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
Abstract
Qunsheng Li, Wei Zhu, Yongquan Fu, Haichuan Wang, Lun Li, Baohua Wang
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.
Key concepts: Chemistry, Non-random two-liquid model, Ionic liquid, Dimethyl carbonate, Isobaric process, Tetrafluoroborate, Vapor–liquid equilibrium, Mole fraction