Vapor-Liquid Equilibrium of Ethylene+Mesitylene System and Process Simulation for Ethylene Recovery

郭敬; 武向红; 荆树宏; 张谦; 郑丹星

doi:10.1016/S1004-9541(11)60019-0

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Vapor-Liquid Equilibrium of Ethylene+Mesitylene System and Process Simulation for Ethylene Recovery

Updated：2026-01-06

- Vapor-Liquid Equilibrium of Ethylene+Mesitylene System and Process Simulation for Ethylene Recovery
- Vapor-Liquid Equilibrium of Ethylene+Mesitylene System and Process Simulation for Ethylene Recovery
- 中国化学工程学报（英文版） 2011年19卷第4期页码：543-548
- Affiliations：
  
  College of Chemical Engineering, Beijing University of Chemical Technology,Beijing,China,100029
- Author bio：
- Funds：
- DOI：10.1016/S1004-9541(11)60019-0
  中图分类号：
- 纸质出版：2011
- Accepted：
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郭敬, 武向红, 荆树宏, 等. Vapor-Liquid Equilibrium of Ethylene+Mesitylene System and Process Simulation for Ethylene Recovery[J]. 中国化学工程学报（英文版）, 2011,19(4):543-548.

GUO Jing, WU Xianghong, JING Shuhong, ZHANG Qian, ZHENG Danxing. Vapor-Liquid Equilibrium of Ethylene+Mesitylene System and Process Simulation for Ethylene Recovery [J]. , 2011, 19(4): 543-548.
郭敬, 武向红, 荆树宏, 等. Vapor-Liquid Equilibrium of Ethylene+Mesitylene System and Process Simulation for Ethylene Recovery[J]. 中国化学工程学报（英文版）, 2011,19(4):543-548. DOI： 10.1016/S1004-9541(11)60019-0.

GUO Jing, WU Xianghong, JING Shuhong, ZHANG Qian, ZHENG Danxing. Vapor-Liquid Equilibrium of Ethylene+Mesitylene System and Process Simulation for Ethylene Recovery [J]. , 2011, 19(4): 543-548. DOI： 10.1016/S1004-9541(11)60019-0.

摘要

Abstract

The amount of ethylene in refinery off-gas is high with a mass fraction of 20%

but the refinery off-gas is usually used as fuel gas in most refineries.The separation and recovery of ethylene is of remarkable significance for saving energy and reducing carbon dioxide emission.The aim of this paper is to use a novel absorbent mesitylene for the ethylene absorption process and assess its application feasibility through the ethylene+mesitylene vapor-liquid equilibrium data measurement and its binary interaction parameter correlation

as well as the simulation for ethylene separation process.

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