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dc.creatorMosorinac, T.
dc.creatorSavković-Stevanović, Jelenka B.
dc.creatorIvanović-Knezević, M.
dc.creatorPejanović, Srđan
dc.creatorPerunicić, M.
dc.creatorBošković-Vragolović, Nevenka
dc.date.accessioned2021-03-10T11:42:20Z
dc.date.available2021-03-10T11:42:20Z
dc.date.issued2012
dc.identifier.issn1337-7027
dc.identifier.urihttp://TechnoRep.tmf.bg.ac.rs/handle/123456789/2002
dc.description.abstractIn this paper substance transfer phenomena in the multistage reactive system were investigated.Substance transfer between liquid and gas phases in a distillation packed column with reactionesterification was examined. Efficiency of substance transfer were examined by HTU-Height of transferunits and volumetric substance transfer coefficients. The esterification reaction of the ethanol andacetic acid was examined. Based on derived mathematical model the total height of transfer units andindividual height of transfer units for the liquid and gas phases were determined. The investigation wasperformed by computer simulation and experiments. Several correlation models for HTU/NTU andsubstance transfer coefficients were studied. The correlations for component transfer were derived inquaternary systems ethanol-ethyl acetate-acetic acid -water.en
dc.rightsrestrictedAccess
dc.sourcePetroleum and Coal
dc.subjectCorrelationen
dc.subjectDistillationen
dc.subjectHeight of transfer unitsen
dc.subjectMultistage reactive systemen
dc.subjectSubstance transfer coefficienten
dc.titleModelling of the substance transfer in the gas-liquid system with chemical reactionen
dc.typearticle
dc.rights.licenseARR
dc.citation.epage286
dc.citation.issue3
dc.citation.other54(3): 278-286
dc.citation.spage278
dc.citation.volume54
dc.identifier.pmid
dc.identifier.rcubhttps://hdl.handle.net/21.15107/rcub_technorep_2002
dc.identifier.scopus2-s2.0-84877659297
dc.type.versionpublishedVersion


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Приказ основних података о документу