Isothermal Vapor-Liquid Equilibria for 2-Methyl-2-butanol + 2-Methyl-1-butanol + 1-Pentanol

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 obta...

Full description

Saved in:
Bibliographic Details
Published in:Journal of chemical and engineering data 1994-07, Vol.39 (3), p.581-583
Main Authors: Aucejo, Antonio, Burguet, M. Cruz, Monton, Juan B, Munoz, Rosa, Sanchotello, Margarita, Vazquez, M. Isabel
Format: Article
Language:English
Subjects:
10 SYNTHETIC FUELS
100300 - Synthetic Fuels- Properties & Composition- (1990-)
400201 - Chemical & Physicochemical Properties
ALCOHOLS
BUTANOLS
Chemistry
DATA
DESIGN
DISTILLATION EQUIPMENT
EQUATIONS
EQUATIONS OF STATE
EQUILIBRIUM
Exact sciences and technology
EXPERIMENTAL DATA
FLUIDS
GASES
General and physical chemistry
HYDROXY COMPOUNDS
INFORMATION
INORGANIC, ORGANIC, PHYSICAL AND ANALYTICAL CHEMISTRY
Liquid-vapor equilibria
LIQUIDS
NUMERICAL DATA
ORGANIC COMPOUNDS
PENTANOLS
Phase equilibria
PHYSICAL PROPERTIES
THERMODYNAMIC PROPERTIES
VAPORS
Online Access:Get full text
Tags: Add Tag
No Tags, Be the first to tag this record!
Description
Summary: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.
ISSN:0021-9568
1520-5134
DOI:10.1021/je00015a041