Abstract
Vapor-liquid equilibrium at 94 kPa has been determined for the systems hexane + heptane and methyl 1,1-dimethylethyl ether (MTBE) + hexane + heptane. The binary system exhibits regular, almost ideal behavior, and no azeotrope is present in the ternary system. The data were correlated by the Redlich-Kister, NRTL, Wilson, UNIQUAC, and Wisniak-Tamir equations and the appropriate parameters are reported. The models allow prediction of the activity coefficients of the ternary system from those of the pertinent binary systems.
| Original language | English |
|---|---|
| Pages (from-to) | 458-462 |
| Number of pages | 5 |
| Journal | Journal of Chemical and Engineering Data |
| Volume | 42 |
| Issue number | 3 |
| DOIs | |
| State | Published - 1 Jan 1997 |
ASJC Scopus subject areas
- General Chemistry
- General Chemical Engineering
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