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dc.contributor.authorJahanshahi, Esmaeil
dc.contributor.authorSkogestad, Sigurd
dc.contributor.authorGrøtli, Esten Ingar
dc.date.accessioned2017-10-20T09:21:01Z
dc.date.available2017-10-20T09:21:01Z
dc.date.created2013-09-20T08:58:37Z
dc.date.issued2013
dc.identifier.citationElsevier IFAC Publications / IFAC Proceedings series. 2013, 301-306.nb_NO
dc.identifier.issn1474-6670
dc.identifier.urihttp://hdl.handle.net/11250/2461219
dc.description.abstractActive control of the production choke valve is the recommended solution to prevent severe slugging flow conditions at offshore oilfields. The slugging flow constitutes an unstable and highly nonlinear system; the gain of the system changes drastically for different operating points. Although PI and PID controllers are the most widely used controllers in the industry, they need to be re-tuned for different operating conditions. The focus of this paper is to design a model-based nonlinear controller in order to counteract nonlinearities of the system. Feedback linearization based on the riser-base pressure and the topside pressure was used for the control design. Stability and convergence of the closed-loop system was verified in theory as well as by experiments on a test rig.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.titleNonlinear model-based control of two-phase flow in risers by feedback linearizationnb_NO
dc.typeJournal articlenb_NO
dc.description.versionacceptedVersionnb_NO
dc.source.pagenumber301-306nb_NO
dc.source.journalElsevier IFAC Publications / IFAC Proceedings seriesnb_NO
dc.identifier.doi10.3182/20130904-3-FR-2041.00041
dc.identifier.cristin1050715
dc.relation.projectNorges forskningsråd: 192427nb_NO
dc.description.localcode© 2016. 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.unitcode194,66,30,0
cristin.unitcode194,63,25,0
cristin.unitnameInstitutt for kjemisk prosessteknologi
cristin.unitnameInstitutt for teknisk kybernetikk
cristin.ispublishedtrue
cristin.fulltextpostprint
cristin.qualitycode0


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Attribution-NonCommercial-NoDerivatives 4.0 Internasjonal
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