Isothermal vapor-liquid equilibria for benzene + cyclohexane + 1-propanol and for three constituent binary systems

Journal Article · Wed Jan 01 00:00:00 EST 1997 · Journal of Chemical and Engineering Data

DOI:https://doi.org/10.1021/je9602475· OSTI ID:438916

Kurihara, Kiyofumi; Uchiyama, Masanori; Kojima, Kazuo ^[1]

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1. Nihon Univ., Tokyo (Japan). Dept. of Industrial Chemistry

Isothermal vapor-liquid equilibria were measured for the ternary system of benzene + cyclohexane + 1-propanol and its constituent binary systems of benzene + cyclohexane, cyclohexane + 1-propanol, and benzene + 1-propanol at 323.15 and 333.15 K, using the apparatus proposed in a previous study. The experimental binary data were correlated using the NRTL equation. The ternary system was predicted using the binary NRTL parameters. The average absolute percent deviations between the predicted and experimental ternary total pressures are 0.5% at 323.15 K and 0.4% at 333.15 K.

• OSTI ID: 438916
• Journal Information: Journal of Chemical and Engineering Data, Vol. 42, Issue 1; Other Information: PBD: Jan-Feb 1997
• Country of Publication: United States
• Language: English

Related Subjects

10 SYNTHETIC FUELS
BENZENE
CYCLOHEXANE
PROPANOLS
THERMODYNAMIC PROPERTIES
EQUILIBRIUM
EQUATIONS OF STATE
SEPARATION PROCESSES
DENSITY
BOILING POINTS
EXPERIMENTAL DATA