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dc.contributor.authorCetinkaya, Sevil
dc.contributor.authorZeybek, Zehra
dc.contributor.authorHapoglu, Hale
dc.contributor.authorAlpbaz, Mustafa
dc.date.accessioned2019-07-27T12:10:23Z
dc.date.accessioned2019-07-28T10:18:03Z
dc.date.available2019-07-27T12:10:23Z
dc.date.available2019-07-28T10:18:03Z
dc.date.issued2006
dc.identifier.issn0098-1354
dc.identifier.issn1873-4375
dc.identifier.urihttps://dx.doi.org/10.1016/j.compchemeng.2006.04.002
dc.identifier.urihttps://hdl.handle.net/20.500.12418/10800
dc.descriptionWOS: 000239163300001en_US
dc.description.abstractIn this work, fuzzy-relational models-dynamics matrix control (Fuzzy-DMC) was applied to the free radical solution polymerization of styrene in a jacketted batch reactor and its performance was examined to reach the required monomer conversion, molecular weight and chain length in a minimum time. The reactor temperature was controlled by manipulating the heat-input to the reactor. The performance of the Fuzzy-DMC controller was compared with that of the nonlinear generalized predictive control (NLGPC). (c) 2006 Elsevier Ltd. All rights reserved.en_US
dc.language.isoengen_US
dc.publisherPERGAMON-ELSEVIER SCIENCE LTDen_US
dc.relation.isversionof10.1016/j.compchemeng.2006.04.002en_US
dc.rightsinfo:eu-repo/semantics/closedAccessen_US
dc.subjectdynamic matrix controlen_US
dc.subjectfuzzy-relational modelsen_US
dc.subjectpolymerizationen_US
dc.titleOptimal temperature control in a batch polymerization reactor using fuzzy-relational models-dynamics matrix controlen_US
dc.typereviewen_US
dc.relation.journalCOMPUTERS & CHEMICAL ENGINEERINGen_US
dc.contributor.departmentCumhuriyet Univ, Dept Chem Engn, TR-58140 Sivas, Turkey -- Ankara Univ, Dept Chem Engn, TR-06100 Ankara, Turkeyen_US
dc.identifier.volume30en_US
dc.identifier.issue9en_US
dc.identifier.endpage1323en_US
dc.identifier.startpage1315en_US
dc.relation.publicationcategoryDiğeren_US


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