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dc.contributor.authorKvernland, Martin Krister
dc.contributor.authorHalvorsen, Ivar J.
dc.contributor.authorSkogestad, Sigurd
dc.date.accessioned2017-10-17T07:10:56Z
dc.date.available2017-10-17T07:10:56Z
dc.date.created2011-01-11T10:37:52Z
dc.date.issued2010
dc.identifier.citationElsevier IFAC Publications / IFAC Proceedings series. 2010, 539-544.nb_NO
dc.identifier.issn1474-6670
dc.identifier.urihttp://hdl.handle.net/11250/2460473
dc.description.abstractThis is a simulation study on controlling a Kaibel distillation column with model predictive control (MPC). A Kaibel distillation column has several advantages compared with conventional binary column setups. The Kaibel column separates a feed stream into four product streams using only a single column shell. The distillation process is a multivariable process which leads to a multivariable control problem. The objective for optimal operation of the column is chosen to be minimization of the total impurity flow. An off-line optimization on a mathematical model leads to temperature setpoints to be used by a controller. An MPC generally obtain less total impurity flow compared to conventional decentralized control when the distillation column is exposed to disturbances. It also counteract process interactions better than decentralized control.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.titleModel Predictive Control of a Kaibel Distillation Columnnb_NO
dc.typeJournal articlenb_NO
dc.typePeer reviewednb_NO
dc.description.versionacceptedVersionnb_NO
dc.source.pagenumber539-544nb_NO
dc.source.journalElsevier IFAC Publications / IFAC Proceedings seriesnb_NO
dc.identifier.doi10.3182/20100705-3-BE-2011.00092
dc.identifier.cristin521565
dc.description.localcode© 2010. This is the authors’ accepted and refereed manuscript to the article. 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.unitcode194,63,25,0
cristin.unitcode194,66,30,0
cristin.unitnameInstitutt for teknisk kybernetikk
cristin.unitnameInstitutt for kjemisk prosessteknologi
cristin.ispublishedtrue
cristin.fulltextpostprint
cristin.qualitycode1


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Attribution-NonCommercial-NoDerivatives 4.0 Internasjonal
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