Phase Equilibrium Study of Binary and Ternary Mixtures of Ionic Liquids + Acetone + Methanol
Author:
Affiliation:
1. Liaoning Provincial Key Laboratory of Chemical Separation Technology, Shenyang University of Chemical Technology, Shenyang 110142, China
Funder
National Natural Science Foundation of China
Program for Liaoning Excellent Talents in University
Publisher
American Chemical Society (ACS)
Subject
General Chemical Engineering,General Chemistry
Link
https://pubs.acs.org/doi/pdf/10.1021/je500418f
Reference26 articles.
1. Vapor-Liquid Equilibria for Acetone + Chloroform + Methanol and Constituent Binary Systems at 101.3 kPa
2. Vapor−Liquid Equilibrium in Extractive Distillation of the Acetone/Methanol System Using Water as Entrainer and Pressure Reduction
3. Monoethanolamine as an Extractive Solvent for the n-Hexane + Benzene, Cyclohexane + Ethanol, and Acetone + Methanol Binary Systems
4. Vapor-Liquid Equilibria for the Ternary System Acetone + Methanol + Chlorobenzene at 101.325 kPa
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