CN1712390A - Method for removing halogen anion impurity in organic electrolytic salt - Google Patents
Method for removing halogen anion impurity in organic electrolytic salt Download PDFInfo
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- CN1712390A CN1712390A CN 200510039183 CN200510039183A CN1712390A CN 1712390 A CN1712390 A CN 1712390A CN 200510039183 CN200510039183 CN 200510039183 CN 200510039183 A CN200510039183 A CN 200510039183A CN 1712390 A CN1712390 A CN 1712390A
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Abstract
Remove for impurity halogen anion in organic electrolyte salt is carried out by adding oxidant into organic electrolyte salt containing impurity halogen anion, heating, oxidizing halogen anion into halogen elementary substance, heating, evaporating and removing, heating and removing surplus oxidant. Bromine ion can reach 8ppm and be used for cell liquor of super-capacitor.
Description
Technical field
The present invention relates to the purifying process of organic electrolytic salt, refer more particularly to the method for removing halide anion in the organic electrolytic salt.
Background technology
Organic electrolytic salt is one of important source material in the organic electrolyte, and organic electrolyte is widely used in all kinds of electrochemical devices such as lithium-ion secondary cell, ultracapacitor, electrolyzer etc.Because organic electrolyte is usually operated under the higher voltage, the trace impurity in the electrolytic solution often has significant effects to the performance and the life-span of associated electrical chemical device.Therefore, preparing high-purity organic electrolyte, is the important prerequisite that guarantees such as electrolyte quality that uses in the electrochemical devices such as ultracapacitor and performance.
Summary of the invention
The present invention provides a kind of method of removing impurity halide anion in the organic electrolytic salt specially.
The technical solution used in the present invention is: the method for impurity halide anion in the described removal organic electrolytic salt, be characterized in: in the organic electrolytic salt that contains the impurity halide anion, the adding oxygenant also heats, utilize oxygenizement that halide anion is oxidized to halogen simple substance, then along with heating evaporation is removed; Excess oxidant further can be removed after the heating.
The further technical scheme of the present invention is: described halide anion comprises chlorion, bromide anion and iodide ion.Further technical scheme is: described halide anion is a bromide anion.
Another further technical scheme of the present invention is: described oxygenant, the standard potential of the redox reaction that it is corresponding are oxidized to the high 0.1～1.0V of standard potential of simple substance than the halide anion that need remove; And oxygenant itself and be reduced later resultant is volatilizable liquid or gas or sublimable solid.Because volatile of itself and the volatile that is reduced after product use this oxygenant can not bring new impurity component into, can effectively reduce the concentration of foreign ion.Wherein qualified oxygenant can be selected hydrogen peroxide, ozone, nitrogen peroxide, nitrogen tetroxide, three oxidations, three nitrogen, nitrous acid, nitric acid, dioxide peroxide (ClO2), hypochlorous acid etc.More preferably hydrogen peroxide wherein.
Need to consider the scale resistance of organic electrolytic salt among the present invention, if the oxygenant and the electrolytic salt that add can produce reaction, then answer the more weak oxygenant of selective oxidation, therefore, the standard potential of the reduction reaction that selected oxygenant takes place in oxidation halogen impurities ionic process, should be oxidized to the high 0.1～1.0V of standard potential of simple substance than this halide-ions, have spontaneity and thoroughness to guarantee oxidising process.But should consider that oxygenant may be to the structure generation effects such as alkyl in the electrolytic salt, oxidisability is not to be high more good more.Under some occasion, can consider the oxygenant that working concentration is lower, perhaps add inert gasses or inert solvent dilutes oxygenant, to reduce its oxidisability.
Wish among the present invention that halide-ions is oxidized to simple substance form and is removed, therefore, the reaction conditions when carrying out removal of impurity ion should guarantee that the elemental halogen that generates disproportionation reaction can not take place or further is oxidized to higher valence state.Usually, halogen simple substance is easy disproportionation in the environment of alkalescence, the suitable weak acid environment of the suitable selection of reaction conditions.
The present invention further technical scheme is: the quality of used hydrogen peroxide than concentration range is: 10%～50%.And the adding quality of aqueous hydrogen peroxide solution can be 10%～500% of solid electrolyte salt weight; Wherein can be more preferably 50%～200%.
The advantage of this programme is: employed oxygenant---have certain acidity as superoxol itself, with halogen-containing negatively charged ion---when mixing as the ionogen of bromine, acidity helps the oxidation of bromide anion, and can avoid the disproportionation reaction of the bromine simple substance that oxidation generates under the alkaline condition.Use hydrogen peroxide can not bring new impurity into, unnecessary hydrogen peroxide can make it to decompose and remove easily by heating.Through the organic electrolytic salt that method of the present invention was handled, bromide anion wherein can reach about 8ppm, can satisfy the requirement of products such as ultracapacitor.In addition, in treating processes, it is few more good more that add-on is fully soaked under solid and the bromine oxide ionic prerequisite in assurance, is convenient to save dry energy needed.But very few hydrogen peroxide can not fully contact with solid interior, can influence the effect of removal of impurities.
Embodiment
The invention will be further described below by specific embodiment.But the present invention is not limited to this embodiment.Selecting the organic electrolytic salt tetraethyl-ammonium tetrafluoroborate (TEATFB, tetraethylammonium tetrafluoroborate) of impure bromide anion in the present embodiment for use is example, and it is example that oxygenant is selected hydrogen peroxide for use.
Embodiment 1
Get 9.0g TEATFB crude product (purity 98.9%), the analysis bromine content is 43ppm, adds 17.0g hydrogen peroxide (concentration 30%), stirs half an hour at 50 ℃.Heating evaporation under the normal pressure then, solid under 120 degree dry 24 hours, recording bromine content was 8.2ppm behind the evaporate to dryness, purity 99.5% reaches the requirement of ultracapacitor electrolysis matter salt.
Claims (9)
1, removes the method for impurity halide anion in the organic electrolytic salt, it is characterized in that: in the organic electrolytic salt that contains the impurity halide anion, the adding oxygenant also heats, and utilizes oxygenizement that halide anion is oxidized to halogen simple substance, then along with heating evaporation is removed; Excess oxidant further can be removed after the heating.
2, the method for impurity halide anion in the removal organic electrolytic salt as claimed in claim 1, it is characterized in that: described halide anion comprises chlorion, bromide anion and iodide ion.
3, the method for impurity halide anion in the removal organic electrolytic salt as claimed in claim 2, it is characterized in that: described halide anion is a bromide anion.
4, the method for impurity halide anion in the removal organic electrolytic salt as claimed in claim 1, it is characterized in that: described oxygenant is: the standard potential of the redox reaction that it is corresponding is oxidized to the high 0.1～1.0V of standard potential of simple substance than the halide anion that need remove; And oxygenant itself and be reduced later resultant is volatilizable liquid or gas or sublimable solid.
5, the method for impurity halide anion in the removal organic electrolytic salt as claimed in claim 4, it is characterized in that: described oxygenant can be selected: hydrogen peroxide, ozone, nitrogen peroxide, nitrogen tetroxide, three oxidations, three nitrogen, nitrous acid, nitric acid, dioxide peroxide (ClO
2), hypochlorous acid.
6, the method for impurity halide anion in the removal organic electrolytic salt as claimed in claim 5, it is characterized in that: described oxygenant is a hydrogen peroxide.
7, the method for impurity halide anion in the removal organic electrolytic salt as claimed in claim 6, it is characterized in that: the quality of used hydrogen peroxide than concentration range is: 10%～50%.
8, as the method for impurity halide anion in claim 6 or the 7 described removal organic electrolytic salts, it is characterized in that: the adding quality of aqueous hydrogen peroxide solution is 10%～500% of an organic electrolytic salt weight.
9, the method for impurity halide anion in the removal organic electrolytic salt as claimed in claim 8, it is characterized in that: the adding quality of aqueous hydrogen peroxide solution is 50%～200% of an organic electrolytic salt weight.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2005100391839A CN1321952C (en) | 2005-04-30 | 2005-04-30 | Method for removing halogen anion impurity in organic electrolytic salt |
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|---|---|---|---|
| CNB2005100391839A CN1321952C (en) | 2005-04-30 | 2005-04-30 | Method for removing halogen anion impurity in organic electrolytic salt |
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| CN1712390A true CN1712390A (en) | 2005-12-28 |
| CN1321952C CN1321952C (en) | 2007-06-20 |
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| CNB2005100391839A Active CN1321952C (en) | 2005-04-30 | 2005-04-30 | Method for removing halogen anion impurity in organic electrolytic salt |
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| JP3159411B2 (en) * | 1992-12-21 | 2001-04-23 | 株式会社トクヤマ | Purification method of fluorinated inert liquid |
| EP1005881B1 (en) * | 1998-11-30 | 2005-01-19 | Canon Kabushiki Kaisha | Method and apparatus for decomposing halogenated aliphatic hydrocarbon compounds or aromatic compounds |
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Address after: 215600 No.35 Nanhai Road, Jiangsu Yangzijiang International Chemical Industrial Park, Zhangjiagang, Suzhou, Jiangsu Province Patentee after: Zhangjiagang Guotai-Huarong New Chemical Materials Co.,Ltd. Address before: 215631 Jiangsu province Zhangjiagang City gold town after Cheng Cheng Road No. 112 Patentee before: Zhangjiagang Guotai-Huarong New Chemical Materials Co.,Ltd. |