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Liquid and Vapor Viscosities of Binary Refrigerant Mixtures Containing R1234yf or R1234ze(E)

  • Masoumeh Akhfash
    Masoumeh Akhfash
    Fluid Science & Resources Division, Department of Chemical Engineering, University of Western Australia, Crawley, WA 6009, Australia
  • Saif ZS. Al Ghafri
    Saif ZS. Al Ghafri
    Fluid Science & Resources Division, Department of Chemical Engineering, University of Western Australia, Crawley, WA 6009, Australia
  • Darren Rowland
    Darren Rowland
    Fluid Science & Resources Division, Department of Chemical Engineering, University of Western Australia, Crawley, WA 6009, Australia
  • Thomas J. Hughes
    Thomas J. Hughes
    Oil and Gas Engineering, Resources Engineering, Department of Civil Engineering, Monash University, Clayton, VIC 3800, Australia
  • Tomoya Tsuji
    Tomoya Tsuji
    Malaysia-Japan International Institute of Technology, Universiti Teknologi Malaysia, Kuala Lumpur 54100, Malaysia
    More by Tomoya Tsuji
  • Yukio Tanaka
    Yukio Tanaka
    Chemical Research Department, Research & Innovation Center, Mitsubishi Heavy Industries, LTD., Hiroshima 733-8553, Japan
    More by Yukio Tanaka
  • Yoshio Seiki
    Yoshio Seiki
    Global Research & Innovation Center, Mitsubishi Heavy Industries Asia Pacific PTE, LTD., Singapore 189720, Singapore
    More by Yoshio Seiki
  • , and 
  • Eric F. May*
    Eric F. May
    Fluid Science & Resources Division, Department of Chemical Engineering, University of Western Australia, Crawley, WA 6009, Australia
    *E-mail: [email protected]. Tel.: +61 8 6488 2954.
    More by Eric F. May
Cite this: J. Chem. Eng. Data 2019, 64, 3, 1122–1130
Publication Date (Web):February 19, 2019
https://doi.org/10.1021/acs.jced.8b01039
Copyright © 2019 American Chemical Society

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    Abstract

    Abstract Image

    Liquid and vapor viscosities are reported for the binary refrigerant mixtures (R125 + R152a), (R125 + R1234ze(E)), (R143a + R1234ze(E)), (R143a + R1234yf), and (R1234ze(E) + R1234yf). The measurements were made with a vibrating wire viscometer and span temperatures from (252 to 403) K and pressures from (0.9 to 4.0) MPa. The performance of the vibrating-wire apparatus was validated by measuring the viscosity of pure R152a in both the vapor and liquid regions. These measurements and previously published data were used to tune binary interaction parameters in the extended corresponding states equation model for viscosity implemented in the NIST software REFPROP 9.1. After tuning, deviations between the model and reported viscosities were reduced from between (−4 and 8)% to within ±2%.

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    Cited By

    This article is cited by 15 publications.

    1. Jingxin Zhao, Peng Hu, Nan Zhang. Molecular Simulation Studies on the Vapor–Liquid Equilibrium of CO2 + 3,3,3-Trifluoropropene (R1243zf) Binary Mixtures. The Journal of Physical Chemistry B 2024, 128 (3) , 812-823. https://doi.org/10.1021/acs.jpcb.3c04515
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    3. Mirhadi S. Sadaghiani, Arash Arami-Niya, Benjamin Marsh, Saif Z.S. Al Ghafri, Eric F. May. Vapor–Liquid Equilibria for Carbon Dioxide + 3,3,3-Trifluoropropene Binary Mixtures at Temperatures between (288 and 348) K. Journal of Chemical & Engineering Data 2021, 66 (11) , 4044-4055. https://doi.org/10.1021/acs.jced.1c00297
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    5. Tao Yang, Jun Shen, Jian Li, Chenyang Zhu, Junwei Cui, Jiangtao Wu. Viscosity Correlation of CO2, HFCs, HFOs, and Their Mixtures: Review of Experimental Data and Modeling Techniques. Fluid Phase Equilibria 2023, 575 , 113934. https://doi.org/10.1016/j.fluid.2023.113934
    6. Xiong Xiao, Dongchan Kim, Fuyu Jiao, Xiaoxian Yang, Saif Al Ghafri, Arman Siahvashi, Tomoya Tsuji, Atsuhiro Yukumoto, Yoshio Seiki, Paul L. Stanwix, Eric F. May. Viscosity, thermal conductivity, and interfacial tension study of CO2 + difluoromethane (R32). International Journal of Refrigeration 2023, 152 , 331-342. https://doi.org/10.1016/j.ijrefrig.2023.04.019
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    8. Ximei Liang, Jinrong Sun, Xianyang Meng, Jiangtao Wu. Liquid viscosity for binary mixtures of R22 + R1234ze(E) and R22 + R1234yf from (273 to 353) K at pressures up to 15 MPa. The Journal of Chemical Thermodynamics 2022, 164 , 106641. https://doi.org/10.1016/j.jct.2021.106641
    9. Dongchan Kim, Saif Z. S. Al Ghafri, Xiaoxian Yang, Sofia K. Mylona, Thomas J. Hughes, Luke McElroy, Eric F. May. High Pressure Thermal Conductivity Measurements of Ternary (Methane + Propane + Heptane) Mixtures with a Transient Hot-Wire Apparatus. International Journal of Thermophysics 2021, 42 (12) https://doi.org/10.1007/s10765-021-02907-9
    10. Saif Z.S. Al Ghafri, Masoumeh Akhfash, Thomas J. Hughes, Xiong Xiao, Xiaoxian Yang, Eric F. May. High pressure viscosity measurements of ternary (methane + propane + heptane) mixtures. Fuel Processing Technology 2021, 223 , 106984. https://doi.org/10.1016/j.fuproc.2021.106984
    11. Saif Z.S. Al Ghafri, Fuyu Jiao, Thomas J. Hughes, Arash Arami-Niya, Xiaoxian Yang, Arman Siahvashi, Armand Karimi, Eric F. May. Natural gas density measurements and the impact of accuracy on process design. Fuel 2021, 304 , 121395. https://doi.org/10.1016/j.fuel.2021.121395
    12. Dongchan Kim, Xiaoxian Yang, Arash Arami-Niya, Darren Rowland, Xiong Xiao, Saif Z.S. Al Ghafri, Tomoya Tsuji, Yukio Tanaka, Yoshio Seiki, Eric F. May. Thermal conductivity measurements of refrigerant mixtures containing hydrofluorocarbons (HFC-32, HFC-125, HFC-134a), hydrofluoroolefins (HFO-1234yf), and carbon dioxide (CO2). The Journal of Chemical Thermodynamics 2020, 151 , 106248. https://doi.org/10.1016/j.jct.2020.106248
    13. Arash Arami-Niya, Xiong Xiao, Saif Z.S. Al Ghafri, Fuyu Jiao, Martin Khamphasith, Ehsan Sadeghi Pouya, Mirhadi S. Sadaghiani, Xiaoxian Yang, Tomoya Tsuji, Yukio Tanaka, Yoshio Seiki, Eric F. May. Measurement and modelling of the thermodynamic properties of carbon dioxide mixtures with HFO-1234yf, HFC-125, HFC-134a, and HFC-32: vapour-liquid equilibrium, density, and heat capacity. International Journal of Refrigeration 2020, 118 , 514-528. https://doi.org/10.1016/j.ijrefrig.2020.05.009
    14. Yi-jian He, Lin-feng He, Shu-peng Zheng, Guang-ming Chen. Measurements of isobaric heat capacity of R143a and R227ea at liquid phase by quasi-steady scanning. Thermochimica Acta 2020, 683 , 178464. https://doi.org/10.1016/j.tca.2019.178464
    15. Saif Z.S. Al Ghafri, Ashley McKenna, Fernando F. Czubinski, Eric F. May. Viscosity of (CH4 + C3H8 + CO2 + N2) mixtures at temperatures between (243 and 423) K and pressures between (1 and 28) MPa: Experiment and theory. Fuel 2019, 251 , 447-457. https://doi.org/10.1016/j.fuel.2019.04.017

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