Vapor–Liquid Equilibria of the CH4 + CO2 + H2S Ternary System with Two Different Global Compositions: Experiments and Modeling-Reference-Cited by-同舟云学术

Vapor–Liquid Equilibria of the CH4 + CO2 + H2S Ternary System with Two Different Global Compositions: Experiments and Modeling

Published:2020-03-06 Issue:4 Volume:65 Page:1802-1813
ISSN:0021-9568
Container-title:Journal of Chemical & Engineering Data
language:en
Short-container-title:J. Chem. Eng. Data

Author:

Theveneau Pascal¹,Xu Xiaochun²,Baudouin Olivier³,Jaubert Jean-Noël²^ORCID,Ceragioli Paola⁴,Coquelet Christophe¹^ORCID

Affiliation:

1. MINES ParisTech, PSL University, CTP-Centre of Thermodynamics of Processes, 35 rue Saint Honoré, 77300 Fontainebleau, France

2. Université de Lorraine, École Nationale Supérieure des Industries Chimiques, Laboratoire Réactions et Génie des Procédés (UMR CNRS 7274), 1 rue Grandville, 54000 Nancy, France

3. ProSim SA, Immeuble Stratège A, 51 rue Ampère, 31670 Labège, France

4. Eni UPS, Via Maritano 26, San Donato Milanese, 20097 Milano, Italy

Publisher

American Chemical Society (ACS)

Subject

General Chemical Engineering,General Chemistry

Link

https://pubs.acs.org/doi/pdf/10.1021/acs.jced.9b01082

Reference47 articles.

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2. 9 Mixing and combining rules

3. VLE predictions with the Peng–Robinson equation of state and temperature dependent kij calculated through a group contribution method

4. Prediction of Thermodynamic Properties of Alkyne-Containing Mixtures with the E-PPR78 Model

5. Relationship between the binary interaction parameters (kij) of the Peng–Robinson and those of the Soave–Redlich–Kwong equations of state: Application to the definition of the PR2SRK model

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