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Journal of Solution Chemistry

, Volume 47, Issue 10, pp 1578–1596 | Cite as

The Ethylbenzene/Styrene Preferential Separation with Ionic Liquids in Liquid–Liquid Extraction

  • Monika Karpińska
  • Michał Wlazło
  • Urszula DomańskaEmail author
Article
  • 199 Downloads

Abstract

The objective of this work was to explore the feasibility of using ionic liquids (ILs), namely N-ethyl-N-methylmorpholinium dicyanamide, [EMMor][DCA], (3-hydroxypropyl)-1-methylmorpholinium dicyanamide, [N-C3OHMMor][DCA], 1-(3-hydroxypropyl)-3-methylimidazolium dicyanamide, [N-C3OHMIM][DCA], 1-(3-hydroxypropyl)pyridinium dicyanamide, [N-C3OHPy][DCA], (3-cyanopropyl)pyridinium dicyanamide, [N-C3CNPy][DCA], and (3-cyanopropyl)methylpyrrolidinium dicyanamide, [N-C3CNMPyr][DCA] for the separation of ethylbenzene and styrene. The liquid–liquid equilibrium (LLE) data in ternary systems of {IL (1) + styrene (2) + ethylbenzene (3)} at T = 298.15 K and ambient pressure is presented for the six ILs synthesized by us. The final chromatography analysis of the composition of tie-lines has shown that the studied ILs are not found in the raffinate phase and they show interesting results on the selectivity and solute distribution ratio for styrene extraction. A comparison of different ILs is presented for the studied separation problem. It was observed that the best separation selectivities were found for [N-C3CNPy][DCA] (SAv = 2.38) and [N-C3OHMMor][DCA] (SAv = 2.42) in comparison with other studied ILs in this work and those presented in the literature. While the data presented here are useful from a theoretical standpoint, the possibility of applications for these ILs in technological processes is questionable because of low solute distribution ratios, especially those calculated from the masses [N-C3CNPy][DCA] (βMAv = 0.08) and [N-C3OHMMor][DCA] (βMAv = 0.07). The experimental tie-lines were correlated with the non-random two liquid NRTL model.

Keywords

Ionic liquids Separation ethylbenzene/styrene Ternary (liquid–liquid) phase diagrams Selectivity Solute distribution ratio NRTL correlation 

Notes

Acknowledgements

This work has been and is supported by the National Centre of Science (NCN) in Poland in the years 2017–2020 (UMO-2016/23/B/ST5/00145).

Supplementary material

10953_2018_755_MOESM1_ESM.docx (49 kb)
Supplementary material 1 (DOCX 49 kb)

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© Springer Science+Business Media, LLC, part of Springer Nature 2018

Authors and Affiliations

  1. 1.Department of Physical Chemistry, Faculty of ChemistryWarsaw University of TechnologyWarsawPoland
  2. 2.Industrial Chemistry Research InstituteWarsawPoland
  3. 3.Thermodynamic Research Unit, School of EngineeringUniversity of KwaZulu-NatalDurbanSouth Africa

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