| 1 |
Accurate modeling of supercritical CO2 for sustainable processes: Water + CO2 and CO2 + fatty acid esters mixtures
Llovell F, Vega LF
Journal of Supercritical Fluids, 96, 86, 2015 |
| 2 |
Classification of global fluid-phase equilibrium behaviors in binary systems
Privat R, Jaubert JN
Chemical Engineering Research & Design, 91(10), 1807, 2013 |
| 3 |
Second through fifth virial coefficients for model methane-ethane mixtures
Kim HM, Schultz AJ, Kofke DA
Fluid Phase Equilibria, 351, 69, 2013 |
| 4 |
Solution thermodynamics near the liquid-liquid critical point I. First-order excess derivatives
Losada-Perez P, Blesic M, Perez-Sanchez G, Cerdeirina CA, Troncoso J, Romani L, Szydlowski J, Rebelo LPN
Fluid Phase Equilibria, 258(1), 7, 2007 |
| 5 |
Thermodynamic data of CO2-rich multi-component systems: opalescence measurements versus ASPEN PLUS (TM) computer simulation
Smejkal Q, Martin A, Kerler B
Journal of Supercritical Fluids, 24(3), 183, 2002 |
| 6 |
Transport properties of carbon dioxide plus ethane and methane plus ethane mixtures in the extended critical region
Kiselev SB, Huber ML
Fluid Phase Equilibria, 142(1-2), 253, 1998 |
| 7 |
Prediction of Thermodynamic and Transport-Properties in the One-Phase Region of Methane Plus N-Hexane Mixtures Near Their Critical End-Points
Cheng HY, Anisimov MA, Sengers JV
Fluid Phase Equilibria, 128(1-2), 67, 1997 |
