| 1 |
Publicly available models to predict normal boiling point of organic compounds
Oprisiu I, Marcou G, Horvath D, Brunel DB, Rivollet F, Varnek A
Thermochimica Acta, 553, 60, 2013 |
| 2 |
P rho T Data for Hydrogen Sulfide plus Propane from (263 to 363) K at Pressures up to 40 MPa
Jarne C, Rivollet F, Richon D
Journal of Chemical and Engineering Data, 56(1), 84, 2011 |
| 3 |
Measurements of Liquid-Liquid Equilibria for a Methanol plus Glycerol plus Methyl Oleate System and Prediction Using Group Contribution Statistical Associating Fluid Theory
Barreau A, Brunella I, de Hemptinne JC, Coupard V, Canet X, Rivollet F
Industrial & Engineering Chemistry Research, 49(12), 5800, 2010 |
| 4 |
New volume translation for cubic equations of state
Laugier S, Rivollet F, Richon D
Fluid Phase Equilibria, 259(1), 99, 2007 |
| 5 |
Measurement of physical properties of refrigerant mixtures. Determination of phase diagrams
Coquelet C, Rivollet F, Jarne C, Valtz A, Richon D
Energy Conversion and Management, 47(20), 3672, 2006 |
| 6 |
P rho T and VLE for ethane plus hydrogen sulfide from (254.05 to 363.21) K at pressures up to 20 MPa
Rivollet F, Jarne C, Richon D
Journal of Chemical and Engineering Data, 50(6), 1883, 2005 |
| 7 |
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 |
