Vapor-liquid equilibria for acetone + chloroform + methanol and constituent binary systems at 101. 3 kPa

Journal Article · Sat Oct 01 04:00:00 EDT 1994 · Journal of Chemical and Engineering Data; (United States)

DOI:https://doi.org/10.1021/je00016a017· OSTI ID:6819148

Hiaki, Toshihiko ^[1]; Kurihara, Kiyofumi; Kojima, Kazuo ^[2]

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

Vapor-liquid equilibria (VLE) and azeotropic data, which are useful for the design and operation of separation processes, have been observed for many systems. Isobaric vapor-liquid equilibria for acetone + chloroform + methanol and for the constituent binary systems chloroform + methanol and chloroform + acetone were measured at 101.3 kPa using a liquid-vapor ebullition-type equilibrium still. The experimental data were correlated with the extended Redlich-Kister and Wilson equations. The data were best correlated and completely calculated for the ternary and three binary azeotropic data using the extended Redlich-Kister equation.

• OSTI ID: 6819148
• Journal Information: Journal of Chemical and Engineering Data; (United States), Journal Name: Journal of Chemical and Engineering Data; (United States) Vol. 39:4; ISSN JCEAAX; ISSN 0021-9568
• Country of Publication: United States
• Language: English

Related Subjects

37 INORGANIC, ORGANIC, PHYSICAL, AND ANALYTICAL CHEMISTRY
400105* -- Separation Procedures
ACETONE
ALCOHOLS
AZEOTROPE
BOILING POINTS
CHLORINATED ALIPHATIC HYDROCARBONS
CHLOROFORM
DATA
DENSITY
DISPERSIONS
EXPERIMENTAL DATA
HALOGENATED ALIPHATIC HYDROCARBONS
HYDROXY COMPOUNDS
INFORMATION
KETONES
MATHEMATICAL MODELS
METHANOL
MIXTURES
NUMERICAL DATA
ORGANIC CHLORINE COMPOUNDS
ORGANIC COMPOUNDS
ORGANIC HALOGEN COMPOUNDS
PHYSICAL PROPERTIES
SEPARATION PROCESSES
SOLVENT PROPERTIES
THERMODYNAMIC PROPERTIES
TRANSITION TEMPERATURE