| Article ID | Journal | Published Year | Pages | File Type |
|---|---|---|---|---|
| 204455 | Fluid Phase Equilibria | 2011 | 5 Pages |
Vapor–liquid equilibria (VLE) for two binary systems 1-propanol + water and methyl acetate + methanol, and the ternary mixtures with the ionic liquid 1-ethyl-3-methylimidazolium ethyl sulfate [EMIM]+[EtSO4]− as entrainer were measured by headspace gas chromatography. From the experimental VLE data, the influence of the ionic liquid on the separation factors was investigated. The experimental results for the ternary systems show that [EMIM]+[EtSO4]− has a great influence on the separation factors of the systems investigated. Furthermore, the experimental separation factors were compared with the predicted ones of other ionic liquids and conventional selective solvents using modified UNIFAC (Dortmund).
► The ionic liquid [EMIM]+[EtSO4]− is considered as entrainer for extractive distillation of two binary azeotropic systems. ► Ternary VLE data containing [EMIM]+[EtSO4]− were measured using headspace GC. ► [EMIM]+[EtSO4]− has a great influence on the separation factors of the systems investigated. ► The experimental separation factors are compared with those of other ionic liquids and typical organic conventional entrainers. ► [EMIM]+[EtSO4]− is a suitable entrainer for the separation of the binary azeotropic mixtures investigated.
