dc.creatorSilva, JMF
dc.creatorKnoechelmann, A
dc.creatorMeirelles, AJA
dc.creatorWolf-Maciel, MR
dc.creatorLopes, CE
dc.date2003
dc.dateJUN
dc.date2014-11-14T03:22:56Z
dc.date2015-11-26T17:12:58Z
dc.date2014-11-14T03:22:56Z
dc.date2015-11-26T17:12:58Z
dc.date.accessioned2018-03-29T00:01:23Z
dc.date.available2018-03-29T00:01:23Z
dc.identifierChemical Engineering And Processing. Elsevier Science Sa, v. 42, n. 6, n. 475, n. 485, 2003.
dc.identifier0255-2701
dc.identifierWOS:000182180200005
dc.identifier10.1016/S0255-2701(02)00064-8
dc.identifierhttp://www.repositorio.unicamp.br/jspui/handle/REPOSIP/68647
dc.identifierhttp://www.repositorio.unicamp.br/handle/REPOSIP/68647
dc.identifierhttp://repositorio.unicamp.br/jspui/handle/REPOSIP/68647
dc.identifier.urihttp://repositorioslatinoamericanos.uchile.cl/handle/2250/1281463
dc.descriptionThe study of the dynamics of a simple batch distillation usually assumes the equilibrium between the liquid and vapour phases. In contrast to that approach, this work considers the analysis of the dynamic behaviour of a nonequilibrium simple batch distillation. A simple batch distillation device is similar to an evapouration unit because no reflux is employed. A mathematical model and their singular points are analysed through the usual technique of linearization followed by the eigenvalues analysis. The stability nature of those points is presented for ideal solutions. Phase plane plots are made to show the occurrence of some unexpected behaviours such as 'dynamic azeotropic points' and 'inversion of the distillation order'. The dependence of these phenomena on the vapour withdrawal flowrate is established for simple batch distillation. (C) 2002 Elsevier Science B.V. All rights reserved.
dc.description42
dc.description6
dc.description475
dc.description485
dc.languageen
dc.publisherElsevier Science Sa
dc.publisherLausanne
dc.publisherSuíça
dc.relationChemical Engineering And Processing
dc.relationChem. Eng. Process.
dc.rightsfechado
dc.rightshttp://www.elsevier.com/about/open-access/open-access-policies/article-posting-policy
dc.sourceWeb of Science
dc.subjectseparations process
dc.subjectdynamic azeotrope
dc.subjectnonequilibrium distillation
dc.subjectdynamic simulation
dc.subjectstability
dc.subjectmass transfer
dc.subjectMulticomponent Separation Processes
dc.subjectHomogeneous Liquid-mixtures
dc.subjectMiddle Vessel
dc.subjectStage Model
dc.subjectSimulation
dc.subjectColumn
dc.titleOn the dynamics of nonequilibrium simple batch distillation processes
dc.typeArtículos de revistas


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