Prediction of Vapor–Liquid Equilibria of Alcohol+Hydrocarbon Binary Systems by Using Wilson Equation with Parameters Estimated from Pure–Component Properties

Author:

Kobuchi Shigetoshi11,Ishige Kenji11,Takakura Kei11,Yonezawa Setsuko22,Fukuchi Kenji33,Arai Yasuhiko22

Affiliation:

1. Department of Environmental Science and Engineering, Graduate School of Science and Engineering, Yamaguchi University

2. Department of Chemical Engineering, Faculty of Engineering, Kyushu University

3. Department of Chemical and Biological Engineering, Ube National College of Technology

Publisher

Society of Chemical Engineers, Japan

Subject

General Chemical Engineering,General Chemistry

Reference17 articles.

1. Boublik, T., V. Fried and E. Hála; The Vapour Pressures of Pure Substances, 2nd ed., Elsevier, Amsterdam, the Netherlands (1984)

2. Isobaric Vapor−Liquid Equilibrium for the Binary Mixtures (2-Butanol + n-Hexane) and (2-Butanol + 1-Butylamine) and for the Ternary System (2-Butanol + n-Hexane + 1-Butylamine) at 101.3 kPa

3. Vapor−Liquid Equilibria of Binary Mixtures 2-Butanol + Butyl Acetate, Hexane + Butyl Acetate, and Cyclohexane + 2-Butanol at 101.3 kPa

4. Gmehling, J. and U. Onken; Vapor–Liquid Equilibrium Data Collection, Organic Hydroxy Compounds: Alcohols, DECHEMA Chemistry Data Series, Vol. 1, Part 2a, DECHEMA, Frankfurt/Main, Germany (1977)

5. Gmehling, J. and U. Onken; Vapor–Liquid Equilibrium Data Collection, Alcohols (Supplement 7), DECHEMA Chemistry Data Series, Vol. 1, Part 2i, DECHEMA, Frankfurt/Main, Germany (2007)

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