2007
DOI: 10.1021/je700253k
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Phase Equilibrium of Aqueous Systems Containing 3-Methyl-1-vinylimidazolium Methyl Sulfate

Abstract: This paper reports experimental data for the activity of water in aqueous solutions of 3-methyl-1-vinylimidazolium methyl sulfate (QVI) at (298 and 338) K and the solid−liquid equilibrium for the ternary system (QVI + sodium sulfate + water) at the same temperatures. QVI is an ionic monomer which is gaining importance as a monomer for water-soluble polymers. The experimental data presented here are to contribute to a database which is needed to develop and test thermodynamic models for the description/predicti… Show more

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Cited by 5 publications
(1 citation statement)
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“…To date, only a few investigations on vapor pressure/activity coefficient data measurements of one or two solvents have been reported for the IL-containing systems. It can be cited here those reported by Heintz and co-workers [7][8][9][10][11][12], Gmehling and co-workers [13][14][15], Lee and co-workers [16,17], Zhao and co-workers by [18][19][20], Wang and co-workers [21][22][23][24][25], Li and co-workers [26], Zhang and co-workers [27,28], Artl and co-workers [29][30][31], Clavar et al [32,33], Martinez-Andreu and co-workers [34,35] Fedicheva et al [36] over the whole concentration range at different temperatures in water and organic solvents in terms of isobaric VLE data (T, x, y) and a few isothermic VLE data (P, x, y). In these studies, activity coefficients of molecular solvents in the studied ionic liquids have been determined and are described formally by using various excess Gibbs free energy models such as NRTL, UNIQUAC, and UNIFAC equations.…”
Section: Introductionmentioning
confidence: 87%
“…To date, only a few investigations on vapor pressure/activity coefficient data measurements of one or two solvents have been reported for the IL-containing systems. It can be cited here those reported by Heintz and co-workers [7][8][9][10][11][12], Gmehling and co-workers [13][14][15], Lee and co-workers [16,17], Zhao and co-workers by [18][19][20], Wang and co-workers [21][22][23][24][25], Li and co-workers [26], Zhang and co-workers [27,28], Artl and co-workers [29][30][31], Clavar et al [32,33], Martinez-Andreu and co-workers [34,35] Fedicheva et al [36] over the whole concentration range at different temperatures in water and organic solvents in terms of isobaric VLE data (T, x, y) and a few isothermic VLE data (P, x, y). In these studies, activity coefficients of molecular solvents in the studied ionic liquids have been determined and are described formally by using various excess Gibbs free energy models such as NRTL, UNIQUAC, and UNIFAC equations.…”
Section: Introductionmentioning
confidence: 87%