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]

---

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), Vol. 39:3; ISSN 0021-9568
• Country of Publication: United States
• Language: English

Related Subjects

10 SYNTHETIC FUELS
37 INORGANIC
ORGANIC
PHYSICAL AND ANALYTICAL CHEMISTRY
BUTANOLS
THERMODYNAMIC PROPERTIES
PENTANOLS
BINARY MIXTURES
DENSITY
DESIGN
DISTILLATION EQUIPMENT
EQUILIBRIUM
EXPERIMENTAL DATA
LIQUIDS
REFRACTIVE INDEX
VAPOR PRESSURE
VAPORS
ALCOHOLS
DATA
DISPERSIONS
EQUIPMENT
FLUIDS
GASES
HYDROXY COMPOUNDS
INFORMATION
MIXTURES
NUMERICAL DATA
OPTICAL PROPERTIES
ORGANIC COMPOUNDS
PHYSICAL PROPERTIES
100300* - Synthetic Fuels- Properties & Composition- (1990-)
400201 - Chemical & Physicochemical Properties