Isothermal vapor-liquid equilibria for 2-methyl-2-butanol + 2-methyl-1-butanol + 1-pentanol

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

DOI:https://doi.org/10.1021/je00015a041· OSTI ID:7044638

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

Vapor-liquid equilibria (VLE) for 2-methyl-2-butanol + 2-methyl-1-butanol and 2-methyl-2-butanol + 2-methyl-1-butanol + 1-pentanol have been measured at 373.15 K. The binary VLE results have been correlated by different liquid-phase activity coefficient models. The binary interaction parameters obtained from Wilson, NRTL, and UNIQUAC models in this and a previously study are used to predict the VLE data for the ternary system. Vapor-liquid equilibrium (VLE) data are necessary for the design of distillation processes.

• OSTI ID: 7044638
• 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
BUTANOLS
DATA
DESIGN
DISTILLATION EQUIPMENT
EQUATIONS
EQUATIONS OF STATE
EQUILIBRIUM
EQUIPMENT
EXPERIMENTAL DATA
FLUIDS
GASES
HYDROXY COMPOUNDS
INFORMATION
LIQUIDS
NUMERICAL DATA
ORGANIC COMPOUNDS
PENTANOLS
PHYSICAL PROPERTIES
THERMODYNAMIC PROPERTIES
VAPORS