| 1 |
Vapor-liquid equilibrium data for the (hexafluoroethane+1,1,1,2-tetrafluoroethane) system at temperatures from 263 to 353 K and pressures up to 4.16 MPa
Madani H, Valtz A, Coquelet C, Meniai AH, Richon D
Fluid Phase Equilibria, 268(1-2), 68, 2008 |
| 2 |
Isothermal P, x, y data for the argon plus carbon dioxide system at six temperatures from 233.32 to 299.21 K and pressures up to 14 MPa
Coquelet C, Valtz A, Dieu F, Richon D, Arpentinier P, Lockwood F
Fluid Phase Equilibria, 273(1-2), 38, 2008 |
| 3 |
(Vapor plus liquid) equilibrium data for (carbon dioxide+1,1-difluoroethane) system at temperatures from (258 to 343) K and pressures up to about 8 MPa
Madani H, Valtz A, Coquelet C, Meniai AH, Richon D
Journal of Chemical Thermodynamics, 40(10), 1490, 2008 |
| 4 |
Vapor-liquid equilibrium data for the hexafluoroethane plus carbon dioxide system at temperatures from 253 to 297 K and pressures up to 6.5 MPa
Valtz A, Coquelet C, Richon D
Fluid Phase Equilibria, 258(2), 179, 2007 |
| 5 |
Vapor-liquid equilibrium data for the carbon dioxide(CO2) plus difluoromethane (R32) system at temperatures from 283.12 to 343.25 K and pressures up to 7.46 MPa
Rivollet F, Chapoy A, Coquelet C, Richon D
Fluid Phase Equilibria, 218(1), 95, 2004 |
| 6 |
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
Valtz A, Coquelet C, Richon D
Fluid Phase Equilibria, 220(1), 77, 2004 |
| 7 |
Vapor-liquid equilibrium data for the CO2+1, 1,1,2,3,3,3,-heptafluoropropane (R227ea) system at temperatures from 276.01 to 367.30 K and pressures up to 7.4 MPa
Valtz A, Coquelet C, Baba-Ahmed A, Richon D
Fluid Phase Equilibria, 207(1-2), 53, 2003 |
