Vapor−Liquid Equilibria for the Binary System Hexane + 1,1-Dimethylpropyl Methyl Ether at 298.15, 308.15, 318.15, and 328.15 K-Reference-Cited by-同舟云学术

Vapor−Liquid Equilibria for the Binary System Hexane + 1,1-Dimethylpropyl Methyl Ether at 298.15, 308.15, 318.15, and 328.15 K

Published:2002-02-08 Issue:5 Volume:41 Page:1364-1369
ISSN:0888-5885
Container-title:Industrial & Engineering Chemistry Research
language:en
Short-container-title:Ind. Eng. Chem. Res.

Author:

del Río Armando¹,Coto Baudilio¹,Pando Concepción¹,Renuncio Juan A. R.¹

Affiliation:

1. Departamento de Química Física I, Universidad Complutense, E-28040 Madrid, Spain, and ESCET, Universidad Rey Juan Carlos, E-28933 Móstoles, Madrid, Spain

Publisher

American Chemical Society (ACS)

Subject

Industrial and Manufacturing Engineering,General Chemical Engineering,General Chemistry

Link

https://pubs.acs.org/doi/pdf/10.1021/ie0106128

Reference30 articles.

1. Vapor-Liquid Equilibrium of the Methanol-tert-Butyl Methyl Ether (MTBE) System

2. Vapor−Liquid Equilibrium for Methanol + 1,1-Dimethylpropyl Methyl Ether at (288.15, 308.15, and 328.15) K

3. Bulk and surface properties for the methanol–1,1-dimethylpropyl methyl ether and methanol–1,1-dimethylethyl methyl ether systems

4. Vapor-liquid equilibrium of the methanol[1,1-dimethylethyl methyl ether (MTBE) or 1,1-dimethylpropyl methy ether (TAME)] systems

5. Vapor-Liquid equilibria of binary mixtures of n-heptane with 1,1-dimethylpropyl methyl ether and 1,1-dimethylethyl methyl ether

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2. Vapor–Liquid Equilibria Measurements for Di-n-Propyl Ether and Butyl Ethyl Ether with n-Heptane;Journal of Chemical & Engineering Data;2016-11-10

3. Measurement and theoretical prediction of the vapor–liquid equilibrium, densities and interfacial tensions of the system hexane+2-methoxy-2-methylbutane;Fluid Phase Equilibria;2011-09

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5. Vapor–liquid equilibria for the binary system 2,2−dimethylbutane + 1,1−dimethylpropyl methyl ether (TAME) at 298.15, 318.15, and 338.15 K;Fluid Phase Equilibria;2004-07