1 - 14 |
Phase-Equilibria for Enzyme-Catalyzed Reactions in Supercritical Carbon-Dioxide Chrisochoou A, Schaber K, Bolz U |
15 - 25 |
A Generalized Equation of State for Liquid Density Calculation Lee HY, Liu GJ |
27 - 46 |
An Equation of State Chemical Association Model for Fluorinated Hydrocarbons and HF Kao CP, Paulaitis ME, Sweany GA, Yokozeki M |
47 - 58 |
Chain-Length Dependence of the Critical Density of Organic Homologous Series Kontogeorgis GM, Fredenslund A, Tassios DP |
59 - 78 |
Capabilities and Limitations of the Wong-Sandler Mixing Rules Coutsikos P, Kalospiros NS, Tassios DP |
79 - 102 |
An Enthalpy-Based Cubic Equation of State Mixing Rule for Cross-Prediction of Excess Thermodynamic Properties of Hydrocarbon and Halogenated Refrigerant Mixtures Peng CL, Stein FP, Gow AS |
103 - 120 |
Vapor-Pressures of 12 Alkylcyclohexanes, Cyclopentane, Butylcyclopentane and Trans-Decahydronaphthalene Down to 0.5 Pa - Experimental Results, Correlation and Prediction by an Equation of State Mokbel I, Rauzy E, Loiseleur H, Berro C, Jose J |
121 - 133 |
Experimental Values and Analysis of Mixing Heats of the Binary-Mixtures Formed by Alkyl Benzoates and N-Alkanes Ortega J, Postigo MA |
135 - 152 |
Linear Alkanoates Plus Aromatic Hydrocarbon Binary-Mixtures - New Excess Enthalpy Measurements and DISQUAC Analysis of Thermodynamic Properties Delcros S, Jimenez E, Romani L, Roux AH, Grolier JP, Kehiaian HV |
153 - 158 |
Excess-Enthalpies of Ethanol-Propanal Binary-Mixtures at 298.15 and 318.15 K Renuncio JA, Cabanas A, Coto B, Menduina C, Pando C |
159 - 165 |
Measurement of the Vapor-Pressure of 2,2,2-Trifluoroethanol and Tetraethylene Glycol Dimethyl Ether by Static Method Chaudhari SK, Patil KR, Allepus J, Coronas A |
167 - 183 |
The Effect of the Molecular Shape on the Enthalpic Behavior of Liquid-Mixtures - Cyclic Hydrocarbons in Heptane and Tetrachloromethane Marongiu B, Porcedda S, Lepori L, Matteoli E |
185 - 198 |
Isobaric VLE Data for the Binary-Systems Dibromomethane with Isomeric Butanols at 40.0 and 101.3 kPa Rodriguez V, Lafuente C, Santafe J, Royo FM, Urieta JS |
199 - 211 |
Vapor-Liquid-Equilibria .7. The Ternary-System Hexane-Methanol-Acetone at 313.15 K Oracz P, Warycha S |
213 - 218 |
The Solubility of Methane in Triethylene Glycol Monomethyl Ether Henni A, Mather AE |
219 - 229 |
Liquid-Liquid-Vapor Phase-Equilibrium Behavior of Binary Xenon Plus 1-Alkanol Mixtures Gricus TA, Luks KD, Patton CL |
231 - 241 |
Liquid-Liquid Equilibrium of the 5 Component System of N-Hexane-N-Heptane-Toluene-O-Xylene-Propylene Carbonate Salem AB, Hamad EZ |
243 - 254 |
Phase-Behavior of Random and ABC Triblock Methacrylic Polyampholytes with Poly(Vinyl Alcohol) in Water - Effect of pH and Salt Patrickios CS, Hertler WR, Hatton TA |
255 - 268 |
Excess-Enthalpies and Excess Heat-Capacities of the Ternary-System Ethanol Plus N,N-Dimethylformamide Plus Tetrahydrofuran at 298.15 K Conti G, Gianni P, Lepori L, Matteoli E |
269 - 292 |
Salt Effect on Liquid-Liquid Equilibrium of the Methyl Isobutyl Ketone-Acetic Acid-Water System at 35-Degrees-C Govindarajan M, Sabarathinam PL |
293 - 303 |
High-Pressure Vapor-Liquid and Vapor-Liquid-Liquid Equilibria for Systems Containing Supercritical Carbon-Dioxide, Water and Furfural Sako T, Sugeta T, Nakazawa N, Otake K, Sato M, Ishihara K, Kato M |
305 - 315 |
Analysis of the Electrostatic Potential Difference in Aqueous Polymer 2-Phase Systems Pfennig A, Schwerin A |