Experimental and Predicted Isobaric Vapour-Liquid Equilibrium for the Binary Systems 1,2-Dibromoethane with Isomeric Butanols.
Author:
Affiliation:
1. Departamento de Química Orgánica-Física, Facultad de Ciencias, Universidad de Zaragoza
2. Departamento de Física Aplicada, Facultad de Ciencias, Universidad de Zaragoza
Publisher
Society of Chemical Engineers, Japan
Subject
General Chemical Engineering,General Chemistry
Link
http://www.jstage.jst.go.jp/article/jcej/28/6/28_6_721/_pdf
Reference18 articles.
1. Statistical thermodynamics of liquid mixtures: A new expression for the excess Gibbs energy of partly or completely miscible systems
2. Amdur, I. and E. A. Mason; “Properties of Gases at Very High Temperatures,” Phys. Fluids, 1, 370–383 (1958)
3. Fredenslund, A., J. Gmehling and P. Rasmussen; Vapor-Liquid Equilibria Using UNIFAC, p. 68–74, Elsevier, Amsterdam, The Netherlands (1977)
4. Group-contribution estimation of activity coefficients in nonideal liquid mixtures
5. A modified UNIFAC model. 2. Present parameter matrix and results for different thermodynamic properties
Cited by 3 articles. 订阅此论文施引文献 订阅此论文施引文献，注册后可以免费订阅5篇论文的施引文献，订阅后可以查看论文全部施引文献
1. Calorimetric Behaviour of Primary Bromobutanes with Isomeric Butanols;Zeitschrift für Physikalische Chemie;2001-01-01
2. Isobaric VLE Data of the Ternary System (1-Butanol+n-Hexane+1-Butylamine) and the Three Constituent Binary Mixtures at 101.3kPa.;JOURNAL OF CHEMICAL ENGINEERING OF JAPAN;1997
3. Vapor−Liquid Equilibria for the Binary Systems of 1-Butanol with Some Halohydrocarbons at 40.0 and 101.3 kPa;Journal of Chemical & Engineering Data;1997-01-01
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