1 - 10 |
Intermolecular Forces Between Hydrocarbons and Ethers, Ketones, or Alcohols Wormald CJ |
11 - 34 |
2nd Virial-Coefficients of Normal-Alkanes, Linear 1-Alkanols (and Water), Alkyl Ethers, and Their Mixtures Tsonopoulos C, Dymond JH |
35 - 44 |
Pressure Effects on the Thermodynamic Properties of (N-Hexane Plus 1-Hexanol) Binary-Mixtures Grolier JP, Randzio SL |
45 - 55 |
Ability of the Nitta-Chao Model for the Prediction of Pressure and Temperature-Dependence of the Volumetric Properties of N-Alkane Plus 1-Alkanol Systems Carballo E, Peleteiro J, Cerdeirina CA, Tovar CA, Legido JL |
57 - 72 |
Estimation of Parameters of Nitta-Chao Model for Linear Monoether Plus 1-Alkanol Mixtures Legido JL, Vijande J, Garcia J, Iglesias TP, Lopez ER, Fernandez J |
73 - 87 |
Limiting Activity-Coefficients in the 1-Alkanol Plus N-Alkane Systems - Survey, Critical-Evaluation and Recommended Values, Interpretation in Terms of Association Models Dohnal V, Vrbka P |
89 - 103 |
Vapor-Liquid-Equilibrium of the Methanol-(1,1-Dimethylethyl Methyl-Ether (Mtbe) or 1,1-Dimethylpropyl Methyl-Ether (Tame)) Systems Coto B, Mossner F, Pando C, Rubio RG, Renuncio JA |
105 - 127 |
An Exact Quasi-Chemical Equation for Excess Heat-Capacity with W-Shaped Concentration-Dependence Cobos JC |
129 - 144 |
A New Evaluation of Ppt Measurements on the Methanol Vapor-Steam Mixture and Its Pure Components with Corrections for Adsorption and Impurity Effects Bich E, Hendl H, Vogel E |
145 - 154 |
Solubility of Long-Chain N-Alkanols in Dipropyl and Dibutyl Ether Rolinska J, Krumplewska E, Hofman T |
155 - 162 |
Isothermal Vapor-Liquid-Equilibria of Binary-Mixtures Containing Methyl tert-Butyl Ether (Mtbe) and/or Substitution Hydrocarbons Lozano LM, Montero EA, Martin MC, Villamanan MA |
163 - 172 |
Excess Thermodynamic Functions for Ternary-Systems Containing Fuel Oxygenates and Substitution Hydrocarbons .1. Total-Pressure Data and G(E) for Methyl tert-Butyl Ether-Benzene-Cyclohexane at 313.15 K Segovia JJ, Martin MC, Chamorro CR, Villamanan MA |
173 - 177 |
Excess Molar Volumes of Ternary Mixtures di-N-Butyl Ether Plus 1-Pentanol Plus N-Octane at 298.15 K Jimenez E, Franjo C, Segade L, Legido JL, Andrade MI |
179 - 185 |
Excess Molar Enthalpies for di-N-Butyl Ether Plus 1-Propanol Plus N-Octane at 298.15 K Jimenez E, Franjo C, Segade L, Legido JL, Andrade MI |
187 - 192 |
Excess Molar Volumes of 1-Propanol Plus N-Polyethers at 298.15 K Serna A, Delafuente IG, Gonzalez JA, Cobos JC |
193 - 211 |
Application of the Extended Real Associated Solution Model to Predict Thermodynamic Properties of N-Alcohol Plus Linear Monoether Mixtures Hofman T, Casanova C |
213 - 227 |
Mixing Properties of (Methanol, Ethanol, or 1-Propanol) with (N-Pentane, N-Hexane, N-Heptane and N-Octane) at 298.15 K Orge B, Iglesias M, Rodriguez A, Canosa JM, Tojo J |
229 - 238 |
Experimental and Predicted Excess-Enthalpies of the Working Pairs (Methanol or Trifluoroethanol Plus Polyglycol-Ethers) for Absorption Cycles Lopez ER, Garcia J, Coronas A, Fernandez J |
239 - 246 |
Vapor-Liquid-Equilibrium of (Ethers Plus Hydrocarbons or Methanol or Water) for Motor Gasoline Modeling Clark AQ, Mcbain SE, Kilner J |
247 - 264 |
Excess Properties of Propan-1-Ol Plus Polyether and Propan-1-Ol Plus Polyamine Mixtures - Experimental Results of H-E and V-E and Application of a Multiple Cross-Association Theory-Based on the Eras Model Mohren S, Heintz A |
VII - IX |
2nd International Workshop on Vapor-Liquid-Equilibria and Related Properties in Binary and Ternary Mixtures of Ethers, Alkanes and Alkanols - Preface Deiters UK, Dymond JH |