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- [22] Experimental measurements and modelling of vapor-liquid equilibria for four mixtures of 2,3,3,3-tetrafluoropropene (R1234yf) with 1,1,1,2-tetrafluoroethane (R134a) or 1,1-difluoroethane (R152a) or trans-1-chloro-3,3,3-Trifluoropropene (R1233zd(E)) or 2-Chloro-3,3,3-tri-fluoropropene (R1233xf) (vol 140, pg 172, 2022) INTERNATIONAL JOURNAL OF REFRIGERATION, 2022, 144 : 366 - 367
- [23] Compressed liquid densities of binary mixtures of difluoromethane (R32) and 2,3,3,3-tetrafluoroprop-1-Ene (R1234yf) at temperatures from (283 to 363) K and pressures up to 100 MPa JOURNAL OF CHEMICAL THERMODYNAMICS, 2020, 141
- [26] 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
- [27] Vapor-liquid equilibrium and molecular simulation data for carbon dioxide (CO2) + trans-1,3,3,3-tetrafluoroprop-1-ene (R-1234ze(E)) mixture at temperatures from 283.32 to 353.02 K and pressures up to 7.6 MPa (vol 98, pg 362, 2019) INTERNATIONAL JOURNAL OF REFRIGERATION-REVUE INTERNATIONALE DU FROID, 2019, 104 : 386 - 389
- [28] 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 -: Representation of the critical point and azeotrope temperature dependence FLUID PHASE EQUILIBRIA, 2004, 220 (01) : 77 - 83