Capacity of ionic liquids [EMim][NTf2] and [EMpy][NTf2] for extraction of toluene from mixtures with alkanes: Comparative study of the effect of the cation
The ionic liquids 1-ethyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide, [EMim][NTf2] and1-ethyl-3-methylpyridinium bis(trifluoromethylsulfonyl)imide, [EMpy][NTf2] have been studied as solventsfor the extraction of toluene from mixtures with alkanes (heptane or cyclohexane). The liquidliquid...
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| Outros Autores: | , , |
| Formato: | article |
| Idioma: | eng |
| Publicado em: |
2012
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| Assuntos: | |
| Texto completo: | https://repositorio-aberto.up.pt/handle/10216/104946 |
| País: | Portugal |
| Oai: | oai:repositorio-aberto.up.pt:10216/104946 |
| Resumo: | The ionic liquids 1-ethyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide, [EMim][NTf2] and1-ethyl-3-methylpyridinium bis(trifluoromethylsulfonyl)imide, [EMpy][NTf2] have been studied as solventsfor the extraction of toluene from mixtures with alkanes (heptane or cyclohexane). The liquidliquidequilibria of ternary systems {heptane or cyclohexane + toluene + [EMim][NTf2] or [EMpy][NTf2]} and{heptane + cyclohexane + [EMim][NTf2] or [EMpy][NTf2]} at 298.15K and atmospheric pressure weredetermined. The solute distribution ratio and selectivity derived from the tie-lines were used to determineif these ionic liquids can be used as extraction solvents. The tie-lines were satisfactorily correlatedby means of the thermodynamic NRTL model for ternary systems with [EMpy][NTf2] and with NRTL andUNIQUAC models for the ternary systems with [EMim][NTf2]. |
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