Vapour + liquid) equilibrium of {diisopropyl ether (DIPE) + n-heptane + isopropanol}, {diisopropyl ether (DIPE) + n-heptane}, {diisopropyl ether (DIPE) + isopropanol} and (n-heptane + isopropanol) were measured at T = 313.15 K. Data reduction by Barker's method provides correlations for the excess m
Excess thermodynamic properties of binary and ternary mixtures containing methyl 1,1-dimethylethyl ether (MTBE),n-heptane, and methanol atT =  313.15 K
✍ Scribed by José J. Segovia; Marı́a C. Martı́n; César R. Chamorro; Miguel A. Villamañán
- Publisher
- Elsevier Science
- Year
- 1999
- Tongue
- English
- Weight
- 426 KB
- Volume
- 31
- Category
- Article
- ISSN
- 0021-9614
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✦ Synopsis
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 energy G E m using the Margules equation for the binary systems, and the Wohl expansion for the ternary. The Wilson, NRTL, and UNIQUAC models have been applied successfully to both the binary and ternary systems reported here. Using literature data of the excess molar enthalpy H E m for the same ternary mixture measured at T = 313.15 K, we have calculated the excess molar entropy S E m for the system at the same temperature.
📜 SIMILAR VOLUMES
TABLE 1. Densities ρ for the pure liquids at T = 298.15 K Liquid ρ/(g • cm -3 ) expt lit 1-Cholorooctane 0.86875 0.86876 (4) 1-Butanol 0.80575 0.80576