Author:
Francesconi R.,Trevissoi C.
Subject
Applied Mathematics,Industrial and Manufacturing Engineering,General Chemical Engineering,General Chemistry
Cited by
15 articles.
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1. An activity coefficient model for predicting salt effects on vapor–liquid equilibria of mixed solvent systems;Fluid Phase Equilibria;2000-04
2. Isothermal Vapor−Liquid Equilibria Measurements, Excess Molar Enthalpies, and Excess Molar Volumes of Dimethyl Carbonate + Methanol, + Ethanol, and + Propan-1-ol at 313.15 K;Journal of Chemical & Engineering Data;1997-07-01
3. Vapor−Liquid Equilibria, Excess Molar Enthalpies, and Excess Molar Volumes of Dialkyl Carbonates + Methyl tert-Butyl Ether at 298.15 K;Journal of Chemical & Engineering Data;1997-07-01
4. Prediction of vapor-liquid equilibria for acetic acid aqueous solutions containing salt;Fluid Phase Equilibria;1996-09
5. Vapor−Liquid Equilibria, Excess Molar Enthalpies, and Excess Molar Volumes of Dimethyl Carbonate + 1,2-Epoxybutane at 288.15, 298.15, or 313.15 K;Journal of Chemical & Engineering Data;1996-01-01