Isobaric Vapor–Liquid Equilibrium Data for the Binary Mixtures 2-Methyl Propan-2-ol with Tetraethoxysilane and 1-Phenyl Ethanone at 95.5 kPa
Author:
Affiliation:
1. Chemical Engineering Division, Indian Institute of Chemical Technology, Hyderabad 500007, India
Publisher
American Chemical Society (ACS)
Subject
General Chemical Engineering,General Chemistry
Link
https://pubs.acs.org/doi/pdf/10.1021/je300076y
Reference11 articles.
1. Polymers from the hydrolysis of tetraethoxysilane
2. Vapor-Liquid Equilibrium. XI. A New Expression for the Excess Free Energy of Mixing
3. Improved equation for prediction of saturated liquid density
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1. Measurements, Correlations, and Modified UNIFAC Predictions of Isobaric Vapor–Liquid Equilibrium Data for the Binary System of Dimethyl Carbonate + Anisole at Different Pressures;Journal of Chemical & Engineering Data;2021-10-01
2. Separation of azeotropic mixture (2, 2, 3, 3-Tetrafluoro-1-propanol + water) by extractive distillation: Entrainers selection and vapour-liquid equilibrium measurements;The Journal of Chemical Thermodynamics;2019-11
3. Isobaric vapour–liquid equilibrium measurements and extractive distillation process for the azeotrope of ( N , N -dimethylisopropylamine + acetone);The Journal of Chemical Thermodynamics;2018-07
4. Isobaric Vapor–Liquid Phase Equilibrium Measurements, Correlation, and Prediction for Separation of the Mixtures of Cyclohexanone and Alcohols;Journal of Chemical & Engineering Data;2018-05-22
5. Refractive index of tetraethoxysilane;Optical Constants;2017
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