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dc.contributor.authorHalvorsen, Ivar Johan
dc.contributor.authorDejanovic, Igor
dc.contributor.authorOlujic, Zarko
dc.contributor.authorSkogestad, Sigurd
dc.date.accessioned2019-02-25T12:50:39Z
dc.date.available2019-02-25T12:50:39Z
dc.date.created2018-11-15T15:06:23Z
dc.date.issued2018
dc.identifier.citationChemical Engineering Transactions. 2018, 69 829-834.nb_NO
dc.identifier.issn1974-9791
dc.identifier.urihttp://hdl.handle.net/11250/2587250
dc.description.abstractIn order to meet current carbon dioxide emissions reduction challenges, natural gas processing and refining industries have to find the ways to minimize energy requirements of distillation operations. Building on foundations lied down in a preceding effort, this paper shows that this could be achieved in a cost-effective way in natural gas liquids fractionation plants and that a conventional demethanizer column combined with either a thermally coupled direct sequence of deethanizer and propane-butane recovery columns or a dividing wall column produces expected savings in capital and hot utilities costs as compared to conventional direct sequence, without any temperature penalty on cold utilities side. The choice between available options will largely depend on important process considerations that may differ for offshore and onshore plants to the extent depending on specific site requirements.nb_NO
dc.language.isoengnb_NO
dc.publisherAIDIC Servizinb_NO
dc.titleDividing wall columns for natural gas liquefaction plantsnb_NO
dc.typeJournal articlenb_NO
dc.typePeer reviewednb_NO
dc.description.versionpublishedVersionnb_NO
dc.source.pagenumber829-834nb_NO
dc.source.volume69nb_NO
dc.source.journalChemical Engineering Transactionsnb_NO
dc.identifier.doi10.3303/CET1869139
dc.identifier.cristin1631088
dc.description.localcodeCopyright © 2018, AIDIC Servizi S.r.l.nb_NO
cristin.unitcode194,66,30,0
cristin.unitnameInstitutt for kjemisk prosessteknologi
cristin.ispublishedtrue
cristin.fulltextoriginal
cristin.qualitycode1


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