Vapor Liquid Phase Equilibrium for Azeotropic Isobutane + trans-1,3,3,3-Tetrafluoropropene + Trifluoroiodomethane System at Temperatures from 243.150 to 283.150 K-Reference-Cited by-同舟云学术

Vapor Liquid Phase Equilibrium for Azeotropic Isobutane + trans-1,3,3,3-Tetrafluoropropene + Trifluoroiodomethane System at Temperatures from 243.150 to 283.150 K

Published:2018-02-06 Issue:3 Volume:63 Page:812-821
ISSN:0021-9568
Container-title:Journal of Chemical & Engineering Data
language:en
Short-container-title:J. Chem. Eng. Data

Author:

Zhao Yanxing¹^ORCID,Zhong Quan¹²,Wang Jingzhou¹²,Dong Xueqiang¹^ORCID,Li Huiya¹,Gao Bo¹,Shen Jun¹²,Gong Maoqiong¹²

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

Funder

Ministry of Science and Technology of the People's Republic of China

Natural Science Foundation of Beijing Municipality

Youth Innovation Promotion Association of the Chinese Academy of Sciences

National Natural Science Foundation of China

Publisher

American Chemical Society (ACS)

Subject

General Chemical Engineering,General Chemistry

Link

https://pubs.acs.org/doi/pdf/10.1021/acs.jced.7b00964

Reference29 articles.

1. Performance Comparison of Zeotropic and Azeotropic Refrigerants in Evaporation Through Inclined Tubes

2. Role of refrigerant mixtures as alternatives to CFCs

3. Vapor–liquid equilibrium data for the sulfur dioxide (SO2) + 1,1,1,2,3,3,3-heptafluoropropane (R227ea) system at temperatures from 288.07 to 403.19 K and pressures up to 5.38 MPa

4. New algorithm for calculation of azeotropes from equations of state

5. Locating All Homogeneous Azeotropes in Multicomponent Mixtures

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