Modeling Phase Equilibrium of H2 + n-Alkane and CO2 + n-Alkane Binary Mixtures Using a Group Contribution Statistical Association Fluid Theory Equation of State (GC−SAFT−EOS) with a kij Group Contribution Method-Reference-Cited by-同舟云学术

Modeling Phase Equilibrium of H2 + n-Alkane and CO2 + n-Alkane Binary Mixtures Using a Group Contribution Statistical Association Fluid Theory Equation of State (GC−SAFT−EOS) with a kij Group Contribution Method

Published:2006-09-01 Issue:20 Volume:45 Page:6803-6810
ISSN:0888-5885
Container-title:Industrial & Engineering Chemistry Research
language:en
Short-container-title:Ind. Eng. Chem. Res.

Author:

Thi Chi Le¹,Tamouza Sofiane¹,Passarello J-Philippe¹,Tobaly Pascal¹,de Hemptinne J-Charles¹

Affiliation:

1. Institut Français du Pétrole, 1 & 4 avenue de Bois-Préau, 92852, Rueil-Malmaison Cedex, France, and Laboratoire d'Ingénierie des Matériaux et des Hautes Pressions (LIMHP), CNRS Université Paris 13, 99 avenue J. B. Clément, 93430, Villetaneuse, France

Publisher

American Chemical Society (ACS)

Subject

Industrial and Manufacturing Engineering,General Chemical Engineering,General Chemistry

Link

https://pubs.acs.org/doi/pdf/10.1021/ie060424n

Reference27 articles.

1. Group contribution method with SAFT EOS applied to vapor liquid equilibria of various hydrocarbon series

2. Application to binary mixtures of a group contribution SAFT EOS (GC-SAFT)

3. Vapor–liquid equilibria predictions of hydrogen–hydrocarbon mixtures with the Huron–Vidal mixing rule

4. Alternate equation of state combining rules and interaction parameter generalizations for asymmetric mixtures

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