| 1 |
Modeling Phase Equilibria of Asymmetric Mixtures Using a Group-Contribution SAFT (GC-SAFT) with a k(ij) Correlation Method Based on London's Theory. 2. Application to Binary Mixtures Containing Aromatic Hydrocarbons, n-Alkanes, CO2, N-2, and H2S
Nguyen-Huynh D, Tran TKS, Tamouza S, Passarello JP, Tobaly P, de Hemptinne JC
Industrial & Engineering Chemistry Research, 47(22), 8859, 2008 |
| 2 |
Modeling phase equilibrium of H-2+n-alkane and CO2+n-alkane binary mixtures using a group contribution statistical association fluid theory equation of state (GC-SAFT-EOS) with a k(ij) group contribution method
Le Thi C, Tamouza S, Passarello JP, Tobaly P, de Hemptinne JC
Industrial & Engineering Chemistry Research, 45(20), 6803, 2006 |
| 3 |
Application to binary mixtures of a group contribution SAFT EOS (GC-SAFT)
Tamouza S, Passarello JP, Tobaly P, de Hemptinne JC
Fluid Phase Equilibria, 228, 409, 2005 |
| 4 |
Application of group contribution SAFT equation of state (GC-SAFT) to model phase behaviour of light and heavy esters
Thi TXN, Tamouza S, Tobaly P, Passarello JP, de Hemptinne JC
Fluid Phase Equilibria, 238(2), 254, 2005 |
| 5 |
Group contribution method with SAFT EOS applied to vapor liquid equilibria of various hydrocarbon series
Tamouza S, Passarello JP, Tobaly P, de Hemptinne JC
Fluid Phase Equilibria, 222, 67, 2004 |
