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- [32] Thermodynamic properties of 1,1,1,2-tetrafluoroethane (R-134a)+2,3,3,3-tetrafluoropropene (R-1234yf) mixtures: Measurements of the critical parameters and a mixture model based on the multi-fluid approximation INTERNATIONAL JOURNAL OF REFRIGERATION-REVUE INTERNATIONALE DU FROID, 2015, 58 : 146 - 153
- [33] Vapour-liquid equilibria for the binary systems of pentafluoroethane {(R125)+2,3,3,3-tetrafluoroprop-1-ene (R1234yf)} and {trans-1,3,3,3-tetrafluoropropene R1234ze(E)} JOURNAL OF CHEMICAL THERMODYNAMICS, 2020, 150
- [34] Comparisons of different ionic liquids combined with trans-1,3,3,3-tetrafluoropropene (R1234ze(E)) as absorption working fluids INTERNATIONAL JOURNAL OF REFRIGERATION-REVUE INTERNATIONALE DU FROID, 2018, 88 : 45 - 57
- [35] VaporLiquid Equilibrium for the Binary Systems 1,1,2,3,3,3-Hexafluoro-1-propene (R1216)+2,3,3,3-Tetrafluoroprop-1-ene (R1234yf) and 1,1,2,3,3,3-Hexafluoro-1-propene (R1216) + trans-1,3,3,3-Tetrafluoropropene (R1234ze(E)) JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2020, 65 (09): : 4215 - 4222
- [36] Phase Equilibria of Difluoromethane (R32), 1,1,1,2-Tetrafluoroethane (R134a), and trans-1,3,3,3-Tetrafluoro-1-propene (R1234ze(E)) Probed by Experimental Measurements and Monte Carlo Simulations Industrial and Engineering Chemistry Research, 2021, 60 (01): : 739 - 752
- [38] Isochoric p-ρ-T Measurements for trans-1,3,3,3-Tetrafluoropropene [R-1234ze(E)] and Trifluoroiodomethane (R13I1) at Temperatures from (205 to 353) K under Pressures up to 40 MPa JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2012, 57 (11): : 3270 - 3277
- [39] Measurements of isothermal (vapour plus liquid) equilibria data for {1,1,2,2-Tetrafluoroethane (R134) + trans-1,3,3,3-tetrafluoropropene (R1234ze (E))} at T = (258.150 to 288.150) K JOURNAL OF CHEMICAL THERMODYNAMICS, 2013, 60 : 25 - 28