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dc.contributor.authorAndreasen, Glenn
dc.contributor.authorLarsen, Lars F.S.
dc.contributor.authorStoustrup, Jakob
dc.contributor.authorSkogestad, Sigurd
dc.date.accessioned2019-09-20T09:53:40Z
dc.date.available2019-09-20T09:53:40Z
dc.date.created2019-06-18T15:56:55Z
dc.date.issued2019
dc.identifier.issn1570-7946
dc.identifier.urihttp://hdl.handle.net/11250/2617997
dc.description.abstractIn this work, we analyze a generic supercritical CO2-refrigeration system with parallel compression, based on systems used for supermarket use. In order to maximize energy efficiency, this system has a “heat-recovery” function, in which part of the heat rejected at high pressure and temperature can be recovered to provide heating. Operating conditions and active constraints are strongly affected by seasonal requirements and ambient temperature. Thus, it is necessary to find a control structure that satisfies operational constraints and maintains (near-)optimal operation with different sets of active constraints. In this paper, we use a systematic procedure to define such control structure.nb_NO
dc.language.isoengnb_NO
dc.titleControl structure design for a CO2-refrigeration system with heat recoverynb_NO
dc.typeJournal articlenb_NO
dc.typePeer reviewednb_NO
dc.description.versionpublishedVersionnb_NO
dc.source.volume46nb_NO
dc.source.journalComputer-aided chemical engineeringnb_NO
dc.identifier.doi10.1016/B978-0-12-818634-3.50208-3
dc.identifier.cristin1705858
dc.description.localcodeThis article will not be available due to copyright restrictions (c) 2019 by Elseviernb_NO
cristin.unitcode194,66,30,0
cristin.unitnameInstitutt for kjemisk prosessteknologi
cristin.ispublishedtrue
cristin.fulltextpreprint
cristin.qualitycode1


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