CN109422252A - A kind of preparation method of fluorine sulphonyl difluoro phosphorimide lithium and products thereof and application - Google Patents

A kind of preparation method of fluorine sulphonyl difluoro phosphorimide lithium and products thereof and application Download PDF

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CN109422252A
CN109422252A CN201710723213.0A CN201710723213A CN109422252A CN 109422252 A CN109422252 A CN 109422252A CN 201710723213 A CN201710723213 A CN 201710723213A CN 109422252 A CN109422252 A CN 109422252A
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lithium
difluoro
phosphorimide
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fluorine
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CN109422252B (en
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邹志群
余意
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Dongguan Dongyang Guangke Research and Development Co Ltd
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Abstract

The present invention relates to preparation methods of a kind of fluorine sulphonyl difluoro phosphorimide lithium and products thereof and application.The preparation method includes: that the sulphonyl difluoro phosphorimide alkali metal salt that reacts with hexafluorophosphoric acid alkali metal salt of trimethyl silicon substrate chlorine sulfimide obtains fluorine sulphonyl difluoro phosphorimide lithium after the fluorination of fluorine-containing lithium salts.The preparation method substitutes active stronger POCl in the prior art using more cheap raw material3Only two-step reaction obtains fluorine sulphonyl difluoro phosphorimide lithium, and whole process avoids the introducing of moisture, side reaction is less, and intermediate only need to be purified simply, and the yield of product is improved to 85% or more, product purity is improved to 99.9% or more, and lower production costs, reaction condition is mild, increases the feasibility of industrialized production.Obtained product can be applied to lithium ion battery lithium salts electrolyte, significantly improve the cycle life of battery.

Description

A kind of preparation method of fluorine sulphonyl difluoro phosphorimide lithium and products thereof and application
Technical field
The present invention relates to technical field of organic chemistry more particularly to a kind of preparation methods of fluorine sulphonyl difluoro phosphorimide lithium And products thereof and application.
Background technique
Fluorine sulphonyl difluoro phosphorimide lithium, since its conductivity is higher, structure is more stable, and to collector corrosivity compared with It is low, the cycle performance of electrolyte can be significantly improved, it is possible to be widely used in lithium ion battery electrolysis as a kind of new lithium salts In liquid, WO2016/133169A1 and WO2016/088766A1 disclose fluorine-containing sulphonyl phosphoric acid imine lithium answering in the electrolytic solution With, and the report in the prior art about the preparation method of fluorine sulphonyl difluoro phosphorimide lithium is less, needs to develop more economical Preparation method.
Zhou Zhibin et al. discloses sulphonyl containing chlorine/phosphorimide alkali metal salt preparation side in patent CN102617414B Method: it first reacts to obtain perfluorinated alkyl sulfonamide under buffer effect with azanol oxygen sulfonic acid using perfluoroalkyl fluorine sulfinate Salt, by the perfluorinated alkyl sulfonamide salt of purification and [(CH3)3Si]2NH reaction generates trimethyl silicon substrate per-fluoroalkyl sulfonyl imines, Again with POCl3Reaction obtains (dichlor-phosphoryl) (per-fluoroalkyl sulfonyl) inferior amine salt, and last perfluorinated dose of fluorination obtains (difluoro phosphorus Acyl) (per-fluoroalkyl sulfonyl) inferior amine salt, synthetic route is as follows:
This method step is more, and not only multistep reaction causes gross production rate lower, but also intermediate purification is cumbersome, introducing Moisture is affected to product quality, and cost is also higher, is not suitable for industrialized production.
Still without step, less, cost is lower at present and product yield and purity higher to prepare fluorine sulphonyl difluoro phosphinylidyne sub- The method of amine lithium is suitable for industrialized production.
Summary of the invention
In view of preparing in the prior art, fluorine sulphonyl difluoro phosphorimide lithium step is more, complicated for operation, product yield and pure The problems such as not high is spent, one of the objects of the present invention is to provide a kind of better simply fluorine sulphonyl difluoro phosphorimide lithium preparation sides Method, it is not only easy to operate, and also yield and purity are higher, are suitable for industrialized production.
For this purpose, the present invention adopts the following technical scheme:
In a first aspect, the present invention provides a kind of preparation method of fluorine sulphonyl difluoro phosphorimide lithium, the preparation method It include: the chlorine sulphonyl difluoro phosphorimide alkali metal that trimethyl silicon substrate chlorine sulfimide is reacted with hexafluorophosphoric acid alkali metal salt Salt obtains fluorine sulphonyl difluoro phosphorimide lithium after the fluorination of fluorine-containing lithium salts.
" comprising " of the present invention, it is intended that it can also include other steps, these other techniques in addition to the step Step assigns the preparation method different paths, and it is directly trimethyl silicon substrate chlorine sulfimide that the present invention, which contains raw material not, Method obtains intermediate product trimethyl silicon substrate chlorine sulfimide in other methods of any raw material Jing Guo any prior art and goes forward side by side The chlorine sulphonyl difluoro phosphorimide alkali metal salt that one step is reacted with hexafluorophosphoric acid alkali metal salt obtains after the fluorination of fluorine-containing lithium salts Method to fluorine sulphonyl difluoro phosphorimide lithium belongs to protection category of the invention, that is to say, that it can be intermediate product, Specific preparation method can be any method in the prior art.In addition to this, " comprising " of the present invention can also replace For enclosed " for ".
Preferably, the preparation method includes the following steps:
(1) under inert environments, hexamethyldisiloxane is added to the non-proton pole of sulfamic acid chloride and/or aminosulfonyl fluorine Property solvent in, heating carry out first time back flow reaction after, be added hexafluorophosphoric acid alkali metal salt organic solution, carry out second time Stream reaction, removes solvent and by-product, obtains sulphonyl difluoro phosphorimide alkali metal salt;
(2) sulphonyl difluoro phosphorimide alkali metal salt obtained by step (1) is dissolved in aprotic polar solvent, inertia ring Under border, fluorine-containing lithium salts is added, after fluorination, isolated fluorine sulphonyl difluoro phosphorimide lithium.
Preferably, step (1) aprotic polar solvent and step (2) described aprotic polar solvent be each independently In acetonitrile, dimethyl carbonate, diethyl carbonate, acetone, 1,4- dioxane, N,N-dimethylformamide and nitromethane Any one or at least two combination;
Preferably, step (1) inert environments and step (2) described inert environments include by indifferent gas each independently Body protection environment, the inert gas in nitrogen, helium and argon gas any one or at least two combination.
Preferably, step (1) the hexafluorophosphoric acid alkali metal salt is lithium hexafluoro phosphate, Potassium Hexafluorophosphate and sodium hexafluoro phosphate In any one or at least two combination.
Preferably, the solvent in the organic solution of step (1) the hexafluorophosphoric acid alkali metal salt is selected from acetonitrile, carbonic acid diformazan In ester, diethyl carbonate, acetone, 1,4- dioxane, N,N-dimethylformamide and nitromethane any one or at least Two kinds of combination.
Sulfamic acid chloride and/or aminosulfonyl fluorine in step (1): hexamethyldisiloxane: hexafluorophosphoric acid alkali metal salt Molar ratio is 1:(3~4): (1~1.5), such as 1:3:1,1:4:1.5,1:3.5:1,1:3.2:3.5 or 1:3.8:1.2 etc. are excellent Select 1:(3~3.5): (1~1.2).
Preferably, the temperature of step (1) the first time back flow reaction be 50~100 DEG C, such as 50 DEG C, 55 DEG C, 60 DEG C, 65 DEG C, 70 DEG C, 75 DEG C, 80 DEG C, 85 DEG C, 90 DEG C, 95 DEG C or 100 DEG C etc., the time be 1~6h, such as 1h, 1.5h, 2h, 2.5h, 3h, 3.5h, 4h, 4.5h, 5h, 5.5h or 6h etc..
Preferably, the temperature of step (1) the first time back flow reaction is 50~80 DEG C, and the time is 2~4h.
Preferably, the temperature of step (1) second of back flow reaction be 50~100 DEG C, such as 50 DEG C, 55 DEG C, 60 DEG C, 65 DEG C, 70 DEG C, 75 DEG C, 80 DEG C, 85 DEG C, 90 DEG C, 95 DEG C or 100 DEG C etc., the time be 6~20h, such as 6h, 7h, 8h, 9h, 10h, 11h, 12h, 15h, 18h, 19h or 20h etc..
Preferably, the temperature of step (1) second of back flow reaction is 50~80 DEG C, and the time is 8~12h.
Preferably, step (1) solvent and the mode of by-product of removing includes distillation, preferably includes to rotate.
Preferably, the fluorine-containing lithium salts includes LiF.
Preferably, step (2) separation includes: to remove solvent after being filtered to remove insoluble matter.
Preferably, the mode for removing solvent includes: that CH is added after filtrate is concentrated2Cl2, stirring precipitates crystal, then incites somebody to action Gained crystal is dried in vacuo.
Preferably, further include purification step after step (2) described separation: gained crude product being dissolved in ethyl acetate and is carried out Recrystallization, vacuum drying obtain fluorine sulphonyl difluoro phosphorimide lithium.
Second aspect, the present invention provides the fluorine sulphonyl difluoro phosphorimides of the preparation of preparation method as described in relation to the first aspect Lithium.
The third aspect, the present invention provides as described in second aspect fluorine sulphonyl difluoro phosphorimide lithium storage lithium electrolyte in Application.
Compared with prior art, the present invention at least has the following beneficial effects:
(1) preparation method substitutes active stronger POCl in the prior art using more cheap raw material3, only two steps are anti- Fluorine sulphonyl difluoro phosphorimide lithium should be obtained, and whole process avoids the introducing of moisture, side reaction is less, and intermediate only needs simply Purification improves the yield of product to 85% or more, and product purity is improved to 99.9% or more, and lower production costs;
(2) the preparation method reaction condition is mild, increases the feasibility of industrialized production.Obtained product can be applied In lithium ion battery lithium salts electrolyte, the cycle life of battery is significantly improved.
Detailed description of the invention
Fig. 1 is the route map of preparation method in the embodiment of the present invention
Specific embodiment
To further illustrate the technical scheme of the present invention below with reference to the accompanying drawings and specific embodiments.But following reality Example is only simple example of the invention, does not represent or limit the scope of the present invention, protection scope of the present invention It is subject to claims.
Embodiment 1
Into 500mL three-necked flask, 57.8g (0.5mol) sulfamic acid chloride, 150mL acetonitrile, 243.6g is added (1.5mol) hexamethyldisiloxane, nitrogen protection after being warming up to 85 DEG C of back flow reaction 2h, will be dissolved with 100mL acetonitrile in advance 76.0g (0.5mol) lithium hexafluoro phosphate be added drop-wise in reaction system, continue back flow reaction 6h.Stopping reaction back spin is evaporated off molten Agent and by-product obtain chlorine sulphonyl difluoro phosphorimide lithium intermediate crude product.It will be in above-mentioned chlorine sulphonyl difluoro phosphorimide lithium Mesosome crude product is dissolved in 200mL acetonitrile, and under nitrogen protection, 13.0g (0.5mol) lithium fluoride is added, and reaction 12h is stirred at room temperature. It is filtered to remove insoluble matter, CH is added in filtrate concentration2Cl2Stirring precipitates crystal, re-crystallizing in ethyl acetate, and vacuum drying obtains purity 99.9% fluorine sulphonyl difluoro phosphorimide lithium 85.9g, yield 90.9%.19F-NMR (600MHz, DMSO-D6): δ=53.2~ 53.3 (s, 1F), -78.1~-78.0 (s, 1F), -80.6~-80.5 (s, 1F);LC-MS:Neg:M/Z=181.9.
Electrolyte quota:
In glove box of the moisture less than 10ppm, by organic solvent according to ethylene carbonate (EC) 30%, methyl ethyl carbonate (EMC) 30%, dimethyl carbonate (DMC) 30%, fluorinated ethylene carbonate (FEC) 5% mass fraction be uniformly mixed, electricity is added Solution matter lithium salts LiPF6 is made into the solution of 1mol/L, adds 2% 1,3-propane sultone (PS) and the fluorine of 3% above-mentioned preparation Sulphonyl difluoro phosphorimide lithium, and be thoroughly mixed uniformly, electrolyte is made.
The composition (being in terms of 100% by positive electrode mass fraction) of the positive electrode of lithium ion battery: 90% ternary material Expect LiNi0.5Co0.2Mn0.3O2, 5% conductive black, 5% Kynoar (PVDF).
The composition (being in terms of 100% by negative electrode material mass fraction) of the negative electrode material of lithium ion battery: 89% graphite, 5% conductive black, 6% Kynoar (PVDF).
The preparation method of battery:
Anode preparation: each raw material is weighed according to above-mentioned anode formula, is dispersed in n-methyl-2-pyrrolidone (NMP) In solution, it is prepared into the mixed slurry of anode, and slurry is coated on positive current collector body aluminium foil, after dry roll-in Obtain anode pole piece.
Cathode preparation: each raw material is weighed according to above-mentioned cathode formula, is dispersed in n-methyl-2-pyrrolidone (NMP) In solution, it is prepared into the mixed slurry of cathode, and slurry is coated in cathodal current current collector aluminum foil, after dry roll-in Obtain cathode pole piece.
By the positive plate of the lithium ion battery of above-mentioned preparation, negative electrode tab and electrolyte and other necessary battery components, Such as PTFE diaphragm and shell etc., 18650 type lithium ions are obtained by winding, filling the processes such as shell, fluid injection, pre- punching, chemical conversion, partial volume Battery.The lithium ion battery of embodiment 1 is made.
Under the conditions of 55 DEG C, 200 are carried out using Land CT2001A battery test system to assembled lithium ion battery Secondary 2.75V~4.2V, 0.2C cyclic charging and discharging test, obtain the discharge capacitance of cycle charge-discharge, such as table 1.
Embodiment 2
Into 500mL three-necked flask, 57.8g (0.5mol) sulfamic acid chloride, 150mL dimethyl carbonate, 284.2g is added (1.75mol) hexamethyldisiloxane, nitrogen protection after being warming up to 90 DEG C of back flow reaction 3h, will use 100mL carbonic acid diformazan in advance 83.6g (0.55mol) lithium hexafluoro phosphate of ester dissolution is added drop-wise in reaction system, continues back flow reaction 8h.Stop reaction back spin Solvent and by-product is evaporated off, obtains chlorine sulphonyl difluoro phosphorimide lithium intermediate crude product.
Above-mentioned chlorine sulphonyl difluoro phosphorimide lithium intermediate crude product is dissolved in 200mL dimethyl carbonate, nitrogen protection Under, 15.6g (0.6mol) lithium fluoride is added, reaction 12h is stirred at room temperature.It is filtered to remove insoluble matter, CH is added in filtrate concentration2Cl2 Stirring precipitates crystal, re-crystallizing in ethyl acetate, and vacuum drying obtains the fluorine sulphonyl difluoro phosphorimide lithium of purity 99.9% 84.8g, yield 89.6%.19F-NMR (600MHz, DMSO-D6): δ=53.2~53.3 (s, 1F), -78.1~-78.0 (s, 1F), -80.6~-80.5 (s, 1F);LC-MS:Neg:M/Z=181.9.
Electrolyte quota is with embodiment 1, and battery preparation method is in addition to by active substances in cathode materials LiNi0.5Co0.2Mn0.3O2Replace with LiNi1/3Co1/3Mn1/3O2Outside, other same as Example 1, obtain 200 cycle charge-discharges Discharge capacitance, such as table 1.
Embodiment 3
Into 500mL three-necked flask, 57.8g (0.5mol) sulfamic acid chloride, 150mL diethyl carbonate, 243.6g is added (1.5mol) hexamethyldisiloxane, nitrogen protection will be molten with 100mL diethyl carbonate in advance after being warming up to 90 DEG C of reaction 3h 83.6g (0.55mol) Potassium Hexafluorophosphate of solution is added drop-wise in reaction system, continues back flow reaction 8h.Stop reaction back spin to be evaporated off Solvent and by-product are removed, chlorine sulphonyl difluoro phosphorimide potassium intermediate crude product is obtained.
Above-mentioned chlorine sulphonyl difluoro phosphorimide potassium intermediate crude product is dissolved in 200mL diethyl carbonate, nitrogen protection Under, 14.3g (0.55mol) lithium fluoride is added, reaction 12h is stirred at room temperature.It is filtered to remove insoluble matter, CH is added in filtrate concentration2Cl2 Stirring precipitates crystal, re-crystallizing in ethyl acetate, and vacuum drying obtains the fluorine sulphonyl difluoro phosphorimide lithium of purity 99.9% 81.6g, yield 86.3%.19F-NMR (600MHz, DMSO-D6): δ=53.2~53.3 (s, 1F), -78.1~-78.0 (s, 1F), -80.6~-80.5 (s, 1F);LC-MS:Neg:M/Z=181.9.
Electrolyte quota is with embodiment 1, and battery preparation method is in addition to by active substances in cathode materials LiNi0.5Co0.2Mn0.3O2Replace with LiCoO2Outside, other same as Example 1, obtain the discharge capacity of 200 cycle charge-discharges Conservation rate, such as table 1.
Embodiment 4
Into 500mL three-necked flask, addition 57.8g (0.5mol) sulfamic acid chloride, 150mL1,4- dioxane, 263.9g (1.63mol) hexamethyldisiloxane, nitrogen protection will use 100mL1,4- bis- after being warming up to 90 DEG C of reaction 4h in advance 100.8g (0.6mol) sodium hexafluoro phosphate of six ring of oxygen dissolution is added drop-wise in reaction system, continues back flow reaction 10h.Stop reaction Solvent and by-product is evaporated off in back spin, obtains chlorine sulphonyl difluoro phosphorimide sodium intermediate crude product.
Above-mentioned chlorine sulphonyl difluoro phosphorimide sodium intermediate crude product is dissolved in 200mL Isosorbide-5-Nitrae-dioxane, nitrogen is protected Under shield, 15.6g (0.6mol) lithium fluoride is added, reaction 12h is stirred at room temperature.It is filtered to remove insoluble matter, filtrate concentration is added CH2Cl2Stirring precipitates crystal, re-crystallizing in ethyl acetate, and vacuum drying obtains the fluorine sulphonyl difluoro phosphorimide lithium of purity 99.9% 83.7g, yield 88.6%.19F-NMR (600MHz, DMSO-D6): δ=53.2~53.3 (s, 1F), -78.1~-78.0 (s, 1F), -80.6~-80.5 (s, 1F);LC-MS:Neg:M/Z=181.9.
Electrolyte quota is with embodiment 1, and battery preparation method is in addition to by active substances in cathode materials LiNi0.5Co0.2Mn0.3 O2Replace with LiFePO4Outside, other same as Example 1, the discharge capacitance of 200 cycle charge-discharges is obtained, such as table 1.
Comparative example 1
CN102617414B embodiment 20.The purity 99.5% of product, yield 83%.19F-NMR (600MHz, DMSO- D6): δ=53.2~53.3 (s, 1F), -78.1~-78.0 (s, 1F), -80.6~-80.5 (s, 1F);LC-MS:Neg:M/Z= 181.9。
Electrolyte quota is with embodiment 1, and active substances in cathode materials can be LiNi in battery preparation method0.5Co0.2Mn0. 3O2、LiNi1/3Co1/3Mn1/3O2、LiCoO2、LiFePO4, it is other same as Example 1, obtain the electric discharge of 200 cycle charge-discharges Capacity retention ratio, such as table 1.
Table 1
The products collection efficiency and purity of comparative examples 1~4 and comparative example 1 are it is found that preparation method of the present invention passes through with replacement Raw material simultaneously designs synthetic route, is not only better than the prior art, but also the production of product on cost, operability and technique simplification degree Rate and purity have significant progress compared with the prior art.As shown in Table 1, the difference of Examples 1 to 4 and comparative example 1 is to prepare Method is different, when electrolyte of the Examples 1 to 4 product as lithium ion battery, under the same conditions, shows compared to comparison The more preferably cycle performance of example 1, illustrates that the obtained fluorine sulphonyl difluoro phosphorimide lithium product of preparation method of the present invention can be applied to Lithium ion battery lithium salts electrolyte, significantly improves the cycle life of battery.
The Applicant declares that the present invention is explained by the above embodiments detailed process equipment and process flow of the invention, But the present invention is not limited to the above detailed process equipment and process flow, that is, it is above-mentioned detailed not mean that the present invention must rely on Process equipment and process flow could be implemented.It should be clear to those skilled in the art, any improvement in the present invention, Addition, selection of concrete mode of equivalence replacement and auxiliary element to each raw material of product of the present invention etc., all fall within of the invention Within protection scope and the open scope.

Claims (10)

1. a kind of preparation method of fluorine sulphonyl difluoro phosphorimide lithium, which is characterized in that the preparation method includes: trimethyl silicane The sulphonyl difluoro phosphorimide alkali metal salt that base sulfimide is reacted with hexafluorophosphoric acid alkali metal salt is fluorinated through fluorine-containing lithium salts After obtain fluorine sulphonyl difluoro phosphorimide lithium.
2. preparation method as described in claim 1, which is characterized in that the preparation method includes the following steps:
(1) under inert environments, the aprotonic polar that sulfamic acid chloride and/or aminosulfonyl fluorine is added in hexamethyldisiloxane is molten In agent, after heating carries out first time back flow reaction, the organic solution of hexafluorophosphoric acid alkali metal salt is added, flow back for the second time anti- It answers, removes solvent and by-product, obtain sulphonyl difluoro phosphorimide alkali metal salt;
(2) sulphonyl difluoro phosphorimide alkali metal salt obtained by step (1) is dissolved in aprotic polar solvent, inert environments Under, fluorine-containing lithium salts is added, after fluorination, isolated fluorine sulphonyl difluoro phosphorimide lithium.
3. preparation method as claimed in claim 2, which is characterized in that step (1) aprotic polar solvent and step (2) The aprotic polar solvent be each independently selected from acetonitrile, dimethyl carbonate, diethyl carbonate, acetone, 1,4- dioxane, In N,N-dimethylformamide and nitromethane any one or at least two combination;
Preferably, step (1) inert environments and step (2) described inert environments include being protected by inert gas each independently The environment of shield, the inert gas in nitrogen, helium and argon gas any one or at least two combination.
4. preparation method as claimed in any one of claims 1 to 3, which is characterized in that step (1) the hexafluorophosphoric acid alkali metal Salt is the combination of any one or at least two in lithium hexafluoro phosphate, Potassium Hexafluorophosphate and sodium hexafluoro phosphate;
Preferably, the solvent in the organic solution of step (1) the hexafluorophosphoric acid alkali metal salt be selected from acetonitrile, dimethyl carbonate, Any one in diethyl carbonate, acetone, 1,4- dioxane, N,N-dimethylformamide and nitromethane or at least two Combination.
5. such as the described in any item preparation methods of claim 2~4, which is characterized in that in step (1) sulfamic acid chloride and/or Aminosulfonyl fluorine: hexamethyldisiloxane: the molar ratio of hexafluorophosphoric acid alkali metal salt is 1:(3~4): (1~1.5), preferably 1: (3~3.5): (1~1.2);
Preferably, the temperature of step (1) the first time back flow reaction is 50~100 DEG C, and the time is 1~6h;
Preferably, the temperature of step (1) the first time back flow reaction is 50~80 DEG C, and the time is 2~4h;
Preferably, the temperature of step (1) second of back flow reaction is 50~100 DEG C, and the time is 6~20h;
Preferably, the temperature of step (1) second of back flow reaction is 50~80 DEG C, and the time is 8~12h;
Preferably, step (1) solvent and the mode of by-product of removing includes distillation, preferably includes to rotate.
6. preparation method as claimed in any one of claims 1 to 5, which is characterized in that the fluorine-containing lithium salts includes LiF.
7. such as the described in any item preparation methods of claim 2~6, which is characterized in that step (2) separation includes: filtering Solvent is removed after removing insoluble matter;
Preferably, the mode for removing solvent includes: that CH is added after filtrate is concentrated2Cl2, stirring precipitates crystal, then by gained Crystal is dried in vacuo.
8. preparation method as claimed in any one of claims 2 to 7, which is characterized in that further include after step (2) described separation Purification step: being dissolved in ethyl acetate for gained crude product and recrystallize, and vacuum drying obtains fluorine sulphonyl difluoro phosphorimide lithium.
9. fluorine sulphonyl difluoro phosphorimide lithium prepared by the preparation method as described in any one of claim 1~8.
10. application of the fluorine sulphonyl difluoro phosphorimide lithium as claimed in claim 9 in storage lithium electrolyte.
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CN111710910A (en) * 2020-07-01 2020-09-25 香河昆仑化学制品有限公司 Electrolyte containing bis-tetrafluorophosphoryl imide salt and lithium ion battery
CN111786020A (en) * 2020-07-20 2020-10-16 香河昆仑化学制品有限公司 Non-aqueous electrolyte containing fluoro phosphoric acid amide salt and lithium ion battery
CN112186249A (en) * 2020-09-30 2021-01-05 香河昆仑化学制品有限公司 Electrolyte containing fluoro-malonic acid difluoro-lithium phosphate and lithium ion battery containing electrolyte
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CN113979454A (en) * 2021-11-23 2022-01-28 山东永浩新材料科技有限公司 Preparation method of fluorosulfonic acid alkali metal salt

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