| 1 |
Predicting solid-liquid-vapor equilibria in highly asymmetric paraffinic systems with EOS-G(E) model
Yang JH, Wang W, Shi GY, Wang D, Gong J, Shi BH, Ding L, Liu Y, Song SF
Fluid Phase Equilibria, 480, 1, 2019 |
| 2 |
Extension of the group contribution NRTL-PRA EoS for the modeling of mixtures containing light gases and alcohols with water and salts
Neau E, Nicolas C, Avaullee L
Fluid Phase Equilibria, 458, 194, 2018 |
| 3 |
Investigation on vapor liquid equilibrium for strongly-zeotropic ternary mixture of 2,3,3,3-tetrafluoroprop-1-ene (R1234yf) + trifluoromethane (R23) + tetrafluoromethane (R14)
Qin YB, Wang ZL, Zhang H, Wu YL
International Journal of Heat and Mass Transfer, 114, 1135, 2017 |
| 4 |
The NRTL-PRA group contribution EoS for the simultaneous prediction of LLE, VLE and h(E) of hydrocarbon mixtures with associating compounds
Neau E, Raspo I, Escandell J
Fluid Phase Equilibria, 427, 126, 2016 |
| 5 |
A simple and generalized model to represent the vapor-liquid equilibria and the liquid-molar-volume of alcohol-alkane binary mixtures
Forero LA, Velasquez JA
Fluid Phase Equilibria, 430, 112, 2016 |
| 6 |
Solubility of polycyclic aromatic hydrocarbons in sub-critical water: A predictive approach using EoS/G(E) models
Raman AS, Chiew YC
Fluid Phase Equilibria, 399, 22, 2015 |
| 7 |
Prediction of solid polycyclic aromatic hydrocarbons solubility in water, with the NRTL-PR model
Escandell J, Raspo I, Neau E
Fluid Phase Equilibria, 362, 87, 2014 |
| 8 |
Prediction of hydrate formation conditions using G(E)-EOS and UNIQUAC models for pure and mixed-gas systems
Delavar H, Haghtalab A
Fluid Phase Equilibria, 369, 1, 2014 |
| 9 |
A self-consistent Gibbs excess mixing rule for cubic equations of state
Staudt PB, Soares RD
Fluid Phase Equilibria, 334, 76, 2012 |
| 10 |
Solubility of xylitol and sorbitol in ionic liquids - Experimental data and modeling
Carneiro AP, Rodriguez O, Macedo EA
Journal of Chemical Thermodynamics, 55, 184, 2012 |
