Application of the van der Waals equation of state to polymers III. Correlation and prediction of upper critical solution temperatures for polymer solutions

Vassilis I. Harismiadis, Georgios M. Kontogeorgis, Ana Saraiva, Aage Fredenslund, Dimitrios P. Tassios

Research output: Contribution to journalJournal articleResearchpeer-review

Abstract

The van der Waals equation of state is used for correlation (using a single binary interaction parameter) and prediction of liquid-liquid equilibrium in many mixtures including a solvent and a polymer. The equation of state parameters for the polymer are estimated from experimental volumetric data at low pressures. For the solvent, the equation of state parameters are estimated via the classical method, i.e. using the critical properties of the solvent and generalized expressions of the acentric factor. When extended to mixtures, the van der Waals one-fluid mixing rules along with the Berthelot combining rule for the molecular cross energy parameter are used. The arithmetic mean combining rule is used for the cross co-volume parameter. A correction to the Berthelot combining rule which is obtained from vapor-liquid equilibrium data of polymer solutions is used for predicting the upper critical solution temperatures for many different binary polymer solutions, including polar and non-polar systems. The results are remarkably successful. Typically, the difference between the predicted and the experimental upper critical solution temperatures is less than twenty degrees. Further, in all cases, correlation is achieved in an easy and straightforward way without difficulty and excellent results are obtained. Unlike other theories and models, the van der Waals equation of state is capable of predicting the flatness of the coexistence curves, which often occurs in polymer solutions.
Original languageEnglish
JournalFluid Phase Equilibria
Volume100
Pages (from-to)63-102
ISSN0378-3812
DOIs
Publication statusPublished - 1994

Keywords

  • Theory
  • Application
  • Liquid-liquid equilibria
  • Equation of state
  • Mixing rules
  • Polymer solutions

Cite this

@article{f60af00507974166b7b6c1965a9ed5a5,
title = "Application of the van der Waals equation of state to polymers III. Correlation and prediction of upper critical solution temperatures for polymer solutions",
abstract = "The van der Waals equation of state is used for correlation (using a single binary interaction parameter) and prediction of liquid-liquid equilibrium in many mixtures including a solvent and a polymer. The equation of state parameters for the polymer are estimated from experimental volumetric data at low pressures. For the solvent, the equation of state parameters are estimated via the classical method, i.e. using the critical properties of the solvent and generalized expressions of the acentric factor. When extended to mixtures, the van der Waals one-fluid mixing rules along with the Berthelot combining rule for the molecular cross energy parameter are used. The arithmetic mean combining rule is used for the cross co-volume parameter. A correction to the Berthelot combining rule which is obtained from vapor-liquid equilibrium data of polymer solutions is used for predicting the upper critical solution temperatures for many different binary polymer solutions, including polar and non-polar systems. The results are remarkably successful. Typically, the difference between the predicted and the experimental upper critical solution temperatures is less than twenty degrees. Further, in all cases, correlation is achieved in an easy and straightforward way without difficulty and excellent results are obtained. Unlike other theories and models, the van der Waals equation of state is capable of predicting the flatness of the coexistence curves, which often occurs in polymer solutions.",
keywords = "Theory, Application, Liquid-liquid equilibria, Equation of state, Mixing rules, Polymer solutions",
author = "Harismiadis, {Vassilis I.} and Kontogeorgis, {Georgios M.} and Ana Saraiva and Aage Fredenslund and Tassios, {Dimitrios P.}",
year = "1994",
doi = "10.1016/0378-3812(94)80003-0",
language = "English",
volume = "100",
pages = "63--102",
journal = "Fluid Phase Equilibria",
issn = "0378-3812",
publisher = "Elsevier",

}

Application of the van der Waals equation of state to polymers III. Correlation and prediction of upper critical solution temperatures for polymer solutions. / Harismiadis, Vassilis I.; Kontogeorgis, Georgios M.; Saraiva, Ana; Fredenslund, Aage; Tassios, Dimitrios P.

In: Fluid Phase Equilibria, Vol. 100, 1994, p. 63-102.

Research output: Contribution to journalJournal articleResearchpeer-review

TY - JOUR

T1 - Application of the van der Waals equation of state to polymers III. Correlation and prediction of upper critical solution temperatures for polymer solutions

AU - Harismiadis, Vassilis I.

AU - Kontogeorgis, Georgios M.

AU - Saraiva, Ana

AU - Fredenslund, Aage

AU - Tassios, Dimitrios P.

PY - 1994

Y1 - 1994

N2 - The van der Waals equation of state is used for correlation (using a single binary interaction parameter) and prediction of liquid-liquid equilibrium in many mixtures including a solvent and a polymer. The equation of state parameters for the polymer are estimated from experimental volumetric data at low pressures. For the solvent, the equation of state parameters are estimated via the classical method, i.e. using the critical properties of the solvent and generalized expressions of the acentric factor. When extended to mixtures, the van der Waals one-fluid mixing rules along with the Berthelot combining rule for the molecular cross energy parameter are used. The arithmetic mean combining rule is used for the cross co-volume parameter. A correction to the Berthelot combining rule which is obtained from vapor-liquid equilibrium data of polymer solutions is used for predicting the upper critical solution temperatures for many different binary polymer solutions, including polar and non-polar systems. The results are remarkably successful. Typically, the difference between the predicted and the experimental upper critical solution temperatures is less than twenty degrees. Further, in all cases, correlation is achieved in an easy and straightforward way without difficulty and excellent results are obtained. Unlike other theories and models, the van der Waals equation of state is capable of predicting the flatness of the coexistence curves, which often occurs in polymer solutions.

AB - The van der Waals equation of state is used for correlation (using a single binary interaction parameter) and prediction of liquid-liquid equilibrium in many mixtures including a solvent and a polymer. The equation of state parameters for the polymer are estimated from experimental volumetric data at low pressures. For the solvent, the equation of state parameters are estimated via the classical method, i.e. using the critical properties of the solvent and generalized expressions of the acentric factor. When extended to mixtures, the van der Waals one-fluid mixing rules along with the Berthelot combining rule for the molecular cross energy parameter are used. The arithmetic mean combining rule is used for the cross co-volume parameter. A correction to the Berthelot combining rule which is obtained from vapor-liquid equilibrium data of polymer solutions is used for predicting the upper critical solution temperatures for many different binary polymer solutions, including polar and non-polar systems. The results are remarkably successful. Typically, the difference between the predicted and the experimental upper critical solution temperatures is less than twenty degrees. Further, in all cases, correlation is achieved in an easy and straightforward way without difficulty and excellent results are obtained. Unlike other theories and models, the van der Waals equation of state is capable of predicting the flatness of the coexistence curves, which often occurs in polymer solutions.

KW - Theory

KW - Application

KW - Liquid-liquid equilibria

KW - Equation of state

KW - Mixing rules

KW - Polymer solutions

U2 - 10.1016/0378-3812(94)80003-0

DO - 10.1016/0378-3812(94)80003-0

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JO - Fluid Phase Equilibria

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