Vapor−Liquid Equilibria and Enthalpies of Mixing in a Temperature Range from 298.15 to 413.15 K for the Further Development of Modified UNIFAC (Dortmund)-Reference-Cited by-同舟云学术

Vapor−Liquid Equilibria and Enthalpies of Mixing in a Temperature Range from 298.15 to 413.15 K for the Further Development of Modified UNIFAC (Dortmund)

Published:2001-11-01 Issue:24 Volume:40 Page:5831-5838
ISSN:0888-5885
Container-title:Industrial & Engineering Chemistry Research
language:en
Short-container-title:Ind. Eng. Chem. Res.

Author:

Wittig Roland¹,Lohmann Jürgen¹,Joh Ralph¹,Horstmann Sven¹,Gmehling Jürgen¹

Affiliation:

1. Lehrstuhl für Technische Chemie (FB9), Carl von Ossietzky Universität Oldenburg, Postfach 2503, D-26111 Oldenburg, Germany, BASF Coatings AG, Werk Münster, Postfach 6123, D-48163 Münster, Germany, Siemens Axiva GmbH & Co. KG, Industriepark Höchst, D-65926 Frankfurt/Main, Germany, and Laboratory for Thermophysical Properties (LTP GmbH), Universität Oldenburg, Postfach 2503, D-26111 Oldenburg, Germany

Publisher

American Chemical Society (ACS)

Subject

Industrial and Manufacturing Engineering,General Chemical Engineering,General Chemistry

Link

https://pubs.acs.org/doi/pdf/10.1021/ie010444j

Reference60 articles.

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

2. A Modified UNIFAC (Dortmund) Model. 3. Revision and Extension

3. Computer-operated differential static apparatus for the measurement of vapor-liquid equilibrium data

4. Vapor−Liquid Equilibria and Vapor Pressure Data for the Systems Ethyl tert-Butyl Ether + Ethanol and Ethyl tert-Butyl Ether + Water

5. Excess enthalpies for 1,1,1-trichloroethane with alkanes, ketones, and esters

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