Vapor–liquid equilibria for the ternary systems of methyl tert-butyl ether + methanol + benzene and methyl tert-butyl ether + methanol + toluene and constituent binary systems at 313.15 K

Isothermal vapor–liquid equilibria (VLE) data are measured for the ternary systems of methyl tert-butyl ether (MTBE)+methanol+benzene and MTBE+methanol+toluene and constituent five binary systems, MTBE+methanol, MTBE+benzene, MTBE+toluene, methanol+benzene, and methanol+toluene, at 313.15 K. The exp...

Full description

Saved in:
Bibliographic Details
Published inFluid phase equilibria Vol. 209; no. 2; pp. 215 - 228
Main Authors Oh, Jong-Hyeok, Han, Kyu-Jin, Won, Dong-Bok, Park, So-Jin
Format Journal Article
LanguageEnglish
Published Elsevier B.V 01.01.2003
Subjects
Activity coefficient
Correlations
Excess Gibbs energy
MTBE
Ternary mixtures
Vapor–liquid equilibria
Activity coefficient
Excess Gibbs energy
Vapor–liquid equilibria
Correlations
MTBE
Ternary mixtures
Online AccessGet full text

Cover

More Information
Summary:Isothermal vapor–liquid equilibria (VLE) data are measured for the ternary systems of methyl tert-butyl ether (MTBE)+methanol+benzene and MTBE+methanol+toluene and constituent five binary systems, MTBE+methanol, MTBE+benzene, MTBE+toluene, methanol+benzene, and methanol+toluene, at 313.15 K. The experimental binary VLE data were correlated with common g E model equations. And the correlated Wilson and NRTL parameters of the constituent binary systems were used to calculate the phase behavior of the ternary mixtures. The calculated ternary VLE data using Wilson and NRTL parameters were compared with experimental ternary data.
ISSN:0378-3812
1879-0224
DOI:10.1016/S0378-3812(03)00085-2