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dc.contributor.authorKrishnamoorthy, Dinesh
dc.contributor.authorJahanshahi, Esmaeil
dc.contributor.authorSkogestad, Sigurd
dc.date.accessioned2019-03-28T12:19:44Z
dc.date.available2019-03-28T12:19:44Z
dc.date.created2019-01-09T23:36:48Z
dc.date.issued2019
dc.identifier.citationIndustrial & Engineering Chemistry Research. 2019, 58 (1), 207-216.nb_NO
dc.identifier.issn0888-5885
dc.identifier.urihttp://hdl.handle.net/11250/2592207
dc.description.abstractThis paper presents a new feedback real-time optimization (RTO) strategy for steady-state optimization that directly uses transient measurements. The proposed RTO scheme is based on controlling the estimated steady-state gradient of the cost function using feedback. The steady-state gradient is estimated using a novel method based on linearizing a nonlinear dynamic model around the current operating point. The gradient is controlled to zero using standard feedback controllers, for example, a PI-controller. In the case of disturbances, the proposed method is able to adjust quickly to the new optimal operation. The advantage of the proposed feedback RTO strategy compared to standard steady-state real-time optimization is that it reaches the optimum much faster and without the need to wait for steady-state to update the model. The advantage, compared to dynamic RTO and the closely related economic NMPC, is that the computational cost is considerably reduced and the tuning is simpler. Finally, it is significantly faster than classical extremum-seeking control and does not require the measurement of the cost function and additional process excitation.nb_NO
dc.language.isoengnb_NO
dc.publisherAmerican Chemical Societynb_NO
dc.relation.urihttps://pubs.acs.org/doi/10.1021/acs.iecr.8b03137
dc.titleFeedback Real-Time Optimization Strategy Using a Novel Steady-state Gradient Estimate and Transient Measurementsnb_NO
dc.typeJournal articlenb_NO
dc.typePeer reviewednb_NO
dc.description.versionacceptedVersionnb_NO
dc.source.pagenumber207-216nb_NO
dc.source.volume58nb_NO
dc.source.journalIndustrial & Engineering Chemistry Researchnb_NO
dc.source.issue1nb_NO
dc.identifier.doi10.1021/acs.iecr.8b03137
dc.identifier.cristin1653666
dc.relation.projectNorges forskningsråd: 237893nb_NO
dc.description.localcode© American Chemical Society 2018. This is the authors accepted and refereed manuscript to the article. Locked until 3.12.2019 due to copyright restrictions.nb_NO
cristin.unitcode194,66,30,0
cristin.unitnameInstitutt for kjemisk prosessteknologi
cristin.ispublishedtrue
cristin.fulltextpostprint
cristin.qualitycode2


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