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dc.contributor.authorDeng, Han
dc.contributor.authorHagen, Brede
dc.contributor.authorNikolaisen, Monika
dc.contributor.authorAndresen, Trond
dc.date.accessioned2020-09-16T13:07:26Z
dc.date.available2020-09-16T13:07:26Z
dc.date.created2020-08-19T14:49:06Z
dc.date.issued2020
dc.identifier.isbn978-2-36215-038-8
dc.identifier.urihttps://hdl.handle.net/11250/2678108
dc.description.abstractThis study applies three methods for design of Rankine cycles utilizing waste heat in the oil and gas industry. The methods differ in the level of detail of heat exchanger model applied and in the flexibility with respect to heat exchanger design. All the methods involve formulating a constrained optimization problem with the objective of maximizing net power output, but vary in the constraints related to limit the size of the heat exchangers. The cycles with using two working fluids, n-butane and a n-butane/n-pentane mixture (30%/70%), are compared for each method. The methods yield different results; both the maximized net power output and the best-performing working fluid differ with respect to the method used, emphasizing the importance of method selection.en_US
dc.language.isoengen_US
dc.publisherInternational Institute of Refrigeration (IIR)en_US
dc.relation.ispartofIIR Rankine Conference 2020
dc.titleComparing Three Methods for Design Analyses of Rankine Cycle for Waste Heat Recovery from Natural Gas Compressionen_US
dc.typeChapteren_US
dc.description.versionacceptedVersionen_US
dc.identifier.doi10.18462/iir.rankine.2020.1149
dc.identifier.cristin1824108
dc.relation.projectNorges forskningsråd: 255016en_US
dc.relation.projectNorges forskningsråd: 257632en_US
dc.description.localcodeThis article will not be available due to copyright restrictions (c) 2020 by International Institute of Refrigerationen_US
cristin.ispublishedtrue
cristin.fulltextpostprint
cristin.qualitycode1


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