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A kind of preparation method of bisfluorosulfonimide lithium salt

A technology of bisfluorosulfonimide lithium salt and bisfluorosulfonimide is applied in the field of preparation of bisfluorosulfonimide lithium salt, which can solve the problem that it is not suitable for industrial production, affects practical application, and is not easy for LiF and LiFSI. separation, etc.

Active Publication Date: 2018-07-27
SHANGHAI CHEMSPEC CORP +1
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Problems solved by technology

However, the product is easily decomposed when heated in the presence of water or under high temperature conditions, and other metal ions introduced in the conventional production process will also adversely affect its performance
In order to meet the requirements for the use of electrolytes, LiFSI has strict restrictions on indicators such as moisture, metal ions, and free acids. However, there is currently no effective purification method. Once impurities are introduced, it is difficult to achieve the above requirements through purification. The production process avoids the introduction of water, acid and other metal ions to control product quality
[0004] Most of the synthesis methods of LiFSI are to synthesize bischlorosulfonimide (HClSI for short), and then react with MFn (M is Group 11-15, elements of period 4-6) to prepare the corresponding metal or organic base The salt intermediate of bisfluorosulfonimide, and then with LiOH or Li 2 CO 3 Carry out cation exchange reaction to make LiFSI, such as patents US2013331609, US2012041233, EP2415757, US2011034716, the shortcoming of these methods is that it is difficult to continue after the exchange reaction reaches a balance, so that the reaction is incomplete and the conversion rate is low; and the unreacted The intermediate MSFI (M refers to metal cation, organic base cation) has similar properties to LiSFI, and it is difficult to completely separate it, resulting in the low quality of LiFSI, which cannot be directly applied to battery electrolytes
[0005] When U.S. Patent US2004097757 uses HClSI to directly react with LiF to prepare LiFSI, a large amount of corrosive tail gas HF will be produced. The free acid HF remaining in the product will be detrimental to the performance of LiFSI, and tail gas absorption will also increase the difficulty of industrial operation; at the same time, excessive LiF and LiFSI are not easy to separate, resulting in low purity of the final product LiFSI
[0006] Although it has also been reported that with purified potassium bisfluorosulfonimide (KFSI) and LiClO 4 LiFSI is prepared by metal exchange, but the potassium ions in the product are often high, which is difficult to remove by conventional purification methods, which affects its practical application, and LiClO 4 and the resulting KClO 4 , there is a certain risk of explosion (Electrochimical Acta, 2012, 66, PP.320-324, Polyhedron, 2006, 25, PP. 1292-1298, CN101747242, CN101747243, CN101654229)
In addition, since LiClO 4 Generally, a slight excess is required to participate in the reaction, but due to its strong hygroscopicity, the final product contains a small amount of LiClO 4 Cannot be removed, so that the purity of the final product LiFSI cannot be guaranteed
[0007] US8377406 discloses the method that bisfluorosulfonimide (HFSI) directly reacts with Lithium Carbonate to prepare LiFSI in aqueous solution, but this method also has obvious deficiencies, when HFSI is dissolved in water, it exothermic violently, thereby causes the decomposition of HFSI; The patent adopts the method of preparing HFSI aqueous solution at ultra-low temperature (-78°C) to solve the technical problem of violent heat release when HFSI is dissolved in water, but this method increases a lot of energy consumption, and more importantly, LiFSI has very good water solubility property, and it is easy to decompose when heated in the water system, and the extraction efficiency is very low, so it is not suitable for industrial production
[0008] The production process of LiFSI mentioned above has high requirements on reaction equipment, difficult operation, and the problem that LiFSI is in contact with water, free acid, and other metal ions, which makes LiFSI unable to realize industrial application.

Method used

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  • A kind of preparation method of bisfluorosulfonimide lithium salt
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  • A kind of preparation method of bisfluorosulfonimide lithium salt

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preparation example Construction

[0051] One aspect of the present invention provides a method for preparing lithium salt of bisfluorosulfonyl imide. The method for preparing lithium salt of bisfluorosulfonyl imide may include: reacting chlorosulfonic acid and chlorosulfonyl isocyanate in the presence of a catalyst Obtain two chlorosulfonimides (HClSI), and the specific reaction equation is as follows:

[0052]

[0053] In the above reaction process, the catalyst may be an acid, more specifically, the catalyst may be a protonic acid and / or a Lewis acid. The Lewis acid is usually based on the Lewis acid-base theory, and generally refers to a substance that can accept electron pairs. Examples of specific Lewis acids that can be used include but are not limited to NiCl 2 , FeCl 2 , FeCl 3 、CoCl 3 , ZnCl 2 , MnCl 2 The combination of one or more of them; the protonic acid is usually based on the Bronster-Lowry acid-base theory, usually refers to the proton (hydrogen ion, H + ) molecules or ions, examples ...

Embodiment 1

[0084] Preparation of bischlorosulfonimide:

[0085] In the 1000mL reaction flask, add 478.6g of chlorosulfonic acid, NiCl 2 2.1g, start stirring, raise the temperature to 105-115°C, and add 679.2g of chlorosulfonyl isocyanate dropwise. After the dropwise addition, gradually raise the temperature to 130-140°C, and continue stirring for 20 hours. Distilled under reduced pressure, 738 g of stable fractions were collected, with a yield of 83.9%. The product is a white solid with a melting point of about 36°C.

Embodiment 2

[0087] Preparation of bisfluorosulfonimide:

[0088] In the 1000mL tetrafluoro reaction bottle, add the HClSI 738g that embodiment 1 makes, MoCl 5 0.48g, heat up to 100-105°C, slowly introduce about 130g of HF gas under stirring, cool down to room temperature after 12 hours of reaction, and blow nitrogen for 16 hours to obtain about 612g of crude product, short-distilled to obtain 516g of product, yield 82.6%. The product is a colorless liquid with a melting point of about 17°C.

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Abstract

The invention relates to the field of chemical synthesizing, in particular to a preparation method of imidodisulfuryl fluoride lithium salt. The preparation method includes the steps of firstly, allowing chlorosulfonic acid and chlorosulfonyl isocyanate to react in the presence of catalyst to obtain dichlorosulfimide; secondly, allowing dichlorosulfimide and hydrogen fluoride to react in the presence of catalyst to obtain imidodisulfuryl fluoride; thirdly, allowing imidodisulfuryl fluoride to react with compound containing lithium to obtain the imidodisulfuryl fluoride lithium salt. The preparation method has the advantages that the chlorosulfonic acid and chlorosulfonyl isocyanate are used as the raw materials in the first-step reaction, the generation of waste gases such as SO2 and HCl is avoided, and environment protection requirements are satisfied.

Description

technical field [0001] The invention relates to the field of chemical synthesis, in particular to a preparation method of lithium bisfluorosulfonyl imide. Background technique [0002] Lithium-ion battery, because of its high working voltage, small size, light weight, high energy, no memory effect, no pollution, small self-discharge, and long cycle life, is an important type of secondary battery and is widely used in various Energy storage unit for similar electronic equipment. Lithium bisfluorosulfonyl imide, referred to as LiFSI, is an electrolyte salt used in lithium-ion secondary batteries. It is different from the widely used electrolyte salt LiPF 6 Compared with the high solubility and conductivity in the solvent, it has a wider working temperature range and better stability, and more importantly, it has a large specific energy density, which can effectively improve the discharge load characteristics at low temperatures, and To maintain the capacity retention rate af...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C01B21/086
CPCC01B21/086
Inventor 何立杨东林盛平刘俊孙元健
Owner SHANGHAI CHEMSPEC CORP
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