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A new method to construct equations of state and some examples

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Hong-Yi, L.
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1992 |
Fluid
Phase Equilibria
81 (C), pp. 153-164
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1
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Vapor-liquid-liquid equilibria for the propane-furfural and
propylene-furfural systems

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Noda, K., Watanabe, H., Iwamoto, S.
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1992 |
Fluid
Phase Equilibria
81 (C), pp. 205-215
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1
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Phase equilibria in very dilute mixtures of water and unsaturated
chlorinated hydrocarbons and of water and benzene

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Cooling, M.R., Khalfaoui, B., Newsham, D.M.T.
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1992 |
Fluid
Phase Equilibria
81 (C), pp. 217-229
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12
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High pressure vapor liquid equilibria at 293 K for systems containing
nitrogen, methane and carbon dioxide

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Xu, N., Dong, J., Wang, Y., Shi, J.
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1992 |
Fluid
Phase Equilibria
81 (C), pp. 175-186
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13
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Critical point calculations for oil reservoir fluid systems using the
SPHCT equation of state

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García-Sánchez, F., Ruiz-Cortina, J.L., Lira-Galeana, C., Ponce-Ramírez, L.
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1992 |
Fluid
Phase Equilibria
81 (C), pp. 39-84
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8
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Vapour pressures of butan-1-ol with n-hexadecane between 293.18 and
323.18 K. Description of butan-1-ol + n-alkane systems by ERAS
model

Show Abstract
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Baños, I., Sánchez, F., Pérez, P., Valero, J., Gracia, M.
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1992 |
Fluid
Phase Equilibria
81 (C), pp. 165-174
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5
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Standard states, reference states and finite-concentration effects in
near-critical mixtures with applications to aqueous solutions

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Sengers, J.M.H.L., Harvey, A.H., Crovetto, R., Gallagher, J.S.
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1992 |
Fluid
Phase Equilibria
81 (C), pp. 85-107
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13
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Correlation of vapour-liquid equilibria for tautomeric mixtures of
acetyl-acetone with non-associated components. I. Nagata and Y.
Fukushima, Fluid phase equilibria, 68 (1991) 1-12
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[No author name available]
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1992 |
Fluid
Phase Equilibria
81 (C), pp. 349
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0
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Comparison of the efficacy and tolerance of a garlic preparation vs.
bezafibrate

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Holzgartner, H., Schmidt, U., Kuhn, U.
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1992 |
Arzneimittel-Forschung/Drug
Research
42 (12), pp. 1473-1477
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36
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Cutoff effect of n-alkanols in an excitable model membrane composed of
dioleyl phosphate

Show Abstract
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Iiyama, S., Toko, K., Murata, T., Ichinose, H., Suezaki, Y., Kamaya, H., Ueda, I., Yamafuji, K.
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1992 |
Biophysical
Chemistry
45 (2), pp. 91-100
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1
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Vapour-liquid equilibria. VI. The ternary system acetone - hexane -
cyclohexane at 313.15 K

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Góral, M., Oracz, P., Warycha, S.
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1992 |
Fluid
Phase Equilibria
81 (C), pp. 261-272
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11
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Application of the modified Kumar-Starling equation of state to predict
the phase behavior of mixtures in the near-critical region

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Chu, J.-Z., Zuo, Y.-X., Guo, T.-M.
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1992 |
Fluid
Phase Equilibria
81 (C), pp. 17-38
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1
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On the consistency of SEMAC equations
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Sayar, A.A.
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1992 |
Fluid
Phase Equilibria
81 (C), pp. 347-348
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0
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Multiphase behavior of binary and ternary systems of heavy aromatic
hydrocarbons with supercritical carbon dioxide. Part I. Experimental
results

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Chung, S.T., Shing, K.S.
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1992 |
Fluid
Phase Equilibria
81 (C), pp. 321-341
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32
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Structure/histotoxicity relationship of parenteral iron
preparations

Show Abstract
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Geisser, P., Baer, M., Schaub, E.
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1992 |
Arzneimittel-Forschung/Drug
Research
42 (12), pp. 1439-1452
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77
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Excess molar enthalpies of binary mixtures ethylbenzene + propylbenzene,
+ butylbenzene and + hexylbenzene at 298.15, 308.15 and 318.15 K

Show Abstract
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Jain, D.V.S., Dhar, N.S.
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1992 |
Fluid
Phase Equilibria
81 (C), pp. 231-239
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0
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The predictive capability of the UNIFAC equation for the calculation of
liquid-liquid equilibria with chemical reactions in Tributyl Phosphate
Extraction Systems for Nitric Acid and Uranyl Nitrate

Show Abstract
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Chen, J., Li, Z., Lu, J., Li, Y.
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1992 |
Fluid
Phase Equilibria
81 (C), pp. 1-15
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4
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Comments concerning "On the isobaric vapour-liquid equilibrium of the
cyclohexanol-phenylmethanol binary at 101.325 ± 0.067 kPa"

Show Abstract
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Acree Jr., W.E.
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1992 |
Fluid
Phase Equilibria
81 (C), pp. 343-345
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0
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Phase equilibrium study for the separation and fractionation of fatty
oil components using supercritical carbon dioxide

Show Abstract
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Bharath, R., Inomata, H., Adschiri, T., Arai, K.
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1992 |
Fluid
Phase Equilibria
81 (C), pp. 307-320
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54
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Excess molar heat capacities of binary mixtures of ethylbenzene with
xylenes from 303.65 to 321.65 K

Show Abstract
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Jain, D.V.S., Chadha, R., Sehgal, S.K.
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1992 |
Fluid
Phase Equilibria
81 (C), pp. 273-283
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5
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