Abstract
Accurate vapor–liquid equilibria were measured for the ternary system ethyl 1,1-dimethylethyl ether + n-heptane + 1-hexene using an isothermal total pressure cell. The experimental data were well correlated using Wohl expansion and Wilson, NRTL and UNIQUAC models. The system shows a slight positive deviation from the ideality. A comparison with similar ternary systems containing other ethers is also discussed in the paper.
Original language | English |
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Pages (from-to) | 12-16 |
Number of pages | 5 |
Journal | Fluid Phase Equilibria |
Volume | 265 |
Issue number | 1-2 |
Early online date | 28 Dec 2007 |
DOIs | |
Publication status | Published - 25 Mar 2008 |
Keywords
- VLE data
- ternary mixture
- ethyl 1
- 1-dimethylethyl ether (ETBE)
- n-Heptane
- 1-hexene