1 |
Experimental research on (vapor plus liquid) equilibria for the {trifluoroiodomethane (CF3I) + carbon dioxide (CO2)} system from 243.150 to 273.150 K Yuan ZK, Tu YP, Wang C, Zhao YX, Dong XQ Journal of Chemical Thermodynamics, 101, 49, 2016 |
2 |
Measurements of isothermal (vapor plus liquid) phase equilibrium for {trifluoroiodomethane (R13I1)+1,1-difluoroethane (R152a)} from T = (258.150 to 283.150) K Gong MQ, Cheng KW, Dong XQ, Guo H, Zhao YX, Wu JF Journal of Chemical Thermodynamics, 88, 90, 2015 |
3 |
(Vapor plus liquid) phase equilibrium measurements for {trifluoroiodomethane (R13I1) + propane (R290)} from T = (258.150 to 283.150) K Gong MQ, Guo H, Dong XQ, Li HY, Wu JF Journal of Chemical Thermodynamics, 79, 167, 2014 |
4 |
Measurements of (vapour plus liquid) equilibrium data for {trifluoroiodomethane (R13I1) plus isobutane (R600a)} at temperatures between (263.150 and 293.150) K Guo H, Gong MQ, Dong XQ, Wu JF Journal of Chemical Thermodynamics, 58, 428, 2013 |
5 |
Phase equilibrium for the binary azeotropic mixture of trifluoroiodomethane (R1311)+1,1,2,2-tetrafluoroethane (R134) at temperatures from 258.150 to 283.150 K Dong XQ, Gong MQ, Wu JF Fluid Phase Equilibria, 315, 35, 2012 |
6 |
(Vapour plus liquid) equilibrium data for the binary system of {trifluoroiodomethane (R13I1) + trans-1, 3, 3, 3-tetrafluoropropene (R1234ze (E))} at various temperatures from (258.150 to 298.150) K Guo H, Gong MQ, Dong XQ, Wu JF Journal of Chemical Thermodynamics, 47, 397, 2012 |
7 |
Viscosity of saturated liquid trifluoroiodomethane from 253 to 338 K Duan YY, Shi L, Han LZ, Zhu MS Fluid Phase Equilibria, 162(1-2), 303, 1999 |