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APPLICATION OF THE VAN-DER-WAALS-EQUATION OF STATE TO POLYMERS .2. PREDICTION

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dc.contributor.author HARISMIADIS, VI en
dc.contributor.author KONTOGEORGIS, GM en
dc.contributor.author FREDENSLUND, A en
dc.contributor.author TASSIOS, DP en
dc.date.accessioned 2014-03-01T01:42:45Z
dc.date.available 2014-03-01T01:42:45Z
dc.date.issued 1994 en
dc.identifier.issn 0378-3812 en
dc.identifier.uri https://dspace.lib.ntua.gr/xmlui/handle/123456789/23928
dc.subject THEORY en
dc.subject APPLICATION en
dc.subject EQUATIONS OF STATE en
dc.subject CUBIC en
dc.subject ACTIVITY COEFFICIENT en
dc.subject VAPOR-LIQUID EQUILIBRIA en
dc.subject MIXING RULES en
dc.subject ATHERMAL POLYMER SOLUTIONS en
dc.subject.classification Thermodynamics en
dc.subject.classification Chemistry, Physical en
dc.subject.classification Engineering, Chemical en
dc.subject.other VAPOR-LIQUID-EQUILIBRIA en
dc.subject.other SOLVENT ACTIVITIES en
dc.subject.other MOLTEN POLYMERS en
dc.subject.other MIXTURES en
dc.subject.other SOLUBILITIES en
dc.subject.other THERMODYNAMICS en
dc.subject.other EOS en
dc.title APPLICATION OF THE VAN-DER-WAALS-EQUATION OF STATE TO POLYMERS .2. PREDICTION en
heal.type journalArticle en
heal.language English en
heal.publicationDate 1994 en
heal.abstract For polymers, the energy and co-volume parameters of cubic equations of state can be reliably estimated using only two low-pressure volumetric data points. This procedure is applied to the van der Waals equation of state, and bubble-point pressure calculations are performed for a number of polymer solutions. The van der Waals one-fluid mixing rules are used. The Berthelot combining rule is used for estimating the cross energy parameter, while the usual arithmetic mean combining rule is used for evaluating the cross co-volume parameter. Deviations from Berthelot's combining rule are taken into account via a simple method requiring only the molecular weight of the solvent. It is shown that when the proposed method is applied, the van der Waals equation of state can predict the equilibrium pressures of polymer solutions. The accuracy of the predictions is very good, comparable to those of other more complex equations of state, but it is in general inferior to those of the free-volume activity coefficient models. The simplicity, accuracy and general applicability of the proposed method makes it an attractive alternative to previously proposed complex models for prediction of equilibrium pressures of nearly athermal and non-polar polymer solutions. en
heal.publisher ELSEVIER SCIENCE BV en
heal.journalName FLUID PHASE EQUILIBRIA en
dc.identifier.isi ISI:A1994NP76100006 en
dc.identifier.volume 96 en
dc.identifier.spage 93 en
dc.identifier.epage 117 en


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