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Miscibility of Polymer Blends with Engineering Models

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dc.contributor.author Harismiadis, VI en
dc.contributor.author Van Bergen, ARD en
dc.contributor.author Saraiva, A en
dc.contributor.author Kontogeorgis, GM en
dc.contributor.author Fredenslund, A en
dc.contributor.author Tassios, DP en
dc.date.accessioned 2014-03-01T01:12:05Z
dc.date.available 2014-03-01T01:12:05Z
dc.date.issued 1996 en
dc.identifier.issn 0001-1541 en
dc.identifier.uri https://dspace.lib.ntua.gr/xmlui/handle/123456789/11943
dc.relation.uri http://www.scopus.com/inward/record.url?eid=2-s2.0-0030294751&partnerID=40&md5=47cc40ad53dc81167b306c20109709f4 en
dc.subject.classification Engineering, Chemical en
dc.subject.other Composition effects en
dc.subject.other Entropy en
dc.subject.other Equations of state of liquids en
dc.subject.other Mathematical models en
dc.subject.other Phase equilibria en
dc.subject.other Phase interfaces en
dc.subject.other Solubility en
dc.subject.other Van der Waals forces en
dc.subject.other Composition independent binary interaction parameter en
dc.subject.other Group contribution models en
dc.subject.other Polymer blends en
dc.subject.other miscibility en
dc.subject.other phase equilibrium model en
dc.subject.other polymers en
dc.title Miscibility of Polymer Blends with Engineering Models en
heal.type journalArticle en
heal.language English en
heal.publicationDate 1996 en
heal.abstract The miscibility behavior of polymer blends that do not exhibit strong specific interactions is examined. Phase equilibrium calculations are presented with the van der Waals equation of state and three group-contribution models (UNIFAC, Entropic-FV, and GC-Flory). Performance of these models is also compared. The van der Waals equation of state was recently shown to accurately correlate and predict vapor-liquid and liquid-liquid equilibria for binary polymer/solvent solutions. In this work, it is demonstrated that it correlates the upper critical solution behavior of polymer blends with excellent accuracy using the usual mixing and combining rules and a single temperature- and composition-independent binary interaction parameter. This interaction parameter can be predicted via a generalized expression that uses only the pure component equation-of-state parameters. Using this generalized expression, the upper critical solution temperature can be predicted with an average error of less than 45 degrees C. The van der Waals equation of state can correlate the lower critical solution behavior of polymer blends, using an interaction parameter that is a linear function of temperature. The UNIFAC and Entropic-FV models, in general, are able to predict qualitatively the phase behavior of polymer blends, but quantitative predictions of the critical solution temperatures es are not achieved The GC-Flory equation of state fails to predict the upper critical solution behavior in polymer blends. en
heal.publisher AMER INST CHEMICAL ENGINEERS en
heal.journalName AIChE Journal en
dc.identifier.isi ISI:A1996VR59500016 en
dc.identifier.volume 42 en
dc.identifier.issue 11 en
dc.identifier.spage 3170 en
dc.identifier.epage 3180 en


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