Vapor-liquid equilibria of binary mixtures containing methyl tert-butyl ether (MTBE) and/or substitution hydrocarbons at 298.15 K and 313.15 K
✍ Scribed by Luis M. Lozano; Eduardo A. Montero; María C. Martín; Miguel A. Villamañán
- Publisher
- Elsevier Science
- Year
- 1995
- Tongue
- English
- Weight
- 544 KB
- Volume
- 110
- Category
- Article
- ISSN
- 0378-3812
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We report liquid-liquid equilibrium data for the ternary system {x1tert-butyl methyl ether(C5H12O)+x2water+(1-x1-x2)1-octanol} at 298.15 and 308.15 K. The data were satisfactorily fitted with UNIQUAC and NRTL equations, and were satisfactorily predicted by the UNIFAC group contribution method.
Vapour + liquid) equilibrium of {methyl 1,1-dimethylethyl ether (MTBE) + n-heptane + methanol}, {methyl 1,1-dimethylethyl ether (MTBE) + methanol}, and (methanol + n-heptane) have been measured at T = 313.15 K. The data reduction by Barker's method provides correlations for the excess molar Gibbs en