| 1 |
Multiple Solutions When Fitting Excess Gibbs Energy Models and Implications for Process Simulation
Vasiliu D, Gottl Q, Brocker S, Burger J
Chemie Ingenieur Technik, 93(3), 490, 2021 |
| 2 |
CH4, C2H6, and C2H4 Phase Equilibria on SAPO-34 Using the Vacancy Solution Theory
Masoudi-Nejad M, Fatemi S, Joda M
Separation Science and Technology, 50(11), 1629, 2015 |
| 3 |
A generalized reference state at constant volume for the prediction of phase equilibria from low pressure model parameters: Application to size-asymmetric systems and to the Wong-Sandler mixing rule
Neau E, Escandell J, Raspo I
Chemical Engineering Science, 66(18), 4148, 2011 |
| 4 |
Measurements and thermodynamic modeling of the ethanol-water system with emphasis to the azeotropic region
Voutsas EC, Pamouktsis C, Argyris D, Pappa GD
Fluid Phase Equilibria, 308(1-2), 135, 2011 |
| 5 |
Extraction of biofuels and biofeedstocks from aqueous solutions using ionic liquids
Simoni LD, Chapeaux A, Brennecke JF, Stadtherr MA
Computers & Chemical Engineering, 34(9), 1406, 2010 |
| 6 |
Application of force field in Gibbs ensemble lattice statistics to model vapor/liquid equilibria
Arturo SG, Knox DE
Fluid Phase Equilibria, 252(1-2), 175, 2007 |
| 7 |
Simultaneous prediction of interfacial tension and phase equilibria in binary mixtures - An approach based on cubic equations of state with improved mixing rules
Mejia A, Segura H, Vega LF, Wisniak J
Fluid Phase Equilibria, 227(2), 225, 2005 |
| 8 |
Modeling of microemulsion phase diagrams from excess Gibbs energy models
Garcia-Sanchez F, Eliosa-Jimenez G, Salas-Padron A, Hernandez-Garduza O, Apam-Martinez D
Chemical Engineering Journal, 84(3), 257, 2001 |
