Tables of Contents service for
Fluid Phase Equilibria

• Preface
  Deiters, U.K. and Dymond, J.H.
  page vii-ix
• Intermolecular forces between hydrocarbons and ethers, ketones, or alcohols
  Wormald, C.J.
  page 1-10
• Second virial coefficients of normal alkanes, linear 1-alkanols (and water), alkyl ethers, and their mixtures
  Tsonopoulos, C. and Dymond, J.H.
  page 11-34
• Pressure effects on the thermodynamic properties of (n-hexane + 1-hexanol) binary mixtures
  Grolier, J.-P.E. and Randzio, S.L.
  page 35-44
• Ability of the Nitta-Chao model for the prediction of pressure and temperature dependence of the volumetric properties of n-alkane + 1-alkanol systems
  Carballo, E., Peleteiro, J., Cerdeirina, C.A., Tovar, C.A. and Legido, J.L.
  page 45-55
• Estimation of parameters of Nitta-Chao model for linear monoether + 1-alkanol mixtures
  Legido, J.L., Vijande, J., Garcia, J., Iglesias, T.P., Lopez, E.R. and Fernandez, J.
  page 57-72
• Limiting activity coefficients in the 1-alkanol + n-alkane systems: survey, critical evaluation and recommended values, interpretation in terms of association models
  Dohnal, V. and Vrbka, P.
  page 73-87
• 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, R.G. and Renuncio, J.A.R.
  page 89-103
• An exact quasi-chemical equation for excess heat capacity with W-shaped concentration dependence
  Cobos, J.C.
  page 105-127
• A new evaluation of pT measurements on the methanol vapor-steam mixture and its pure components with corrections for adsorption and impurity effects
  Bich, E., Hendl, H. and Vogel, E.
  page 129-144
• Solubility of long-chain n-alkanols in dipropyl and dibutyl ether
  Rolinska, J., Krumplewska, E. and Hofman, T.
  page 145-154
• Isothermal vapor-liquid equilibria of binary mixtures containing methyl tert-butyl ether (MTBE) and/or substitution hydrocarbons
  Lozano, L.M., Montero, E.A., Martin, M.C. and Villamanan, M.A.
  page 155-162
• 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, J.J., Martin, M.C., Chamorro, C.R. and Villamanan, M.A.
  page 163-172
• Excess molar volumes of ternary mixtures di-n-butyl ether + 1-pentanol + n-octane at 298.15 K
  Jimenez, E., Franjo, C., Segade, L., Legido, J.L. and Paz Andrade, M.I.
  page 173-177
• Excess molar enthalpies for di-n-butyl ether + 1-propanol + n-octane at 298.15 K
  Jimenez, E., Franjo, C., Segade, L., Legido, J.L. and Paz Andrade, M.I.
  page 179-185
• Excess molar volumes of 1-propanol + n-polyethers at 298.15 K
  Serna, A., Garcia de la Fuente, I., Gonzalez, J.A. and Cobos, J.C.
  page 187-192
• Application of the extended real associated solution model to predict thermodynamic properties of n-alcohol + linear monoether mixtures
  Hofman, T. and Casanova, C.
  page 193-211
• 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, J.M. and Tojo, J.
  page 213-227
• Experimental and predicted excess enthalpies of the working pairs (methanol or trifluoroethanol + polyglycol ethers) for absorption cycles
  Lopez, E.R., Garcia, J., Coronas, A. and Fernandez, J.
  page 229-238
• Vapour-liquid equilibrium of (ethers + hydrocarbons or methanol or water) for motor gasoline modelling
  Clark, A.Q., McBain, S.E. and Kilner, J.
  page 239-246
• Excess properties of propan-1-ol + polyether and propan-1-ol + 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. and Heintz, A.
  page 247-264
• Subject Index
  page 265
• Author Index
  page 267
• Contents of Volume 133 (1997)
  page 269-270