Salting-out effect of ionic liquids on isobaric vapor-liquid equilibrium of acetonitrile-water system

Jing Fang; Rui Zhao; HuiWang; Chunli Li; Jing Liu

doi:10.1016/j.cjche.2015.04.011

Your Location：

Home >

Browse articles >

Salting-out effect of ionic liquids on isobaric vapor-liquid equilibrium of acetonitrile-water system

化工热力学 | Updated：2026-01-06

- Salting-out effect of ionic liquids on isobaric vapor-liquid equilibrium of acetonitrile-water system
- Chinese Journal of Chemical Engineering Vol. 23, Issue 8, Pages: 1369-1373(2015)
- Affiliations：
  
  2 Environmental Monitoring Central Station of Suqian City,Jiangsu Province,Suqian,China,223800
- Author bio：
- Funds：
- DOI：10.1016/j.cjche.2015.04.011
  CLC：
- Published：2015
- Accepted：
Scan QR Code
Jing Fang, Rui Zhao, HuiWang, Chunli Li, Jing Liu. Salting-out effect of ionic liquids on isobaric vapor-liquid equilibrium of acetonitrile-water system[J]. Chin.J.Chem.Eng., 2015, 23(8): 1369-1373.
DOI：

Jing Fang, Rui Zhao, HuiWang, Chunli Li, Jing Liu. Salting-out effect of ionic liquids on isobaric vapor-liquid equilibrium of acetonitrile-water system[J]. Chin.J.Chem.Eng., 2015, 23(8): 1369-1373. DOI： 10.1016/j.cjche.2015.04.011.

摘要

Abstract

This paper presents the vapor-liquid equilibrium (VLE) data of acetonitrile-water system containing ionic liquids (ILs) at atmospheric pressure (101.3 kPa). Since ionic liquids dissociate into anions and cations

the VLE data for the acetonitrile + water + ILs systems are correlated by salt effect models

Furter model and improved Furter model. The overall average relative deviation of Furter model and improved Furter model is 5.43% and 4.68%

respectively. Thus the salt effect models are applicable for the correlation of IL containing systems. The salting-out effect theory can be used to explain the change of relative volatility of acetonitrile-water system.

关键词

Keywords

references

Views

156

Downloads

CSCD

Alert me when the article has been cited

Submit

Tools

Publicity Resources

Efficient and reversible separation of NH3 by deep eutectic solvents with multiple active sites and low viscosities

Numerical simulation of two-phase flow and droplet breakage of glycerin-water mixture and kerosene in the cyclone reactor

Effects of imidazolium-based ionic liquids on the isobaric vapor-liquid equilibria of methanol + dimethyl carbonate azeotropic systems

Vapor pressure measurement and correlation of acetonitrile +1-butyl-3-methylimidazolium chloride, +1-butyl-3-methylimidazolium tetrafluoroborate, and +1-hexyl-3-methylimidazolium chloride

Vapor-Liquid Equilibrium Prediction of Ammonia-Ionic Liquid Working Pairs of Absorption Cycle Using UNIFAC Model

Related Author

Jiayin Zhang

Lu Zheng

Siqi Fang

Hongwei Zhang

Zhenping Cai

Kuan Huang

Lilong Jiang

Yanni Chi

Related Institution

National Engineering Research Center of Chemical Fertilizer Catalyst (NERC-CFC), College of Chemical Engineering, Fuzhou University

Qingyuan Innovation Laboratory

State Key Laboratory of Heavy Oil Processing, China University of Petroleum-, Beijing

Beijing Key Laboratory of Ionic Liquids Clean Process, CAS Key Laboratory of Green Process and Engineering, State Key Laboratory of Multiphase Complex Systems, Institute of Process Engineering, Chinese Academy of Sciences

School of Chemical Engineering, University of Chinese Academy of Sciences

⁰