Article ID Journal Published Year Pages File Type
4907373 The Journal of Chemical Thermodynamics 2017 24 Pages PDF
Abstract
Liquid-liquid equilibrium (LLE) for ternary systems of heptane + alcohols (ethanol, 1-propanol and 2-propanol) + ionic liquids (ILs) were carried out at 298.15 K and atmospheric pressure. The values of distribution coefficient (β) and selectivity (S) were calculated for the systems to investigate the influence of ionic liquids' anion and length of the n-alkyl chain in alcohols on the LLE. The NRTL and UNIQUAC models were used to correlated the experimental data, and the results indicated that both the models fit the experimental systems. The UNIFAC model was used to predict the LLE behaviors of the studied systems and compare with experimental and correlated tie-lines.
Related Topics
Physical Sciences and Engineering Chemical Engineering Chemical Engineering (General)
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