Isobaric vapor-liquid equilibria for binary and ternary systems composed of water, 1-propanol, and 2-propanol at 100 kPa

Journal Article · Fri Nov 01 00:00:00 EST 1996 · Journal of Chemical and Engineering Data

DOI:https://doi.org/10.1021/je960108n· OSTI ID:404521

Gabaldon, C; Marzal, P; Monton, J B; Rodrigo, M A ^[1]

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1. Univ. de Valencia (Spain). Dept. de Ingenieria Quimica

Isobaric vapor-liquid equilibria data were obtained for the 2-propanol + 1-propanol binary system and the water + 1-propanol + 2-propanol ternary system at 100 kPa. The data were found to be thermodynamically consistent according to the Van Ness-Byer-Gibbs method for the binary system and according to the McDermott-Ellis method for the ternary one. The binary system is well represented by assuming ideal behavior. The binary interaction parameters obtained from this and previous work are used to predict the vapor-liquid equilibrium for the ternary system using the UNIQUAC, NRTL, and Wilson models. The ternary system is well predicted from binary data.

• OSTI ID: 404521
• Journal Information: Journal of Chemical and Engineering Data, Vol. 41, Issue 6; Other Information: PBD: Nov-Dec 1996
• Country of Publication: United States
• Language: English

Related Subjects

10 SYNTHETIC FUELS
PROPANOLS
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EQUATIONS OF STATE
DENSITY
REFRACTIVE INDEX
BOILING POINTS
EXPERIMENTAL DATA