Vapor–liquid equilibrium data and their correlation for binary systems consisting of ethanol, 2-propanol, 1,2-ethanediol and methyl benzoate
Author:
Publisher
Elsevier BV
Subject
Physical and Theoretical Chemistry,General Physics and Astronomy,General Chemical Engineering
Reference19 articles.
1. The separation of lower boiling alcohols by extractive distillation;Berg;Chem. Eng. Comm.,1988
2. Vapor–liquid equilibrium data collection;Gmehling,1977
3. Total vapor pressure measurements and excess Gibbs energies for the binary systems methanol+ethanol, ethanol+2-propanol, benzene+cyclohexane, benzene+carbon tetrachloride and benzene+ethanol at 303.15 and 313.15 K;Zielkiewicz;Fluid Phase Equilib.,1990
4. Activity coefficients at infinite dilution for ternary system;Kojima;AIChE J.,1972
5. Vapor–liquid equilibrium data for ethanol-n-heptane-1-propanol and ethanol-n-heptane-2-propanol and their interpretation by a simple association model;Pradhan;Fluid Phase Equilib.,1993
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