| 1 - 22 |
Further Development, Status and Results of the Psrk Method for the Prediction of Vapor-Liquid-Equilibria and Gas Solubilities
Fischer K, Gmehling J |
| 23 - 32 |
Evaluation of the Carboxylate Chlorine Interaction Parameters Using the DISQUAC Group-Contribution Model
Farkova J, Wichterle I, Kehiaian HV |
| 33 - 44 |
Methane Hydrocarbon Interaction Parameters Correlation for the Peng-Robinson and the T-Mpr Equation of State
Kordas A, Magoulas K, Stamataki S, Tassios D |
| 45 - 61 |
Improving Predictions of Equation of State by Modifying Its Parameters for Super Critical Components of Hydrocarbon Reservoir Fluids
Danesh A, Xu DH, Tehrani DH, Todd AC |
| 63 - 87 |
Application of the Zeroth Approximation of the DISQUAC Model to Cyclohexane Plus N-Alkane Mixtures Using Different Combinatorial Entropy Terms
Gonzalez JA, Delafuente I, Cobos JC, Casanova C, Aitkaci A |
| 89 - 99 |
Prediction of Liquid Density of LNG, N-2, H2S and CO2 Multicomponent Systems by the Corgc Equation of State
Nasrifar K, Moshfeghian M |
| 101 - 123 |
Modeling of Thermodynamic Properties of Associated Solutions with Equilibrium-Constants Defined on Activities
Schafer B, Lacmann R |
| 125 - 129 |
Vapor-Liquid-Equilibrium in the Carbon Dioxide-Ethyl Propanoate System at Pressures from 2 to 9 MPa and Temperatures from 303 to 323 K
Wagner Z |
| 131 - 149 |
Application of the Eras Model to H-E and V-E of 1-Alkanol Plus 1-Alkene and 1-Alkanol Plus 1-Alkyne Mixtures
Letcher TM, Mercerchalmers J, Schnabel S, Heintz A |
| 151 - 156 |
Excess Molar Volumes of Binary-Mixtures Containing Ethylbenzene and Isomeric Xylenes at 303.65, 312.65 and 321.65 K
Jain DV, Chadha R, Sehgal SK |
| 157 - 162 |
On the Temperature Calibration of a Thermooptical Apparatus
Pfohl O, Hino T, Prausnitz JM |
| 163 - 165 |
On the Temperature Calibration of a Thermooptical Apparatus
Saraiva A, Persson O |
| 167 - 168 |
The Correlation of the Vapor-Liquid-Equilibrium in Hydrogen Sulfide-Paraffin Hydrocarbons Using the Peng-Robinson Equation
Carroll JJ, Mather AE |
