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Modélisation des données d'équilibre liquide-vapeur contenant des perfluorocarbures à l'aide des équations d'état de Peng-Robinson et PC-SAFT.

Modeling binary vapor–liquid equilibrium data containing perfluorocarbons using the Peng–Robinson and the PC-SAFT equations of state.

Auteurs : PANAH H. S.

Type d'article : Article, Article de la RIF

Résumé

In this communication, thermodynamic modeling of twenty four binary systems containing perfluorocarbon compounds is studied using the Peng–Robinson and the PC-SAFT equations of state. Interaction parameters of binary systems were estimated through fitting to experimental equilibrium pressures and vapor phase compositions. Very good results were obtained through using temperature-independent interaction parameter for both equations of state. According to the results, percent deviations in pressure were varying between 0.5 and 7.7 for the PR EoS and 0.2 and 6.5 for the PC-SAFT EoS. Also, percent deviations in vapor phase composition were varying between 0.1 and 6.6 for the PR EoS and 0.1 and 7.4 for the PC-SAFT EoS. Furthermore, when binary system has critical point, phase equilibrium calculations using the PR EoS do not converge through common methods. For solving this problem, a solution is suggested that was absolutely effective on all the studied systems.

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Format PDF

Pages : 13-26

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    20 €

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Détails

  • Titre original : Modeling binary vapor–liquid equilibrium data containing perfluorocarbons using the Peng–Robinson and the PC-SAFT equations of state.
  • Identifiant de la fiche : 30022716
  • Langues : Anglais
  • Source : International Journal of Refrigeration - Revue Internationale du Froid - vol. 85
  • Date d'édition : 01/2018
  • DOI : http://dx.doi.org/10.1016/j.ijrefrig.2017.09.008

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