Vapor−Liquid Equilibrium of Binary and Ternary Mixtures Containing Isopropyl Ether, 2-Butanol, and Benzene at T = 313.15 K-Reference-Cited by-同舟云学术

Vapor−Liquid Equilibrium of Binary and Ternary Mixtures Containing Isopropyl Ether, 2-Butanol, and Benzene at T = 313.15 K

Published:2005-11-01 Issue:1 Volume:51 Page:148-152
ISSN:0021-9568
Container-title:Journal of Chemical & Engineering Data
language:en
Short-container-title:J. Chem. Eng. Data

Author:

Villamañán Rosa M.¹,Martín M. Carmen¹,Chamorro César R.¹,Segovia José J.¹

Affiliation:

1. Grupo de Termodinámica y Calibración (TERMOCAL), Departamento Ingeniería Energética y Fluidomecánica, E.T.S. de Ingenieros Industriales, Universidad de Valladolid, E-47071 Valladolid, Spain

Publisher

American Chemical Society (ACS)

Subject

General Chemical Engineering,General Chemistry

Link

https://pubs.acs.org/doi/pdf/10.1021/je0502896

Reference27 articles.

1. A Procedure for Rapid Degassing of Liquids

2. Vapor-Liquid Equilibria from Total-Pressure Measurements. A New Apparatus

3. Excess thermodynamic functions for ternary systems. 3. Total pressure data and GE for acetone-acetonitrile-methyl acetate at 50.degree.C

4. Vapor-liquid equilibria of binary mixtures containing methyl tert-butyl ether (MTBE) and/or substitution hydrocarbons at 298.15 K and 313.15 K

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