2012Journal of Chemical & Engineering DataRequires access

Isobaric Vapor–Liquid Equilibrium for Methanol + Dimethyl Carbonate + 1-Octyl-3-methylimidazolium Tetrafluoroborate

Qunsheng Li, Wei Zhu, Yongquan Fu, Haichuan Wang, Lun Li, Baohua Wang

Open publisher page 37 citations

Abstract

Isobaric vapor–liquid equilibrium data for {methanol (1) + dimethyl carbonate (2) + 1-octyl-3-methylimidazolium (3)} where 3 is an ionic liquid ([OMIM] + [BF 4 ] − ) were obtained at 101.32 kPa using a modified Othmer still. The results indicated that [OMIM] + [BF 4 ] − can transfer the azeotropic point and totally eliminate the azeotropic phenomena when its mole fraction is up to x 3 = 0.20. This shows that [OMIM] + [BF 4 ] − could be used as a alternative entrainer in the extractive distillation for methanol (1) + dimethyl carbonate (2) system. The measured ternary vapor–liquid equilibrium data were fitted with the NRTL.

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Isobaric vapor–liquid equilibrium data for {methanol (1) + dimethyl carbonate (2) + 1-octyl-3-methylimidazolium (3)} where 3 is an ionic liquid ([OMIM] + [BF 4 ] − ) were obtained at 101.32 kPa using a modified Othmer still. The results indicated that [OMIM] + [BF 4 ] − can transfer the azeotropic point and totally eliminate the azeotropic phenomena when its mole fraction is up to x 3 = 0.20. This shows that [OMIM] + [BF 4 ] − could be used as a alternative entrainer in the extractive distillation for methanol (1) + dimethyl carbonate (2) system. The measured ternary vapor–liquid equilibrium data were fitted with the NRTL.

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Available abstract

Isobaric vapor–liquid equilibrium data for {methanol (1) + dimethyl carbonate (2) + 1-octyl-3-methylimidazolium (3)} where 3 is an ionic liquid ([OMIM] + [BF 4 ] − ) were obtained at 101.32 kPa using a modified Othmer still. The results indicated that [OMIM] + [BF 4 ] − can transfer the azeotropic point and totally eliminate the azeotropic phenomena when its mole fraction is up to x 3 = 0.20. This shows that [OMIM] + [BF 4 ] − could be used as a alternative entrainer in the extractive distillation for methanol (1) + dimethyl carbonate (2) system. The measured ternary vapor–liquid equilibrium data were fitted with the NRTL.

Key concepts: Chemistry, Non-random two-liquid model, Ionic liquid, Dimethyl carbonate, Isobaric process, Tetrafluoroborate, Vapor–liquid equilibrium, Mole fraction

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