Приказ основних података о документу

dc.creatorBrzić, Danica
dc.creatorSchubert, M.
dc.creatorHaering, H.
dc.creatorLange, R.
dc.creatorPetkovska, Menka
dc.date.accessioned2021-03-10T11:17:19Z
dc.date.available2021-03-10T11:17:19Z
dc.date.issued2010
dc.identifier.issn0009-2509
dc.identifier.urihttp://TechnoRep.tmf.bg.ac.rs/handle/123456789/1613
dc.description.abstractIn this paper, we propose a new procedure for fast evaluation of the potential of periodic operations in trickle-bed reactors, based on empirical modeling. Step response experiments, with different input amplitudes, were performed on a laboratory trickle-bed reactor, in order to derive a simple nonlinear dynamic model. a-methylstyrene (AMS) hydrogenation was used as a test reaction and the feed AMS concentration was used as the modulated input. An empirical nonlinear model was postulated and used for simulation of periodic operations. The simulation of a periodic operation with sinusoidal modulation of the inlet AMS concentration with 40 % amplitude resulted up to 35% higher time-averaged conversion than the corresponding steady-state one.en
dc.publisherPergamon-Elsevier Science Ltd, Oxford
dc.relationDAADDeutscher Akademischer Austausch Dienst (DAAD) [FK-06-324]
dc.relationinfo:eu-repo/grantAgreement/MESTD/MPN2006-2010/142014/RS//
dc.rightsrestrictedAccess
dc.sourceChemical Engineering Science
dc.subjectPeriodic operationen
dc.subjectStep responseen
dc.subjectMathematical modelingen
dc.subjectNonlinear dynamicsen
dc.subjectMultiphase reactorsen
dc.subjectParameter identificationen
dc.titleEvaluation of periodic operation of a trickle-bed reactor based on empirical modelingen
dc.typearticle
dc.rights.licenseARR
dc.citation.epage4165
dc.citation.issue14
dc.citation.other65(14): 4160-4165
dc.citation.rankM21
dc.citation.spage4160
dc.citation.volume65
dc.identifier.doi10.1016/j.ces.2010.04.032
dc.identifier.scopus2-s2.0-77953230884
dc.identifier.wos000278603500006
dc.type.versionpublishedVersion


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Приказ основних података о документу