both energy and exergy analyses have been performed to evaluate and compare the two integration options. The results indicate that the single column ASU process, precooled by an LNG stream, has a lower specific power consumption (0.281 kWh/kg) than the integration option with a liquid nitrogen production cycle (0.310 kWh/kg). The integration option with precooling also delivers a higher exergy efficiency for different LNG pumping pressure levels compared to the alternative with a liquid nitrogen production cycle.en_US
dc.language.isoengen_US
dc.publisherAmerican Chemical Societyen_US
dc.titleOptimal Use of Liquefied Natural Gas (LNG) Cold Energy in Air Separation Unitsen_US
dc.typePeer revieweden_US
dc.typeJournal articleen_US
dc.description.versionacceptedVersionen_US
dc.source.pagenumber5914-5923en_US
dc.source.volume57en_US
dc.source.journalIndustrial & Engineering Chemistry Researchen_US
dc.source.issue17en_US
dc.identifier.doi10.1021/acs.iecr.7b04282
dc.identifier.cristin1663196
dc.description.localcode© American Chemical Society 2018. This is the authors accepted and refereed manuscript to the article. The final article is available at DOIen_US
cristin.unitcode194,64,25,0
cristin.unitnameInstitutt for energi- og prosessteknikk
cristin.ispublishedtrue
cristin.fulltextpreprint
cristin.qualitycode2


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