Isobaric Vapor−Liquid Equilibria for Ternary Mixtures: Saturated Hydrocarbons, Xylenes, and Ethylbenzene with Sulfolane at 101.325 kPa
Author:
Affiliation:
1. Indian Institute of Petroleum, Dehradun-248 005, India
Publisher
American Chemical Society (ACS)
Subject
General Chemical Engineering,General Chemistry
Link
https://pubs.acs.org/doi/pdf/10.1021/je970252o
Reference21 articles.
1. Some thermodynamic properties of the sulfolane–benzene and sulfolane–dichloromethane systems
2. Group-contribution estimation of activity coefficients in nonideal liquid mixtures
3. Vapor-liquid equilibriums by UNIFAC group contribution. Revision and extension. 2
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1. Separation of benzene and cyclohexane by extractive distillation intensified with ionic liquid;Chemical Engineering and Processing - Process Intensification;2018-04
2. Liquid–Liquid Equilibria of Ternary Systemscis-1,2-Dimethylcyclohexane+Toluene+Sulfolane;Chinese Journal of Chemical Engineering;2014-11
3. Isobaric (vapour+liquid) equilibria for sulfolane with toluene, ethylbenzene, and isopropylbenzene at 101.33kPa;The Journal of Chemical Thermodynamics;2011-12
4. Extractive rectification by means of sulfolane in chemical technology: A review;Coke and Chemistry;2011-08
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