Abstract
| - Diisopropyl ether (DIPE) could be a suitable gasoline additive. In this work, we report liquid−liquidequilibrium data for the ternary system isopropyl ether + ethanol + water at (298.15, 308.15, and 318.15)K. The parameters for the NRTL and UNIQUAC models were obtained by fitting the thermodynamicmodels to the experimental data. The predictive ability of the UNIFAC method was tested.
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