| 1 |
The Eyring's Theory Combined with PR Equation of State and G(E) Mixing Rule for High-Pressure Viscosity Prediction of Binary Liquid Mixtures
He SY, Wang XP, Liu ZG
Journal of Chemical Engineering of Japan, 47(6), 443, 2014 |
| 2 |
Determination of cost-effective operating condition for CO2 capturing using 1-butyl-3-methylimidazolium tetrafluoroborate ionic liquid
Ali E, Alnashef I, Ajbar A, Mulyono S, Hizaddin HF, Hadj-Kali MK
Korean Journal of Chemical Engineering, 30(11), 2068, 2013 |
| 3 |
Effect of mixing rule boundary conditions on high pressure (liquid plus liquid) equilibrium prediction
Hsieh MK, Lin ST
Journal of Chemical Thermodynamics, 47, 33, 2012 |
| 4 |
Prediction of Critical Endpoints Based on the PR Equation of State
Yang Q, Zhu SL, Li YG
Chinese Journal of Chemical Engineering, 17(5), 791, 2009 |
| 5 |
Vapor-liquid equilibrium of binary CO2-organic solvent systems (ethanol, tetrahydrofuran, ortho-xylene, meta-xylene, para-xylene)
Knez Z, Skerget M, Ilic L, Lutge C
Journal of Supercritical Fluids, 43(3), 383, 2008 |
| 6 |
Prediction of VLE data for alternative refrigerant mixtures
Sawjanya Y, Rao YC
Korean Journal of Chemical Engineering, 24(1), 106, 2007 |
| 7 |
Determination and modelling of the high-pressure vapour-liquid equilibrium carbon dioxide-methyl acetate
Schwinghammer S, Siebenhofer M, Marr R
Journal of Supercritical Fluids, 38(1), 1, 2006 |
| 8 |
Supercritical water gasification of biomass: thermodynamic analysis with direct Gibbs free energy minimization
Tang HQ, Kitagawa K
Chemical Engineering Journal, 106(3), 261, 2005 |
