Modeling Vapor Liquid Phase Equilibrium for CxHy + CxHyFz Using Peng–Robinson and Perturbed-Chain SAFT-Reference-Cited by-同舟云学术

Modeling Vapor Liquid Phase Equilibrium for CxHy + CxHyFz Using Peng–Robinson and Perturbed-Chain SAFT

Published:2017-06-13 Issue:25 Volume:56 Page:7384-7389
ISSN:0888-5885
Container-title:Industrial & Engineering Chemistry Research
language:en
Short-container-title:Ind. Eng. Chem. Res.

Author:

Zhao Yanxing¹²^ORCID,Dong Xueqiang¹,Zhong Quan¹²,Zhang Haiyang³,Li Huiya¹,Shen Jun¹,Gong Maoqiong¹

Affiliation:

1. Key Laboratory of Cryogenics, Technical Institute of Physics and Chemistry, Chinese Academy of Sciences, P.O. Box 2711, Beijing 100190, China

2. University of Chinese Academy of Sciences, Beijing 100039, China

3. Technical Institute of Physics and Chemistry, Chinese Academy of Sciences, P.O. Box 2711, Beijing 100190, China

Funder

National Natural Science Foundation of China

Publisher

American Chemical Society (ACS)

Subject

Industrial and Manufacturing Engineering,General Chemical Engineering,General Chemistry

Link

https://pubs.acs.org/doi/pdf/10.1021/acs.iecr.7b00941

Reference23 articles.

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2. A New Two-Constant Equation of State

3. A simple model for temperature-independent k of the PR-vdW model for mixtures containing HCs, HFCs, PFCs, HFOs, CO2, RE170 and R13I1

4. A modified differential-model for interaction parameters in PR EoS with vdW mixing rules for mixtures containing HFCs and HCs

5. Vapor−Liquid Equilibria Predictions for New Refrigerant Mixtures Based on Group Contribution Theory

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