Molecular Modeling of Fluid-Phase Equilibria Using an Isotropic Multipolar Potential

Erich A. Müller*
Departamento de Termodinámica y Fenómenos de Transferencia, Universidad Simón Bolívar, Caracas 1080, Venezuela
Lev D. Gelb
Department of Chemistry, Washington University, St. Louis, Missouri 63130-1134
Ind. Eng. Chem. Res., 2003, 42 (17), pp 4123–4131
DOI: 10.1021/ie030033y
Publication Date (Web): July 19, 2003
Copyright © 2003 American Chemical Society

Abstract

We apply a simplified intermolecular potential function to model the fluid-phase behavior of realistic multicomponent polar systems. The isotropic multipolar potential includes dispersion, repulsion, and spherically averaged multipolar contributions and has a simple isotropic mathematical form with only two adjustable parameters. These energy and size parameters may be fitted to experimental pure-component properties such as liquid densities or critical points. These potentials, coupled with large-scale temperature-quench molecular dynamics simulations, yield thermophysical data such as the temperature−density diagram of benzene and naphthalene, the high-pressure PvT properties of carbon dioxide, the vapor−liquid equilibria of 1,2-dichloroethane/cyclohexane, and the liquid−liquid equilibria of the sulfolane/n-octane/benzene system. Despite the explicit omission of both molecular shape and directionality of multipolar interactions from the potential, the results are in quantitative agreement with experimental results, suggesting that it is the average energetic interactions that dictate the gross details of fluid phase equilibria.

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This article has been cited by 6 ACS Journal articles (5 most recent appear below).

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History

  • Published In Issue August 20, 2003
  • Resubmitted for review January 15, 2003
    Revised manuscript received May 29, 2003
    Accepted June 11, 2003

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