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dc.contributor.authorHamedi, Homa
dc.contributor.authorKarimi, Iftekhar A
dc.contributor.authorGundersen, Truls
dc.date.accessioned2020-01-02T12:22:06Z
dc.date.available2020-01-02T12:22:06Z
dc.date.created2018-09-14T11:41:49Z
dc.date.issued2018
dc.identifier.citationComputers and Chemical Engineering. 2018, 112 101-111.nb_NO
dc.identifier.issn0098-1354
dc.identifier.urihttp://hdl.handle.net/11250/2634601
dc.description.abstractNitrogen rejection processes are usually needed for two natural gas sources: sub-quality natural gas reserves and produced gas from enhanced oil/gas recovery technologies. The nitrogen content of natural gas in the former is usually constant during the project lifetime, but it varies from 5 to 70% during enhanced oil/gas recovery programs. This variation leads to different process flowsheets for nitrogen removal: single-column, double-column, three-column, and two-column processes. In order to determine which configuration is more suitable for a particular nitrogen content in a feed stream, we must minimize the energy requirement for each process. In this study, we merge all the four configurations into two categories: single-column and multi-column processes and then use the Particle Swarm Optimization algorithm to optimize process parameters for each process with the objective of energy consumption minimization. Finally, we use the exergy concept to analyze theoretically these different processes.nb_NO
dc.language.isoengnb_NO
dc.publisherElseviernb_NO
dc.rightsAttribution-NonCommercial-NoDerivatives 4.0 Internasjonal*
dc.rights.urihttp://creativecommons.org/licenses/by-nc-nd/4.0/deed.no*
dc.titleOptimal cryogenic processes for nitrogen rejection from natural gasnb_NO
dc.typeJournal articlenb_NO
dc.typePeer reviewednb_NO
dc.description.versionacceptedVersionnb_NO
dc.source.pagenumber101-111nb_NO
dc.source.volume112nb_NO
dc.source.journalComputers and Chemical Engineeringnb_NO
dc.identifier.doi10.1016/j.compchemeng.2018.02.006
dc.identifier.cristin1609501
dc.description.localcode© 2018. This is the authors’ accepted and refereed manuscript to the article. Locked until 6 April 2020 due to copyright restrictions. This manuscript version is made available under the CC-BY-NC-ND 4.0 license http://creativecommons.org/licenses/by-nc-nd/4.0/nb_NO
cristin.unitcode194,64,25,0
cristin.unitnameInstitutt for energi- og prosessteknikk
cristin.ispublishedtrue
cristin.fulltextpostprint
cristin.qualitycode2


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Attribution-NonCommercial-NoDerivatives 4.0 Internasjonal
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