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dc.contributor.authorWillersrud, Anders
dc.contributor.authorImsland, Lars Struen
dc.contributor.authorHauger, Svein Olav
dc.contributor.authorKittilsen, Pål
dc.date.accessioned2017-11-16T08:36:43Z
dc.date.available2017-11-16T08:36:43Z
dc.date.created2013-01-10T22:42:40Z
dc.date.issued2013
dc.identifier.citationJournal of Process Control. 2013, 23 (2), 215-223.nb_NO
dc.identifier.issn0959-1524
dc.identifier.urihttp://hdl.handle.net/11250/2466573
dc.description.abstractThe topic of this paper is the application of nonlinear model predictive control (NMPC) for optimizing control of an offshore oil and gas production facility. Of particular interest is the use of NMPC for direct short-term production optimization, where two methods for (one-layer) production optimization in NMPC are investigated. The first method is the unreachable setpoints method where an unreachable setpoint is used in order to maximize oil production. The ideas from this method are combined with the exact penalty function for soft constraints in a second method, named infeasible soft-constraints. Both methods can be implemented within standard NMPC software tools. The case-study first looks into the use of NMPC for ‘conventional’ pressure control, where disturbance rejection of time-varying disturbances (caused, e.g., by the ‘slugging’ phenomenon) is an issue. Then the above two methods for production optimization are employed, where both methods find the economically optimal operating point. Two different types of reservoir models are studied, using rate-independent and rate-dependent gas/oil ratios. These models lead to different types of optimums. The relative merits of the two methods for production optimization, and advantages of the two one-layer approaches compared to a two-layer structure, are discussed.nb_NO
dc.language.isoengnb_NO
dc.publisherElseviernb_NO
dc.titleShort-term production optimization of offshore oil and gas production using nonlinear model predictive controlnb_NO
dc.typeJournal articlenb_NO
dc.description.versionsubmittedVersionnb_NO
dc.source.pagenumber215-223nb_NO
dc.source.volume23nb_NO
dc.source.journalJournal of Process Controlnb_NO
dc.source.issue2nb_NO
dc.identifier.doi10.1016/j.jprocont.2012.08.005
dc.identifier.cristin985831
dc.relation.projectNorges forskningsråd: 210432nb_NO
dc.description.localcodeThis is a submitted manuscript of an article published by Elsevier Ltd in Journal of Process Control, 6 September 2012.nb_NO
cristin.unitcode194,63,25,0
cristin.unitnameInstitutt for teknisk kybernetikk
cristin.ispublishedtrue
cristin.fulltextoriginal
cristin.qualitycode2


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