| 1 |
Updated versions of the generalized Soave alpha-function suitable for the Redlich-Kwong and Peng-Robinson equations of state
Pina-Martinez A, Privat R, Jaubert JN, Peng DY
Fluid Phase Equilibria, 485, 264, 2019 |
| 2 |
Solubility of caffeic acid in CO2 + ethanol: Experimental and predicted data using Cubic Plus Association Equation of State
Bitencourt RG, Palma AM, Coutinho JAP, Cabral FA, Meirelles AJA
Journal of Supercritical Fluids, 138, 238, 2018 |
| 3 |
Comparison of GERG-2008 and simpler EoS models in calculation of phase equilibrium and physical properties of natural gas related systems
Varzandeh F, Stenby EH, Yan W
Fluid Phase Equilibria, 434, 21, 2017 |
| 4 |
A consistency test for alpha-functions of cubic equations of state
Le Guennec Y, Lasala S, Privat R, Jaubert JN
Fluid Phase Equilibria, 427, 513, 2016 |
| 5 |
Volume translation methods for real-gas computational fluid dynamics simulations
Matheis J, Muller H, Lenz C, Pfitzner M, Hickel S
Journal of Supercritical Fluids, 107, 422, 2016 |
| 6 |
Soave alpha function at supercritical temperatures
Mahmoodi P, Sedigh M
Journal of Supercritical Fluids, 112, 22, 2016 |
| 7 |
PVT modeling of reservoir fluids using PC-SAFT EoS and Soave-BWR EoS
Yan W, Varzandeh F, Stenby EH
Fluid Phase Equilibria, 386, 96, 2015 |
| 8 |
Experimental and modeling study of the phase behavior of synthetic crude oil + CO2
Al Ghafri SZ, Maitland GC, Trusler JPM
Fluid Phase Equilibria, 365, 20, 2014 |
| 9 |
Reliability of the correlation allowing the k(ij) to switch from an alpha function to another one in hydrogen-containing systems
Jaubert JN, Qian JW, Privat R, Leibovici CF
Fluid Phase Equilibria, 338, 23, 2013 |
| 10 |
Volume-translated cubic EoS and PC-SAFT density models and a free volume-based viscosity model for hydrocarbons at extreme temperature and pressure conditions
Burgess WA, Tapriyal D, Morreale BD, Soong Y, Baled HO, Enick RM, Wu Y, Bamgbade BA, McHugh MA
Fluid Phase Equilibria, 359, 38, 2013 |
