Method for removing water from ionic liquid alcoholic solution
A technology of ionic liquids and acidic ionic liquids, applied in chemical instruments and methods, preparation of organic compounds, catalysts of organic compounds/hydrides/coordination complexes, etc. Poor performance and other problems, to achieve the effect of reducing energy consumption and meeting operating conditions
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Embodiment 1
[0038] Take by weighing 300g ethanol, 21g water and 9g 1-methyl-3-propanesulfonic acid imidazolium bisulfate ([MPSIm][HSO 4 ]) is configured as an initial ionic liquid alcohol solution, and the pH value of the ionic liquid alcohol solution is 0.71 at this moment. Add 1.31 g of diethylamine to the prepared ionic liquid alcohol solution at 10° C. to adjust the pH of the system to 5.21. The adjusted ionic liquid alcohol solution enters the pervaporation unit, wherein the pervaporation membrane is a molecular sieve membrane. Under the operating conditions of 40° C. and permeation side pressure of 200 Pa, the dehydration was circulated in the pervaporation unit for 4 hours to obtain the ionic liquid alcohol solution after water removal. The ionic liquid alcohol solution after water removal was heated to reflux at 60° C., the temperature of the condensation column was 40° C., and the final product was obtained after 1 hour. The water content in the system measured by a Karl Fische...
Embodiment 2
[0042] Take by weighing 300g ethanol, 21g water and 9g 1-methyl-3-propanesulfonic acid imidazolium bisulfate ([MPSIm][HSO 4 ]) is configured as an initial ionic liquid alcohol solution, and the pH value of the ionic liquid alcohol solution is 0.71 at this moment. Add 3.00 g of triethylamine to the prepared ionic liquid alcohol solution at 10° C. to adjust the pH of the system to 6.72. The adjusted ionic liquid alcohol solution enters the pervaporation unit, wherein the pervaporation membrane is a molecular sieve membrane. Under the operating conditions of 40° C. and permeation side pressure of 200 Pa, the dehydration was circulated in the pervaporation unit for 4 hours to obtain the ionic liquid alcohol solution after water removal. The ionic liquid alcohol solution after water removal was heated to reflux at 65° C., the temperature of the condensation column was 40° C., and the final product was obtained after 1 hour. The water content in the system measured by a Karl Fisch...
Embodiment 3
[0044] Take by weighing 300g ethanol, 21g water and 9g 1-methyl-3-propanesulfonic acid imidazolium bisulfate ([MPSIm][HSO 4 ]) is configured as an initial ionic liquid alcohol solution, and the pH value of the ionic liquid alcohol solution is 0.71 at this moment. Add 2.87 g of dimethyl sulfoxide to the prepared ionic liquid alcohol solution at 10° C. to adjust the pH of the system to 7.89. The adjusted ionic liquid alcohol solution enters the pervaporation unit, wherein the pervaporation membrane is a molecular sieve membrane. Under the operating conditions of 40° C. and permeation side pressure of 200 Pa, the dehydration was circulated in the pervaporation unit for 4 hours to obtain the ionic liquid alcohol solution after water removal. The ionic liquid alcohol solution after water removal was heated to reflux at 60° C., the temperature of the condensation column was 40° C., and the final product was obtained after 1 hour. The water content in the system measured by a Karl ...
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