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

Journal Article · Tue Dec 31 23:00:00 EST 1996 · 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, Journal Name: Journal of Chemical and Engineering Data Journal Issue: 1 Vol. 42; ISSN JCEAAX; ISSN 0021-9568
• Country of Publication: United States
• Language: English

Related Subjects

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