Fluid Phase Equilibria, 1995, V 113, N 1-2, 15 Dec.
DISQUAC calculation of thermodynamic properties of ether + 1-alkanol systems.
Comparison with UNIFAC calculation
1 -- 19
S. Delcros, J.R. Quint, J.E. Grolier, H.V. Kehiaian
Determination of partial molar volumes at critical end points
21 -- 26
C.L. Patton, K.D. Luks
An implicit type EOS-GE(VP) model employing vapor
pressure standard state I. Prediction of high-pressure
vapor-liquid equilibria based on low temperature data
27 -- 43
K. Kurihara, K. Kojima
An implicit type EOS-GE(VP) model employing v
apor pressure standard state. II. Prediction of
excess enthalpy using the EOS-GE model
45 -- 60
K. Kurihara, K. Kojima
Solution algorithms and parameter sensitivity
analysis for the SPHCT equation of state
61 -- 77
R.D. Shaver, R.L. Jr. Robinson, K.A.M. Gasem
Correlation and prediction of Henry constants for
liquids and gases in five industrially important
polymers using a CS-type correlation based on the van
der Waals equation of state.
Comparison with other predictive models
79 -- 102
S. Bithas, G.M. Kontogeorgis, N. Kalospiros,
A. Fredenslund, D.P. Tassios
Improved phase boundary for one-component vapor-liquid
equilibrium: incorporating critical behavior
and cubic equations of state
103 -- 115
D.H. Smith, M. Ferer
Solid-liquid equilibria in binary mixtures of
organic compounds
117 -- 126
A. Jakob, R. Joh, C. Rose, J. Gmehling
VLE for cryogenic methyl fluoride + nitrous oxide + xenon
at 182.33 K
127 -- 138
I.M.A. Fonseca, L.Q. Lobo
Excess volumes of binary systems formed by a
2,4,6-trimethylpyridine and n-alkane
139 -- 149
T. Kasprzycka-Guttman, E. Megiel
Ternary diagram: alpha-(3-benzoylphenyl)-propionic acid
(ketoprofen) in acetone-water mixtures at different
temperatures. Experimental data and predicted results
151 -- 171
F. Espitalier, B. Biscans, P.S. Peyrigain, C. Laguerie
Densities and excess volumes of cyclohexane + hexane
between 298.15 K and 473.15 K
173 -- 184
S.A. Beg, N.M. Tukur, D.K. Al-Harbi
Bubble points measurement for system
chloroform-ethanol-benzene by inclined ebulliometer
185 -- 195
L. Haoran, H. Shijun, T. Ying