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
- Measurement and Correlation of Vapor-Liquid Equilibrium for Binary System 1,2-Epoxycyclohexane+1,2-Dichloroethane
- 中国化学工程学报（英文版） 2013年21卷第8期页码：901-9051004-954160538-8
- Affiliations：
  
  School of Chemical Engineering & Energy, Zhengzhou University,Zhengzhou,China,450001
- Author bio：
- Funds：
- DOI：10.1016/S1004-9541(13)60538-8
  中图分类号：
- 纸质出版：2013
- Accepted：
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周彩荣, 王海峰, 石晓华, 等. Measurement and Correlation of Vapor-Liquid Equilibrium for Binary System 1,2-Epoxycyclohexane+1,2-Dichloroethane[J]. 中国化学工程学报（英文版）, 2013,21(8):901-9051004-954160538-8.

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.
周彩荣, 王海峰, 石晓华, 等. Measurement and Correlation of Vapor-Liquid Equilibrium for Binary System 1,2-Epoxycyclohexane+1,2-Dichloroethane[J]. 中国化学工程学报（英文版）, 2013,21(8):901-9051004-954160538-8. DOI： 10.1016/S1004-9541(13)60538-8.

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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