Measurements of isothermal (vapor + liquid) equilibrium for the (propane + cis-1,3,3,3-tetrafluoropropene) system at temperatures from (253.150 to 293.150) K

Maoqiong Gong; Yanxing Zhao; Xueqiang Dong; Hao Guo; Jun Shen; Jianfeng Wu

doi:10.1016/j.jct.2016.03.018

Measurements of isothermal (vapor + liquid) equilibrium for the (propane + cis-1,3,3,3-tetrafluoropropene) system at temperatures from (253.150 to 293.150) K

Maoqiong Gong^*, Yanxing Zhao, Xueqiang Dong, Hao Guo, Jun Shen, Jianfeng Wu

^*Corresponding author for this work

Research output: Contribution to journal › Article › peer-review

23 Citations (Scopus)

Abstract

cis-1,3,3,3-Tetrafluoropropene, with zero ozone depleting potential and low global warming potential, has received much attention in recent years. In this work, the (vapor + liquid) phase equilibrium for the (propane + cis-1,3,3,3-tetrafluoropropene) binary system was investigated using an apparatus based on the recirculation method over the temperature range from (253.150 to 293.150) K. The VLE results were correlated by the PR-VDW model and PR-HV-NRTL model. Both models can give satisfactory results and the PR-HV-NRTL model exhibits better performance than PR-VDW model on the VLE description for this binary system. No azeotropic behavior was observed during the experiment.

Original language	English
Pages (from-to)	319-323
Number of pages	5
Journal	Journal of Chemical Thermodynamics
Volume	98
DOIs	https://doi.org/10.1016/j.jct.2016.03.018
Publication status	Published - Jul 2016
Externally published	Yes

Keywords

Propane (R290)
Refrigerants
Vapor liquid equilibrium (VLE)
cis-1,3,3,3-Tetrafluoropropene {R1234ze(Z)}

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10.1016/j.jct.2016.03.018

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Gong, M., Zhao, Y., Dong, X., Guo, H., Shen, J., & Wu, J. (2016). Measurements of isothermal (vapor + liquid) equilibrium for the (propane + cis-1,3,3,3-tetrafluoropropene) system at temperatures from (253.150 to 293.150) K. Journal of Chemical Thermodynamics, 98, 319-323. https://doi.org/10.1016/j.jct.2016.03.018

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title = "Measurements of isothermal (vapor + liquid) equilibrium for the (propane + cis-1,3,3,3-tetrafluoropropene) system at temperatures from (253.150 to 293.150) K",

abstract = "cis-1,3,3,3-Tetrafluoropropene, with zero ozone depleting potential and low global warming potential, has received much attention in recent years. In this work, the (vapor + liquid) phase equilibrium for the (propane + cis-1,3,3,3-tetrafluoropropene) binary system was investigated using an apparatus based on the recirculation method over the temperature range from (253.150 to 293.150) K. The VLE results were correlated by the PR-VDW model and PR-HV-NRTL model. Both models can give satisfactory results and the PR-HV-NRTL model exhibits better performance than PR-VDW model on the VLE description for this binary system. No azeotropic behavior was observed during the experiment.",

keywords = "Propane (R290), Refrigerants, Vapor liquid equilibrium (VLE), cis-1,3,3,3-Tetrafluoropropene {R1234ze(Z)}",

author = "Maoqiong Gong and Yanxing Zhao and Xueqiang Dong and Hao Guo and Jun Shen and Jianfeng Wu",

year = "2016",

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journal = "Journal of Chemical Thermodynamics",

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AU - Gong, Maoqiong

AU - Zhao, Yanxing

AU - Dong, Xueqiang

AU - Guo, Hao

AU - Shen, Jun

AU - Wu, Jianfeng

PY - 2016/7

Y1 - 2016/7

N2 - cis-1,3,3,3-Tetrafluoropropene, with zero ozone depleting potential and low global warming potential, has received much attention in recent years. In this work, the (vapor + liquid) phase equilibrium for the (propane + cis-1,3,3,3-tetrafluoropropene) binary system was investigated using an apparatus based on the recirculation method over the temperature range from (253.150 to 293.150) K. The VLE results were correlated by the PR-VDW model and PR-HV-NRTL model. Both models can give satisfactory results and the PR-HV-NRTL model exhibits better performance than PR-VDW model on the VLE description for this binary system. No azeotropic behavior was observed during the experiment.

AB - cis-1,3,3,3-Tetrafluoropropene, with zero ozone depleting potential and low global warming potential, has received much attention in recent years. In this work, the (vapor + liquid) phase equilibrium for the (propane + cis-1,3,3,3-tetrafluoropropene) binary system was investigated using an apparatus based on the recirculation method over the temperature range from (253.150 to 293.150) K. The VLE results were correlated by the PR-VDW model and PR-HV-NRTL model. Both models can give satisfactory results and the PR-HV-NRTL model exhibits better performance than PR-VDW model on the VLE description for this binary system. No azeotropic behavior was observed during the experiment.

KW - Propane (R290)

KW - Refrigerants

KW - Vapor liquid equilibrium (VLE)

KW - cis-1,3,3,3-Tetrafluoropropene {R1234ze(Z)}

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DO - 10.1016/j.jct.2016.03.018

M3 - Article

AN - SCOPUS:84962224535

SN - 0021-9614

VL - 98

SP - 319

EP - 323

JO - Journal of Chemical Thermodynamics

JF - Journal of Chemical Thermodynamics

ER -

Measurements of isothermal (vapor + liquid) equilibrium for the (propane + cis-1,3,3,3-tetrafluoropropene) system at temperatures from (253.150 to 293.150) K

Abstract

Keywords

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