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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

Active Publication Date: 2021-04-27
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Although pervaporation has been widely used in the dehydration process, and compared with traditional rectification, pervaporation can save energy by more than 30%, but for pervaporation in acidic systems (especially strong acidic systems, PH<2), it is still difficulty
[0009] As can be seen from the above analysis, there are still various difficulties in the removal of water in the ionic liquid, alcohol and water system: (1) adopting rectification method, it is difficult to apply to the low boiling point alcohol system, the energy consumption is huge and the operability is poor; (2) Adopting the adsorption method, it is easy to make the ionic liquid in the system adsorb on the adsorbent; (3) Using the pervaporation method, due to the strong acidity of the acidic ionic liquid, it is difficult to find a suitable pervaporation membrane

Method used

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  • Method for removing water from ionic liquid alcoholic solution
  • Method for removing water from ionic liquid alcoholic solution
  • Method for removing water from ionic liquid alcoholic solution

Examples

Experimental program
Comparison scheme
Effect test

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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Abstract

The invention relates to a method for removing water from an ionic liquid alcoholic solution. The method comprises the following steps: S1, adding an additive into an ionic liquid alcoholic solution for adjustment to obtain an adjusted ionic liquid alcoholic solution; S2, enabling the adjusted ionic liquid alcoholic solution to pass through a pervaporation unit to obtain a dehydrated ionic liquid alcoholic solution; and S3, heating the dehydrated ionic liquid alcoholic solution, and recovering the additive in the ionic liquid alcoholic solution. According to the method disclosed by the invention, the acidity in the system is greatly reduced by adding the additive into the acidic ionic liquid alcoholic solution, so that the system does not damage the pervaporation membrane, and the operation conditions of the conventional pervaporation membrane are met; the whole water removal process can be completed at low temperature, so that the energy consumption of the whole process is greatly reduced; and the whole process is simple and easy to be continuous, and the obtained treated final product can directly enter esterification, ester exchange and other reaction units to realize direct reuse of the ionic liquid.

Description

technical field [0001] The invention belongs to the field of water removal of ionic liquid alcohol solution, in particular to a water removal method of ionic liquid alcohol solution. Background technique [0002] Ionic liquids, also known as low-temperature molten salts, generally refer to substances that are in a liquid state at or near room temperature and are composed of organic cations and inorganic anions with large volume differences. Ionic liquids are different from ordinary molten salts in that their melting points are different. The size of the electrostatic potential between anions and cations determines the melting point. Ionic liquids cannot attract each other in an orderly manner due to the large difference in volume between anions and cations, thereby reducing the two. The electrostatic potential between them leads to its lower melting point. However, the electrostatic potential still dominates the interior of ionic liquids, making ionic liquids have almost no...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07D233/60B01J31/02C07C67/08C07C69/76
CPCC07D233/60B01J31/0285B01J31/0284C07C67/08B01J2231/49C07C69/76
Inventor 秦春曦陈亮张洪福
Owner CHINA PETROLEUM & CHEM CORP
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