1 |
A statistical thermodynamic model with strong adaptability for liquid mixtures Dai H, Tao DP Fluid Phase Equilibria, 473, 154, 2018 |
2 |
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 |
3 |
A modification of Wong-Sandler mixing rule for the prediction of vapor-liquid equilibria in binary asymmetric systems Zanganeh I, Sargolzaei J, Khodakarami B Korean Journal of Chemical Engineering, 28(7), 1613, 2011 |
4 |
Equation of state modeling of the phase equilibria of asymmetric CO2 + n-alkane binary systems using mixing rules cubic with respect to mole fraction Cismondi M, Mollerup JM, Zabaloy MS Journal of Supercritical Fluids, 55(2), 671, 2010 |
5 |
A combined determination of phase diagrams of asymmetric binary mixtures by equations of state and transitiometry Deiters UK, Randzio SL Fluid Phase Equilibria, 260(1), 87, 2007 |
6 |
Infinite dilution activity coefficients, specific retention volumes and solvation thermodynamics of hydrocarbons in C78H158 branched alkane solvent Dallos A, Kresz R Fluid Phase Equilibria, 248(1), 78, 2006 |
7 |
A modified free-volume-based model for predicting vapor-liquid and solid-liquid equilibria for size asymmetric systems Radfarnia HR, Ghotbi C, Taghikhani V, Kontogeorgis GM Fluid Phase Equilibria, 234(1-2), 94, 2005 |
8 |
Vapor-liquid equilibria calculation for asymmetric systems using Patel-Teja equation of state with a new mixing rule Gao J, Li LD, Zhu ZY, Ru SG Fluid Phase Equilibria, 224(2), 213, 2004 |
9 |
Transitiometric determination of the three-phase curve in asymmetric binary systems Randzio SL, Stachowiak C, Grolier JPE Journal of Chemical Thermodynamics, 35(4), 639, 2003 |
10 |
Prediction of solid-gas equilibria with the Peng-Robinson equation of state Coutsikos P, Magoulas K, Kontogeorgis GM Journal of Supercritical Fluids, 25(3), 197, 2003 |