| 1 |
IMPLEMENTATION OF MATHEMATICA FOR DEVELOPMENT AND APPLICATION OF EOS MODELS. I: DERIVATION OF THE EXPRESSIONS FOR HARD-CHAIN AND HARD-SPHERE COMPRESSIBILITY FACTORS
Polishuk I, Yona Y
Chemical Engineering Communications, 196(4), 443, 2009 |
| 2 |
The modified PGR equation of state: Pure-fluid predictions
Row KH, Park JK, Gasem KAM
Chemical Engineering Communications, 193(4), 438, 2006 |
| 3 |
Equations of state for the calculation of fluid-phase equilibria
Wei YS, Sadus RJ
AIChE Journal, 46(1), 169, 2000 |
| 4 |
Homotopy continuation method for calculating critical loci of binary mixtures
Wang MC, Wong DSH, Chen HY, Yan W, Guo TM
Chemical Engineering Science, 54(17), 3873, 1999 |
| 5 |
The performance of EOS models in the prediction of vapor-liquid equilibria in asymmetric natural gas mixtures
Wang LS, Gardeler H, Gmehling J
Chinese Journal of Chemical Engineering, 6(3), 213, 1998 |
| 6 |
Modeling of gas solubilities in polymers with cubic equation of state
Zhong CL, Masuoka H
Fluid Phase Equilibria, 144(1-2), 49, 1998 |
| 7 |
The evolution of multicomponent systems at high pressures : I. The high-pressure, supercritical, gas-liquid phase transition
Kenney JF
Fluid Phase Equilibria, 148(1-2), 21, 1998 |
| 8 |
Heat capacities at constant volume of pure water in the temperature range 412-693 K at densities from 250 to 925 kg center dot m(-3)
Abdulagatov IM, Dvoryanchikov VI, Kamalov AN
Journal of Chemical and Engineering Data, 43(5), 830, 1998 |
| 9 |
Improved Models for the Prediction of Activity-Coefficients in Nearly Athermal Mixtures .2. A Theoretically-Based G(E)-Model Based on the Van-der-Waals Partition-Function
Kontogeorgis GM, Nikolopoulos GI, Fredenslund A, Tassios DP
Fluid Phase Equilibria, 127(1-2), 103, 1997 |
| 10 |
EOS Mixing Rules and the Quadratic Concentration-Dependence of the 2nd Virial-Coefficient
Kemeny S, Farkas I, Deak A
Fluid Phase Equilibria, 128(1-2), 131, 1997 |
