Vapor-liquid equilibria of ethanol with 2,2,4-trimethylpentane or octane 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/je00016a018· OSTI ID:6993613

Hiaki, Toshihiko; Takahashi, Kenji; Tsuji, Tomoya; Hongo, Masaru ^[1]; 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) are required for engineering use such as in the design and operation of separation processes. Isobaric vapor-liquid equilibria were measured for ethanol with 2,2,4-trimethylpentane or octane at 101.3 kPa in an equilibrium still with circulation of both the vapor and liquid phases. The results were correlated with the Wilson and nonrandom two-liquid (NRTL) equations.

• OSTI ID: 6993613
• 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
ALCOHOLS
ALKANES
BOILING POINTS
DATA
DENSITY
DESIGN
ETHANOL
EXPERIMENTAL DATA
HYDROCARBONS
HYDROXY COMPOUNDS
INFORMATION
MATHEMATICAL MODELS
NUMERICAL DATA
OCTANE
ORGANIC COMPOUNDS
PHYSICAL PROPERTIES
SEPARATION EQUIPMENT
SOLVENT PROPERTIES
THERMODYNAMIC PROPERTIES
TRANSITION TEMPERATURE