Isothermal vapor-liquid equilibria of 1-pentanol with 2-methyl-1-butanol, 2-methyl-2-butanol, and 3-methyl-2-butanol

Journal Article · Fri Jul 01 00:00:00 EDT 1994 · Journal of Chemical and Engineering Data; (United States)

DOI:https://doi.org/10.1021/je00015a040· OSTI ID:6965284

Aucejo, A; Burguet, M C; Monton, J B; Munoz, R; Sanchotello, M; Vazquez, M I ^[1]

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

The separation of liquid mixtures through distillation is one of the most common operations in chemical industry, and the efficient design of distillation equipment requires a quantitative knowledge of vapor-liquid equilibria (VLE). Vapor-liquid equilibria were measured for binary systems of 1-pentanol + 2-methyl-1-butanol, + 2-methyl-2-butanol, and + 3-methyl-2-butanol at 373.15 K. The results are thermodynamically consistent according to the point-to-point consistency test, and deviation from ideal behavior is small in all cases.

• OSTI ID: 6965284
• Journal Information: Journal of Chemical and Engineering Data; (United States), Journal Name: Journal of Chemical and Engineering Data; (United States) Vol. 39:3; ISSN JCEAAX; ISSN 0021-9568
• Country of Publication: United States
• Language: English

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ALCOHOLS
BINARY MIXTURES
BUTANOLS
DATA
DENSITY
DESIGN
DISPERSIONS
DISTILLATION EQUIPMENT
EQUILIBRIUM
EQUIPMENT
EXPERIMENTAL DATA
FLUIDS
GASES
HYDROXY COMPOUNDS
INFORMATION
LIQUIDS
MIXTURES
NUMERICAL DATA
OPTICAL PROPERTIES
ORGANIC COMPOUNDS
PENTANOLS
PHYSICAL PROPERTIES
REFRACTIVE INDEX
THERMODYNAMIC PROPERTIES
VAPOR PRESSURE
VAPORS