Thermodynamic properties of hydrofluoroolefin (R1234yf and R1234ze(E)) refrigerant mixtures: Density, vapour-liquid equilibrium, and heat capacity data and modelling

被引:58
作者
Al Ghafri, Saif Z. S. [1 ]
Rowland, Darren [1 ]
Akhfash, Masoumeh [1 ]
Arami-Niya, Arash [1 ]
Khamphasith, Martin [1 ]
Xiao, Xiong [1 ]
Tsuji, Tomoya [2 ]
Tanaka, Yukio [3 ]
Seiki, Yoshio [4 ]
May, Eric F. [1 ]
Hughes, Thomas J. [5 ]
机构
[1] Univ Western Australia, Dept Chem Engn, Fluid Sci & Resources Div, Crawley, WA 6009, Australia
[2] Univ Teknol Malaysia, Malaysia Japan Int Inst Technol, Kuala Lumpur 54100, Malaysia
[3] Mitsubishi Heavy Ind Co Ltd, Res & Innovat Ctr, Chem Res Dept, Hiroshima 7338553, Japan
[4] Mitsubishi Heavy Ind Asia Pacific Pte Ltd, Global Res & Innovat Ctr, Singapore 189720, Singapore
[5] Monash Univ, Dept Civil Engn, Oil & Gas Engn Resources Engn, Clayton, Vic 3800, Australia
来源
INTERNATIONAL JOURNAL OF REFRIGERATION-REVUE INTERNATIONALE DU FROID | 2019年 / 98卷
关键词
Hydrofluoroolefins; Vapour-liquid equilibrium; Density; Heat capacity; DIFFERENTIAL SCANNING CALORIMETRY; EQUATION-OF-STATE; INTERNATIONAL STANDARD FORMULATION; BUBBLE POINT PRESSURE; METHANE PLUS ETHANE; BINARY-MIXTURES; TEMPERATURES; PHASE; PROPANE; SYSTEMS;
D O I
10.1016/j.ijrefrig.2018.10.027
中图分类号
O414.1 [热力学];
学科分类号
摘要
Liquid-phase and vapour-phase densities are reported for the binary refrigerant mixtures (R125 + R1234ze(E)), (R134a + R1234ze(E)), (R143a + R1234ze(E)), (R1234ze(E) + R1234yf), (R125 + R1234yf), (R143a + R1234yf) and (R125 + R152a). The measurements span temperatures from (252 to 294) K and pressures from (0.8 to 4.2) MPa. Vapour-liquid equilibria (VLE) and liquid isobaric heat capacities are also reported for some mixtures. These measurements and previously published data were used to tune binary interaction parameters in existing Helmholtz energy models. Significant improvements in the predicted densities were achieved, for example the root mean squared relative deviation decreased from 0.33% to 0.021% for (R143a + R1234yf). The most significant improvement in the description of VLE occurred for (R1234yf + R1234ze(E)) where the root mean squared deviation in the predicted vapour phase compositions decreased from 0.010 to 0.00084 (a factor of 12). (C) 2018 Elsevier Ltd and IIR. All rights reserved.
引用
收藏
页码:249 / 260
页数:12
相关论文
共 51 条
  • [2] Measurements of saturated densities and critical parameters for the binary mixture of 2,3,3,3-tetrafluoropropene (R-1234yf) + difluoromethane (R-32)
    Akasaka, Ryo
    Tanaka, Katsuyuki
    Higashi, Yukihiro
    [J]. INTERNATIONAL JOURNAL OF REFRIGERATION-REVUE INTERNATIONALE DU FROID, 2013, 36 (04): : 1341 - 1346
  • [4] Measurement of vapor viscosity of R1234yf and its binary mixtures with R32, R125
    Dang, Yagu
    Kim, Hong Seok
    Dang, Chaobin
    Hihara, Eiji
    [J]. INTERNATIONAL JOURNAL OF REFRIGERATION-REVUE INTERNATIONALE DU FROID, 2015, 58 : 131 - 136
  • [5] Experimental measurement of vapor-liquid equilibrium for (trans-1,3,3,3-tetrafluoropropene (R1234ze(E)) + propane (R290))
    Dong, Xueqiang
    Gong, Maoqiong
    Shen, Jun
    Wu, Jianfeng
    [J]. INTERNATIONAL JOURNAL OF REFRIGERATION-REVUE INTERNATIONALE DU FROID, 2011, 34 (05): : 1238 - 1243
  • [6] Measurements of the isobaric heat capacity of pressurized liquid trans-1,3,3,3-tetrafluoropropene [R1234ze(E)] by scanning calorimetry
    Gao, Neng
    Chen, Guangming
    Li, Rong
    Wang, Yi
    He, Yijian
    Yang, Bo
    [J]. JOURNAL OF THERMAL ANALYSIS AND CALORIMETRY, 2015, 122 (03) : 1469 - 1476
  • [7] Measurements of the isobaric heat capacity of R1234yf in liquid phase at temperatures from 305 K to 355 K and pressures up to 5 MPa
    Gao, Neng
    Jiang, Yunyun
    Wu, Jie
    He, Yijian
    Chen, Guangming
    [J]. FLUID PHASE EQUILIBRIA, 2014, 376 : 64 - 68
  • [8] Measurements of thermodynamic properties for the 50 mass% R1234yf+50 mass% R1234ze(E) blend
    Higashi, Yukihiro
    [J]. SCIENCE AND TECHNOLOGY FOR THE BUILT ENVIRONMENT, 2016, 22 (08) : 1185 - 1190
  • [9] Vapor-liquid equilibria for the 1,1,1,2-tetrafluoroethane (HFC-134a)+1,1,1,2,3,3,3-heptafluoropropane (HFC-227ea) and 1,1,1-trifluoroethane (HFC-143a)+2,3,3,3-tetrafluoroprop-1-ene (HFO-1234yf) systems
    Hu, Peng
    Chen, Long-Xiang
    Chen, Ze-Shao
    [J]. FLUID PHASE EQUILIBRIA, 2013, 360 : 293 - 297
  • [10] High pressure multi-component vapor-liquid equilibrium data and model predictions for the LNG industry
    Hughes, Thomas J.
    Guo, Jerry Y.
    Baker, Corey J.
    Rowland, Darren
    Graham, Brendan F.
    Marsh, Kenneth N.
    Huang, Stanley H.
    May, Eric F.
    [J]. JOURNAL OF CHEMICAL THERMODYNAMICS, 2017, 113 : 81 - 90