CIESC Journal

• Volume 2 • 上一篇    下一篇

NON-CUBIC EQUATION OF STATE FOR PHASE EQUILIBRIUM CALCULATIONS

童张法; 赵传钧; 卢焕章   

  1. Department of Chemical Engineering, Beijing Institute of Chemical Technology, Beijing 100029, China
  • 收稿日期:1992-09-19 修回日期:1993-02-16 出版日期:1994-03-28 发布日期:1994-03-28
  • 通讯作者: 童张法

NON-CUBIC EQUATION OF STATE FOR PHASE EQUILIBRIUM CALCULATIONS

TONG Zhangfa; ZHAO Chuanjun; LU Huanzhang   

  1. Department of Chemical Engineering, Beijing Institute of Chemical Technology, Beijing 100029, China
  • Received:1992-09-19 Revised:1993-02-16 Online:1994-03-28 Published:1994-03-28
  • Contact: TONG Zhangfa

摘要: A new non-cubic equation of state is proposed for calculation of the thermodynamic properties ofnonpolar and polar fluids and their mixtures,including,saturated vapor pressure,saturated liquid volume,saturated vapor volume,heats of vaporization and vapor-liquid equilibria.The new equation is derived from thegeneralized van der Waals partition function in which the repulsive terms are expressed with the Carnahan andStarling equation for hard spheres,and the attractive terms are made up of the dispersive energy and theChemical association energy. The rules of dependence of parameters αand σand on temperature are considered broadly so that the newequation yields good agreement with experimental saturated properties of 20 nonpolar and 27 polar fluids in therange of reduced temperatures of 0.5 to 1.0 The new equation with parameters group-contributed generally givessatisfactory predictions on saturated properties. Correlations of vapor-liquid equilibrium data for alcohol-containing systems by using van der Waalsone-fluid mixing rules prove that the new equation is superior to the M-PR equation of state.

关键词: equation of state;phase equilibrium;mixing rule

Abstract: A new non-cubic equation of state is proposed for calculation of the thermodynamic properties ofnonpolar and polar fluids and their mixtures,including,saturated vapor pressure,saturated liquid volume,saturated vapor volume,heats of vaporization and vapor-liquid equilibria.The new equation is derived from thegeneralized van der Waals partition function in which the repulsive terms are expressed with the Carnahan andStarling equation for hard spheres,and the attractive terms are made up of the dispersive energy and theChemical association energy. The rules of dependence of parameters αand σand on temperature are considered broadly so that the newequation yields good agreement with experimental saturated properties of 20 nonpolar and 27 polar fluids in therange of reduced temperatures of 0.5 to 1.0 The new equation with parameters group-contributed generally givessatisfactory predictions on saturated properties. Correlations of vapor-liquid equilibrium data for alcohol-containing systems by using van der Waalsone-fluid mixing rules prove that the new equation is superior to the M-PR equation of state.

Key words: equation of state, phase equilibrium, mixing rule