| 1 |
Isothermal vapor-liquid equilibrium data for the ethene+2,2,3-trifluoro-3-(trifluoromethyl)oxirane binary system between 258 and 308 K at pressures up to 4.5 MPa
Subramoney SC, Nelson WM, Naidoo P, Coquelet C, Richon D, Ramjugernath D
Fluid Phase Equilibria, 394, 88, 2015 |
| 2 |
Phase equilibrium data for mixtures involving 1,1,2,3,3,3-hexafluoro-1-propene with either propane or n-butane between 312 and 343 K
Subramoney SC, Nelson WM, Naidoo P, Coquelet C, Richon D, Ramjugernath D
Fluid Phase Equilibria, 406, 156, 2015 |
| 3 |
Isothermal Vapor-Liquid Equilibrium Data for the Binary System 1,1,2,3,3,3-Hexafluoro-1-propene (R1216)+2,2,3-Trifluoro-3-(trifluoromethyl)oxirane from (268.13 to 308.19) K
Nelson WM, Williams-Wynn M, Subramoney SC, Ramjugernath D
Journal of Chemical and Engineering Data, 60(3), 568, 2015 |
| 4 |
Isothermal phase (vapour plus liquid) equilibrium data for binary mixtures of propene (R1270) with either 1,1,2,3,3,3-hexafluoro-1-propene (R1216) or 2,2,3-trifluoro-3-(trifluoromethyl)oxirane in the temperature range of (279 to 318) K
Subramoney SC, Nelson WM, Courtial X, Naidoo P, Coquelet C, Richon D, Ramjugernath D
Journal of Chemical Thermodynamics, 90, 100, 2015 |
| 5 |
Isothermal vapor-liquid equilibrium data for the ethylene+1,1,2,3,3,3-hexafluoro-1-propene binary system between 258 and 308 K at pressures up to 4.56 MPa
Subramoney SC, Courtial X, Naidoo P, Coquelet C, Richon D, Ramjugernath D
Fluid Phase Equilibria, 353, 7, 2013 |
| 6 |
Experimental vapour-liquid equilibrium data and modeling for binary mixtures of 1-butene with 1,1,2,3,3,3-hexafluoro-1-propene, 2,2,3-trifluoro-3-(trifluoromethyl)oxirane, or difluoromethane
Subramoney SC, Valtz A, Coquelet C, Richon D, Naidoo P, Ramjugernath D
Journal of Chemical Thermodynamics, 61, 18, 2013 |
| 7 |
Experimental (vapour plus liquid) equilibrium data and modelling for binary mixtures of decafluorobutane with propane and 1-butene
Subramoney SC, Naidoo P, Valtz A, Coquelet C, Richon D, Ramjugernath D
Journal of Chemical Thermodynamics, 67, 134, 2013 |
| 8 |
Isothermal Vapor-Liquid Equilibrium Data for the Propan-1-ol + Dodecane System at (323.0, 343.4, 353.2, 363.1, and 369.2) K
Narasigadu C, Subramoney SC, Naidoo P, Coquelet C, Richon D, Ramjugernath D
Journal of Chemical and Engineering Data, 57(3), 862, 2012 |
| 9 |
Vapor-Liquid Equilibrium Measurements and Modeling for the Ethane (R-170) plus 1,1,2,3,3,3-Hexafluoro-1-propene (R-1216) Binary System
Subramoney SC, Valtz A, Coquelet C, Richon D, Naidoo P, Ramjugernath D
Journal of Chemical and Engineering Data, 57(11), 2947, 2012 |
| 10 |
Vapor-Liquid Equilibrium Data for Binary Systems Consisting of Either Hexafluoropropene (HFP) or 2,2,3-Trifluoro-3-(trifluoromethyl)oxirane (HFPO) with Carbon Dioxide (R-744) or 2,2-Dichloro-1,1,1-trifluoroethane (R-123)
Nelson WM, Subramoney SC, Valtz A, Coquelet C, Richon D, Naidoo P, Ramjugernath D
Journal of Chemical and Engineering Data, 56(1), 74, 2011 |
