| 1 |
Hydraulic and mass transfer performances of a commercial hybrid packing: The RSP200X-Key modelling parameters for gas treatment applications
Alix P, Roesler J, Courtial X, Schultes M
Chemical Engineering Research & Design, 147, 597, 2019 |
| 2 |
Isothermal Vapor-Liquid Equilibrium Data for the 1,1,2,3,3,3-Hexafluoroprop-1-ene+1,1,2,2,3,3,4,4-Octafluorocyclobutane Binary System: Measurement and Modeling from (292 to 352) K and Pressures up to 2.6 MPa
Conradie FJ, Crouse PL, Courtial X, Nelson WM, van der Walt IJ, Ramjugernath D
Journal of Chemical and Engineering Data, 60(3), 966, 2015 |
| 3 |
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 |
| 4 |
Isothermal Vapor-Liquid Equilibrium Data for the 1,1,2,2-Tetrafluoroethene+1,1,2,3,3,3-Hexafluoroprop-1-ene Binary System: Measurement and Modeling from (248 to 283) K
Conradie FJ, Crouse PL, Courtial X, Nelson WM, van der Walt IJ, Ramjugernath D
Journal of Chemical and Engineering Data, 59(1), 82, 2014 |
| 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 |
Isothermal Vapor-Liquid Equilibrium Data and Modeling for the Ethane (R170) + Perfluoropropane (R218) System at Temperatures from (264 to 308) K
Tshibangu MM, Courtial X, Coquelet C, Naidoo P, Ramjugernath D
Journal of Chemical and Engineering Data, 58(5), 1316, 2013 |
| 7 |
Isothermal Vapor-Liquid Equilibrium Data for the 1,1,2,2-Tetrafluoroethene plus 1,1,2,2,3,3,4,4-Octafluorocyclobutane Binary System: Measurement and Modeling from (248 to 283) K
Conradie FJ, Crouse PL, Courtial X, van der Walt IJ, Ramjugernath D
Journal of Chemical and Engineering Data, 57(7), 1978, 2012 |
| 8 |
Isothermal vapor-liquid equilibrium data for the carbon dioxide (R744) + decafluorobutane (R610) system at temperatures from 263 to 353 K
Valtz A, Courtial X, Johansson E, Coquelet C, Ramjugernath D
Fluid Phase Equilibria, 304(1-2), 44, 2011 |
| 9 |
P-x data for binary systems using a novel static total pressure apparatus
Raal JD, Motchelaho AM, Perumal Y, Courtial X, Ramjugernath D
Fluid Phase Equilibria, 310(1-2), 156, 2011 |
| 10 |
Vapor-liquid equilibrium in the n-butane plus methanol system, measurement and modeling from 323.2 to 443.2 K
Courtial X, Soo CB, Coquelet C, Paricaud P, Ramjugernath D, Richon D
Fluid Phase Equilibria, 277(2), 152, 2009 |
