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A Simple Method for Simulation of Stationary and Non-stationary Operation of Trayed Distillation Column

dc.creatorĐorđević, Dimitrije R.
dc.creatorJaćimović, Branislav M.
dc.creatorGenić, Srbislav
dc.creatorAranđelović, Ivan
dc.creatorKolendić, Petar
dc.creatorRajić, Radenko S.
dc.date.accessioned2022-09-19T16:35:04Z
dc.date.available2022-09-19T16:35:04Z
dc.date.issued2011
dc.identifier.issn0034-7752
dc.identifier.urihttps://machinery.mas.bg.ac.rs/handle/123456789/1169
dc.description.abstractA numerical method was developed for the analysis of the stationary and non-stationary operation of distillation columns, for mathematical model based on the concept of a theoretical tray and the ideal mixing of the phases on the tray. The approximation of the phase equilibrium equation by its Taylor polynomial is used for solving the system of equations representing the mathematical model of the column. The method was successfully applied in the analysis of the multi-component azeotropic mixtures distillation.en
dc.publisherChiminform Data S A, Bucharest
dc.rightsrestrictedAccess
dc.sourceRevista De Chimie
dc.subjectphase equilibriaen
dc.subjectmathematical modellingen
dc.subjectdistillationen
dc.subjectazeotropeen
dc.titleA Simple Method for Simulation of Stationary and Non-stationary Operation of Trayed Distillation Columnen
dc.typearticle
dc.rights.licenseARR
dc.citation.epage334
dc.citation.issue3
dc.citation.other62(3): 328-334
dc.citation.rankM23
dc.citation.spage328
dc.citation.volume62
dc.identifier.rcubhttps://hdl.handle.net/21.15107/rcub_machinery_1169
dc.identifier.scopus2-s2.0-79955636970
dc.identifier.wos000289814300014
dc.type.versionpublishedVersion


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