Isobaric Vapor−Liquid Equilibria and Excess Quantities for Binary Mixtures of an Ethyl Ester + tert-Butanol and a New Approach to VLE Data Processing-Reference-Cited by-同舟云学术

Isobaric Vapor−Liquid Equilibria and Excess Quantities for Binary Mixtures of an Ethyl Ester + tert-Butanol and a New Approach to VLE Data Processing

Published:2003-06-21 Issue:4 Volume:48 Page:916-924
ISSN:0021-9568
Container-title:Journal of Chemical & Engineering Data
language:en
Short-container-title:J. Chem. Eng. Data

Author:

Ortega Juan¹,Espiau Fernando¹,Postigo Miguel¹

Affiliation:

1. Laboratorio de Termodinámica y Fisicoquímica, Escuela Superior de Ingenieros Industriales, Universidad de Las Palmas de Gran Canaria, 35071-Las Palmas de Gran Canaria, Islas Canarias, Spain

Publisher

American Chemical Society (ACS)

Subject

General Chemical Engineering,General Chemistry

Link

https://pubs.acs.org/doi/pdf/10.1021/je0202073

Reference21 articles.

1. Azeotropic Data for Binary and Ternary Systems at Moderate Pressures

2. Experimental VLE at 101.32 kPa in binary systems composed of ethyl methanoate and alkan-1-ols or alkan-2-ols and treatment of data using a correlation with temperature-dependent parameters

3. A modified UNIFAC model. 2. Present parameter matrix and results for different thermodynamic properties

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