High pressure vapor–liquid equilibria of methyl acetate or ethyl acetate with 2-propanol at 1.5MPa. Experimental data and predictions-Reference-Cited by-同舟云学术

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High pressure vapor–liquid equilibria of methyl acetate or ethyl acetate with 2-propanol at 1.5MPa. Experimental data and predictions

Published:2015-10 Issue: Volume:102 Page:337-344
ISSN:0263-8762
Container-title:Chemical Engineering Research and Design
language:en
Short-container-title:Chemical Engineering Research and Design

Author:

Susial Rodrigo,Susial Pedro

Publisher

Elsevier BV

Subject

General Chemical Engineering,General Chemistry

Reference27 articles.

1. Vapor–Liquid Equilibria Using UNIFAC. A Group Contribution Model;Fredenslund,1977

2. A modified UNIFAC model. 2. Present parameter matrix and results for different thermodynamic properties;Gmehling;Ind. Eng. Chem. Res.,1993

3. Azeotropic Data. Part 1;Gmehling,2004

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3. Fundamentals of Phase Equilibria;Thermodynamics of Phase Equilibria in Food Engineering;2019

4. Measurement and Modelization of VLE for Butyl Acetate with Methanol, Ethanol, 1-Propanol, and 1-Butanol. Experimental Data at 0.15 MPa;Journal of Chemical & Engineering Data;2018-06-04

5. Separation of ethyl acetate and 2-propanol azeotropic mixture using ionic liquids as entrainers;Fluid Phase Equilibria;2016-12

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