Measurement and Correlation of Vapor-Liquid Equilibrium for Binary System 1,2-Epoxycyclohexane+1,2-Dichloroethane

周彩荣; 王海峰; 石晓华; 蒋登高

doi:10.1016/S1004-9541(13)60538-8

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Measurement and Correlation of Vapor-Liquid Equilibrium for Binary System 1,2-Epoxycyclohexane+1,2-Dichloroethane

化工热力学 | Updated：2026-01-06

- Measurement and Correlation of Vapor-Liquid Equilibrium for Binary System 1,2-Epoxycyclohexane+1,2-Dichloroethane
- Chinese Journal of Chemical Engineering Vol. 21, Issue 8, Pages: 901-9051004-954160538-8(2013)
- Affiliations：
  
  School of Chemical Engineering & Energy, Zhengzhou University,Zhengzhou,China,450001
- Author bio：
- Funds：
- DOI：10.1016/S1004-9541(13)60538-8
  CLC：
- Published：2013
- Accepted：
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ZHOU Cairong, WANG Haifeng, SHI Xiaohua, JIANG Denggao. Measurement and Correlation of Vapor-Liquid Equilibrium for Binary System 1,2-Epoxycyclohexane+1,2-Dichloroethane[J]. Chin.J.Chem.Eng., 2013, 21(8): 901-905.
DOI：

ZHOU Cairong, WANG Haifeng, SHI Xiaohua, JIANG Denggao. Measurement and Correlation of Vapor-Liquid Equilibrium for Binary System 1,2-Epoxycyclohexane+1,2-Dichloroethane[J]. Chin.J.Chem.Eng., 2013, 21(8): 901-905. DOI： 10.1016/S1004-9541(13)60538-8.

摘要

Abstract

Vapor-liquid equilibrium data (T

y) of binary system 1

2-epoxycyclohexane + 1

2-dichloroethane were determined experimentally by using a modified ROSE-Williams equilibrium vaporization system at 101.33 kPa. The results show that this binary system does not have azeotropic point. The vapor-liquid equilibrium data are in thermodynamic consistency. The binary interaction parameters in the Wilson equation are presented with the correlation of vapor-liquid equilibrium data. The measurements of liquid phase composition and bubble point temperature are well represented by the Wilson equation. Values of vapor molecular fractions and activity coefficients from the Wilson equation are presented. This work provides important engineering data for the separation of 1

2-dichloroethane and 1

2-epoxycyclohexane.

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