| 1 |
Isothermal vapor-liquid equilibria for the pentafluoroethane plus propane and pentafluoroethane+1,1,1,2,3,3,3-heptafluoropropane systems
Hou SX, Duan YY
Fluid Phase Equilibria, 290(1-2), 121, 2010 |
| 2 |
Vapour-liquid equilibrium measurements and correlation of the difluoromethane (R32) plus propane (R290) plus 1,1,1,2,3, 3,3-heptafluoropropane (R227ea) ternary mixture at temperatures from 269.85 to 328.35 K
Coquelet C, Chareton A, Richon D
Fluid Phase Equilibria, 218(2), 209, 2004 |
| 3 |
Isothermal vapour plus liquid equilibrium measurements and correlation for the dimethyl ether+1,1,1,2,3,3,3-heptafluoropropane and the propane+1,1,1,2,3,3,3-heptafluoropropane systems
Bobbo S, Fedele L, Scattolini M, Camporese R, Stryjek R
Fluid Phase Equilibria, 224(1), 119, 2004 |
| 4 |
Use of artificial neural networks for calculating derived thermodynamic quantities from volumetric property data
Laugier S, Richon D
Fluid Phase Equilibria, 210(2), 247, 2003 |
| 5 |
Vapor-liquid equilibrium data for the propane plus 1,1,1,2,3,3,3-heptafluoropropane (R227ea) system at temperatures from 293.16 to 353.18 K and pressures up to 3.4 MPa
Valtz A, Coquelet C, Baba-Ahmed A, Richon D
Fluid Phase Equilibria, 202(1), 29, 2002 |
