dc.contributor.author | Kontogeorgis, GM | en |
dc.contributor.author | Saraiva, A | en |
dc.contributor.author | Fredenslund, A | en |
dc.contributor.author | Tassios, DP | en |
dc.date.accessioned | 2014-03-01T01:11:25Z | |
dc.date.available | 2014-03-01T01:11:25Z | |
dc.date.issued | 1995 | en |
dc.identifier.issn | 0888-5885 | en |
dc.identifier.uri | https://dspace.lib.ntua.gr/xmlui/handle/123456789/11630 | |
dc.subject | Polymer Solution | en |
dc.subject.classification | Engineering, Chemical | en |
dc.subject.other | VAPOR-LIQUID | en |
dc.subject.other | SOLVENT ACTIVITIES | en |
dc.subject.other | PHASE-EQUILIBRIA | en |
dc.subject.other | EQUATION | en |
dc.subject.other | STATE | en |
dc.subject.other | MIXTURES | en |
dc.subject.other | SYSTEMS | en |
dc.subject.other | UNIFAC | en |
dc.title | Prediction of liquid-liquid equilibrium for binary polymer solutions with simple activity coefficient models | en |
heal.type | journalArticle | en |
heal.identifier.primary | 10.1021/ie00044a033 | en |
heal.identifier.secondary | http://dx.doi.org/10.1021/ie00044a033 | en |
heal.language | English | en |
heal.publicationDate | 1995 | en |
heal.abstract | Liquid-liquid equilibrium predictions for binary polymer solutions using four simple UNIFAC-based activity coefficient models are presented in this work. The four models are the original UNIFAC, the new UNIFAC recently developed in Lyngby, a modified Flory-Huggins model, and the recently developed entropic-FV model. All four models are purely predictive, since they are based on the group-contribution approach. They employ existing UNIFAC group interaction parameter tables, which have been estimated from vapor-liquid equilibrium data of mixtures with exclusively low molecular weight compounds. The investigated models are capable of predicting UCST qualitatively well, but only the modified Flory-Huggins and the entropic-FV models can predict LCST (near the critical temperature of the solvent) and are, thus, able to describe the combined UCST/LCST behavior often found in polymer solutions. In particular, the entropic-FV model can represent the five types of phase diagrams which are most often encountered in polymer solutions, including closed loops and hourglass type. Furthermore the predictions with the entropic-FV model are in several cases (especially for nonpolar solutions) semiquantitatively correct and generally far more accurate than those provided by the classical UNIFAC models. © 1995 American Chemical Society. | en |
heal.publisher | AMER CHEMICAL SOC | en |
heal.journalName | Industrial and Engineering Chemistry Research | en |
dc.identifier.doi | 10.1021/ie00044a033 | en |
dc.identifier.isi | ISI:A1995QX50500033 | en |
dc.identifier.volume | 34 | en |
dc.identifier.issue | 5 | en |
dc.identifier.spage | 1823 | en |
dc.identifier.epage | 1834 | en |
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