Method for producing alkali sulfonylimide salts

Abstract

The present disclosure relates to a new method for producing alkali salts of bis(fluorosulfonyl)imides with high purity on an industrial scale and at reasonable cost compared to other available methods, comprising the steps of reacting bis(chlorosulfonyl)imide or a salt thereof with onium chloride to produce the onium salt of bis(chlorosulfonyl)imide, reacting the onium salt of bis(chlorosulfonyl)imide with anhydrous hydrogen fluoride in at least one organic solvent to produce the onium salt of bis(fluorosulfonyl)imide, and reacting the onium salt of bis(fluorosulfonyl)imide with an alkali salt to obtain the alkali salt of bis(fluorosulfonyl)imide.

Description

[Technical field]

[0001] CROSS-REFERENCE TO RELATED PATENT APPLICATIONS This application claims priority to European Patent Application Publication No. 21305685.6, filed in Europe on May 26, 2021, the entire contents of which are incorporated herein by reference for all purposes.

[0002] The present invention relates to a method for producing an alkali salt of a bis(fluorosulfonyl)imide. More specifically, the present invention provides a new method for producing an alkali salt of a bis(fluorosulfonyl)imide, which is economically feasible on an industrial scale and provides a product of high purity. [Background technology]

[0003] Fluorosulfonylimide salts, particularly the lithium salt of bis(fluorosulfonyl)imide (LiFSI), are compounds useful in battery electrolytes. Various processes, reactants, and intermediates leading to LiFSI have been described in the patent literature.

[0004] One of the known intermediates leading to LiFSI is ammonium bis(fluorosulfonyl)imide (NH 4 Several patent documents specifically describe the first step of fluorination of bis(chlorosulfonyl)imide (HCSI) with a fluorinating agent, followed by the subsequent NH reaction to give the LiFSI product. 4 The preparation of LiFSI by a second step of lithiation of FSI is described.

[0005] In particular, WO 2017 / 090877A1 (CLS) discloses a method for producing a fluorinated bis(chlorosulfonyl)imide (HCSI) by reacting it with a fluorinating agent in a solvent, followed by treatment with an alkaline agent to obtain a fluorinated bis(chlorosulfonyl)imide (NH 4 (2) generating FSI; and 4 and reacting FSI with a lithium base.

[0006] According to this literature, NH 4 The FSI intermediate is obtained directly by fluorination of CSIH with a fluorinating agent in a solvent, followed by treatment with an alkaline reagent to precipitate the product.

[0007] The object of the present invention is to provide a process for the preparation of onium salts of bis(fluorosulfonyl)imides (onium salts of FSI), in particular NH 4 The objective of the present invention is to provide an alternative route for the preparation of FSI, which is based on the intermediate onium salts of CSI, in particular NH 4 The high purity of CSI provides the advantage of positively impacting the purity of other intermediates and final products as well as the efficiency of the overall process.

[0008] WO 2015 / 158979A1 (Arkema) 4 Formula (III) R 2 -(SO 2 )-NX-(SO 2 (a) a compound of formula (II)R 1 -(SO 2 )-NX-(SO 2 A first step of obtaining a chloro compound of formula (I)R 0 -(SO 2 )-NH 2 with sulfurous acid and a chlorinating agent, and (b) a second step to obtain a fluoro compound of formula (III), which comprises reacting a chloro compound of formula (II) with anhydrous hydrofluoric acid HF in at least one organic solvent.

[0009] WO 2019 / 229361A1 (Arkema) also describes lithium bis(fluorosulfonyl)imide salts F-(SO 2 )-NLi-(SO 2 describes a similar process to produce sulfamic acid, HO-(SO2 )-NH 2 is reacted to give bis(chlorosulfonyl)imide Cl-(SO 2 )-NH-(SO 2 )-Cl in a first step, and optionally in at least one organic solvent SO1, by the addition of anhydrous HF to the bis(chlorosulfonyl)imide Cl-(SO 2 )-NH-(SO 2 and a second step of fluorinating -Cl, said step being carried out in a reactor made of a corrosion-resistant material M3 or in a reactor comprising a substrate made of a material M1 coated with a surface layer made of a corrosion-resistant material M2.

[0010] WO 2020 / 099527 (Solvay SA) discloses a method for producing an alkali salt of bis(fluorosulfonyl)imide, which comprises the steps of: a) reacting bis(chlorosulfonyl)imide or a salt thereof with ammonium fluoride to produce an ammonium salt of bis(fluorosulfonyl)imide; b) crystallizing by adding at least one precipitating solvent and isolating the ammonium salt of bis(fluorosulfonyl)imide; and c) reacting the crystallized ammonium salt of bis(fluorosulfonyl)imide with an alkali salt to obtain an alkali salt of bis(fluorosulfonyl)imide. Preferably, ammonium fluoride is used at the end of the process to obtain ammonium bis(fluorosulfonyl)imide. As detailed in the present description and shown in the examples, step a) is carried out in a solvent.

[0011] European Patent No. 2674395 (Nippon Soda Co., Ltd.) discloses reacting ammonium N-(chlorosulfonyl)-N-(fluorosulfonyl)imide with hydrogen fluoride to obtain ammonium N,N-di(fluorosulfonyl)imide.

[0012] European Patent Specification No. 3203570 (Nippon Shokubai Co., Ltd.) discloses a method for producing an electrolyte solution material containing a fluorosulfonylimide salt and a solvent, which is characterized by reducing pressure and / or heating a solution containing a fluorosulfonylimide salt and an electrolyte solution solvent to volatilize the fluorosulfonylimide salt-producing solvent.

[0013] The object of the present invention is to provide onium salts of bis(fluorosulfonyl)imides (FSI onium salts, in particular NH 4 The object of the present invention is to provide an alternative route for the preparation of bis(fluorosulfonyl)imide (FSI) and then alkali salts of FSI (alkali salts of FSI, especially LiFSI), which is feasible on an industrial scale and provides a high purity bis(fluorosulfonyl)imide product. In particular, the key part of the process of the present invention (i.e. step a), the first step) is carried out in the presence of a molten reaction product, such as molten HCSI, which acts to disperse the reactants, and in the absence of a solvent (or in the presence of a very limited amount of solvent). Since the intermediate onium salt of CSI is prepared in the molten state in the absence of a solvent, there is no longer any possibility of side reactions occurring between the molten reaction product (such as HCSI) and the solvent, which has a positive impact on the purity of the following products, especially the purity of the onium salt of FSI and the alkali metal salt of FSI. Moreover, such an alternative route offers the additional advantage that the reaction by-products (e.g., HCl gas) can be valorized without special separation / purification steps, in addition, the preparation process of the onium salts of CSI exhibits an endothermic thermal equilibrium (due to the significant evolution of HCl gas), making the steps and the overall process safer compared to the processes described in the prior art. Summary of the Invention

[0014] In this application: - the expression "included in..." is to be understood as including the limiting values, - any description, even if made in relation to a particular embodiment, is applicable and interchangeable with other embodiments of the invention; - when an element or component is said to be included in and / or selected from a list of enumerated elements or components, in the relevant embodiments expressly contemplated herein, it is to be understood that the element or component may be any one of the individual enumerated elements or components, or may also be selected from the group consisting of any two or more of the explicitly enumerated elements or components, and that any element or component enumerated in a list of elements or components may be omitted from such list; - Any recitation herein of numerical ranges by endpoints includes all numbers subsumed within the recited range, as well as the endpoints of the range and equivalents thereof.

[0015] The first object of the present invention is a method for producing an alkali salt of a bis(fluorosulfonyl)imide, comprising the steps of: a) reacting bis(chlorosulfonyl)imide (or a salt thereof) with onium chloride to produce an onium salt of bis(chlorosulfonyl)imide (onium salt of CSI), which is carried out in the absence of a solvent or in the presence of less than 5% by weight of a solvent based on the total weight of the reaction mixture involved in step a) in molten bis(chlorosulfonyl)imide (or a salt thereof); b) reacting the onium salt of CSI with anhydrous hydrogen fluoride in at least one organic solvent to produce the onium salt of bis(fluorosulfonyl)imide (the onium salt of FSI); c) reacting the onium salt of FSI with an alkali salt to obtain an alkali salt of bis(fluorosulfonyl)imide (alkali salt of FSI); The method includes:

[0016] The process of the present invention is advantageous in comparison with the NHF fluorination procedures described in the prior art mainly because the intermediate onium salts of CSI, particularly NH4CSI, exhibit high purity due to their preparation process in the molten state and can therefore be directly fluorinated to form the onium salts of FSI, particularly NH4FSI, without the formation of significant solid waste.

[0017] Step a) of the process according to the invention comprises reacting bis(chlorosulfonyl)imide (or its salt) with onium chloride to produce an onium salt of CSI. This step a) is carried out in the molten state in the absence of solvents and diluents. More precisely, the process is carried out in a molten salt of bis(chlorosulfonyl)imide (or its salt), e.g. molten HCSI, which acts to disperse the reactants so that the reactants involved in step a) can react in contact. Importantly, step a) of the process according to the invention is a solvent-free process. In other words, no solvent / diluent is added to the reaction mixture during the reaction of step a), but instead a very small amount of solvent / diluent is added. This is advantageous because, firstly, the step of removing the solvent not only increases the complexity of the industrial process, but also its overall cost. Secondly, only anhydrous solvents (characterized by residual water content in the ppm range) can be practically used, so that the solvents typically need to be treated before use in such processes, and in addition, the inherent reactivity of bis(chlorosulfonyl)imides (or their salts) can lead to undesired side reactions in the presence of various solvents considered in such chemical processes, which can lead to the formation of unexpected solvent by-products. Significant efforts are usually required in subsequent steps of the process to remove these impurities (among others) from the final alkali salts of bis(fluorosulfonyl)imides (alkali salts of FSI).

[0018] In the context of the present invention, the term "solvent" is intended to mean a compound that exhibits the following three cumulative properties: 1 / it is present from the beginning to the end of the reaction and is optionally added during the process; 2 / it does not change during the process, in other words it is non-reactive with the reactants involved; and 3 / it needs to be removed at the end of the process if the reaction product is in its pure form. Examples of solvents that fall within this definition are given below. For clarity, the molten bis(chlorosulfonyl)imide (or a salt thereof) used in the process of the present invention does not fall under the definition of "solvent" above.

[0019] According to one embodiment of the present invention, step a) of the method described herein is carried out in the presence of a very small amount of solvent, i.e. less than 5% by weight, based on the total weight of the reaction mixture involved in step a). Preferably, according to this embodiment, the amount of solvent is less than 4%, less than 3%, less than 2%, less than 1%, less than 0.5%, less than 0.1%, less than 0.01% or less than 0.001% by weight, based on the total weight of the reaction mixture involved in step a). The total weight of the reaction mixture is obtained by adding the weights of the reactants and the weight of the molten bis(chlorosulfonyl)imide (or salt thereof).

[0020] Solvents typically used in such processes are well known or widely described in the literature. Such solvents may be aprotic, e.g. polar aprotic solvents, cyclic and acyclic carbonates, such as ethylene carbonate, propylene carbonate, butylene carbonate, dimethyl carbonate, ethyl methyl carbonate, diethyl carbonate, cyclic and acyclic esters, such as gamma-butyrolactone, gamma-valerolactone, methyl formate, methyl acetate, methyl propionate, ethyl acetate, ethyl propionate, isopropyl acetate, propyl propionate, butyl acetate, cyclic and acyclic ethers, such as diethyl ether, diisopropyl ether, methyl tert-butyl ether, dimethoxymethane, 1,2-dimethoxyethane, tetrahydrofuran, 2-methyltetrahydrofuran, 1,3-dioxane, 4-methyl-1,3-dioxane, 1,4-dioxane, amide compounds, such as N,N-dimethylformamide, N-methyloxazolidinone, Sulfoxide and sulfone compounds, such as sulfolane, 3-methylsulfolane, dimethylsulfoxide, and - cyano, nitro, chloro or alkyl substituted alkanes or aromatic hydrocarbons, e.g. acetonitrile, valeronitrile, adiponitrile, benzonitrile, nitromethane, nitrobenzene may be selected from the group consisting of:

[0021] Typically, the organic solvent used to carry out such a process may be selected from the group consisting of ethyl acetate, isopropyl acetate, butyl acetate, ethylene carbonate, dimethyl carbonate, ethyl methyl carbonate, propylene carbonate, valeronitrile and acetonitrile, for example as in the documents listed in the background section.

[0022] According to step a), before adding the reactant (or reactive entity), a certain amount of bis(chlorosulfonyl)imide (or its salt), e.g., HCSI, is heated above its melting temperature Tm(I) so that it is in a molten state (also called liquid state). The reactant, which may be in powder or liquid form, is then added to the reaction mixture and allowed to react to form, e.g., NH 4 This means that the amount of such reaction product, i.e., bis(chlorosulfonyl)imide (or its salt), increases during step a). In other words, the molten reaction product is used to disperse the reactants and provide a medium for them to come into contact and react. Thus, according to the present invention, no solvent is required to carry out step a). This is because the amount of the corresponding onium salt of CSI, e.g., high purity NH 4 This is advantageous since it is not necessary to remove such solvents after the reaction to obtain the CSI, which greatly simplifies the overall production process, and presents the added advantage that no additional steps are required to remove the water of the solvent.

[0023] In step a), bis(chlorosulfonyl)imide (or a salt thereof) is used as a starting material, which has the formula: (Cl-SO 2 -N - -SO 2 -Cl)X + where X represents one from the group consisting of H, Li, Na, K and Cs.

[0024] According to a preferred embodiment, X represents H, which means that the starting material has the formula: Cl-SO 2 -NH-SO 2 -Cl(HCSI) This means that the compound is a bis(chlorosulfonyl)imide of the formula:

[0025] According to this preferred embodiment, step a) comprises reacting bis(chlorosulfonyl)imide (HCSI) with an onium chloride in the absence of a solvent to produce the onium salt of CSI. Even more preferably, the onium chloride used in this preferred step a) is ammonium chloride (NH 4 According to this even more preferred embodiment, step a) comprises reacting HCSI with NH 4 Cl to give the ammonium salt of bis(chlorosulfonyl)imide (NH 4 CSI). In this case, in the absence of a solvent, the reaction is such that HCl is released from the medium as an anhydrous gas, which is highly advantageous. Optionally, the use of reduced pressure can be considered to facilitate the release of HCl during the addition of the onium chloride or after the addition of the onium chloride is complete.

[0026] HCSI may be obtained from commercially available sources or may be prepared, for example, by - Chlorosulfonyl isocyanate ClSO 2 NCO, chlorosulfonic acid, ClSO 2 By reacting with OH, - Cyanogen chloride CNCl, sulfuric anhydride SO 3 and chlorosulfonic acid ClSO 2 By reacting with OH, - Sulfamic acid NH 2 SO 2 OH to thionyl chloride SOCl 2 and chlorosulfonic acid ClSO 2 By reacting with OH, It may be produced by known methods.

[0027] HCSI can be prepared either by the so-called isocyanate route or by the sulfamic acid route. In the latter case, the sulfamic acid used is optionally ground and dried under vacuum to reduce its water content and accelerate the conversion rate, which can significantly shorten the reaction time.

[0028] In some embodiments, the onium chloride used in step a), such as NH 4 The Cl has a water content of less than 2,000 ppm, less than 1,000 ppm, less than 500 ppm, less than 100 ppm, less than 50 ppm or even less than 10 ppm.

[0029] In another embodiment, step a) comprises reacting a salt of bis(chlorosulfonyl)imide (Cl-SO 2 -N - -SO 2 -Cl)X + to ammonium chloride (NH 4 Cl) to give bis(chlorosulfonyl)imide (NH 4 CSI), where X is selected from the group consisting of Li, Na, K, and Cs.

[0030] Step b) of the process according to the invention comprises reacting the onium salt of CSI of step a) with anhydrous hydrogen fluoride (HF) in at least one organic solvent to produce the onium salt of FSI.

[0031] According to the present invention, the hydrogen fluoride is anhydrous. The water content may preferably be less than 5,000 ppm, less than 1,000 ppm, less than 500 ppm, less than 100 ppm or even less than 50 ppm.

[0032] Hydrogen fluoride HF is preferably introduced into the reaction medium in gaseous form. Alternatively, it can be introduced into the reaction in liquid form.

[0033] The amount of hydrogen fluoride used in step b) is preferably comprised between 1 and 10 equivalents, more preferably between 1 and 7 equivalents, and even more preferably between 2 and 5 equivalents per mole of bis(chlorosulfonyl)imide (or a salt thereof).

[0034] Step b) is carried out in an organic solvent which may be selected from the group consisting of: cyclic and acyclic carbonates, such as ethylene carbonate, propylene carbonate, butylene carbonate, dimethyl carbonate, ethyl methyl carbonate, diethyl carbonate, cyclic and acyclic esters, such as gamma-butyrolactone, gamma-valerolactone, methyl formate, methyl acetate, methyl propionate, ethyl acetate, ethyl propionate, isopropyl acetate, propyl propionate, butyl acetate, cyclic and acyclic ethers, such as diethyl ether, diisopropyl ether, methyl tert-butyl ether, dimethoxymethane, 1,2-dimethoxyethane, tetrahydrofuran, 2-methyltetrahydrofuran, 1,3-dioxane, 4-methyl-1,3-dioxane, 1,4-dioxane, amide compounds, such as N,N-dimethylformamide, N-methyloxazolidinone, sulfoxide and sulfone compounds, such as sulfolane, 3-methylsulfolane, dimethylsulfoxide, - cyano, nitro, chloro or alkyl substituted alkanes or aromatic hydrocarbons, such as acetonitrile, valeronitrile, adiponitrile, benzonitrile, nitromethane, nitrobenzene.

[0035] According to a preferred embodiment, the organic solvent is anhydrous. The water content may preferably be less than 5,000 ppm, less than 1,000 ppm, less than 500 ppm, less than 100 ppm or even less than 50 ppm.

[0036] According to the present invention, before step b) or in step b), the onium salt of CSI can be dissolved or suspended in an organic solvent before the addition of anhydrous hydrogen fluoride.

[0037] In some embodiments, step b) is carried out at a temperature ranging between 30° C. and the boiling point of the organic solvent. For example, step b) can be carried out at a temperature between 30° C. and 100° C., preferably between 50° C. and 90° C. or between 70° C. and 80° C.

[0038] Step b) can be carried out at atmospheric pressure or under reduced pressure. In some embodiments, step b) is carried out under reduced pressure. For example, step b) can be carried out at pressures ranging from 0 to 1013 mbar or from 0 to 500 mbar, preferably from 0 to 200 mbar, more preferably from 0 to 50 mbar.

[0039] In some embodiments, step b) comprises reacting the ammonium salt of the CSI of step a) with anhydrous hydrogen fluoride in at least one organic solvent to produce the ammonium salt of the FSI.

[0040] When anhydrous HF is used as the fluorinating agent, the fluorination reaction results in the formation of HCl, most of which can be degassed (as well as the excess HF) from the reaction medium, for example by sparging with a neutral gas (such as nitrogen, helium or argon). The sparged HF / HCl mixture can be further recycled.

[0041] The concentration of the onium salt of bis(fluorosulfonyl)imide in the reaction medium after step b) may be comprised between 10% and 95% by weight, for example between 30% and 80% by weight or between 40% and 70% by weight.

[0042] After step b) but before step c), the process according to the invention may comprise a step comprising adding a basic compound to the reaction medium. This optional step corresponds to the neutralization of the partially fluorinated onium salt before lithiation. The basic compound that can be used according to this optional step may be a solid, a pure liquid, an aqueous or organic solution or a gas. The basic compound may be selected from the group consisting of gaseous ammonia, aqueous ammonia, amines, hydroxides, carbonates, phosphates, silicates, borates, formates, acetates, stearates, palmitates, propionates or oxalates of alkali or alkaline earth metals. Among the amines, aliphatic amines (such as ethylamine, propylamine, butylamine, pentylamine, hexylamine, heptylamine, octylamine, dimethylamine, diethylamine, dipropylamine, dibutylamine, 2-ethylhexylamine, trimethylamine, triethylamine, tripropylamine, and tributylamine), alkylenediamines (such as ethylenediamine, diethylenetriamine, triethylenetetramine, tetraethylenepentamine, and pentaethylenehexamine), alkanolamines (monoethanolamine, diethanolamine, triethanolamine, mono ... Any type of amine may be advantageous, including isopropanolamine, diisopropanolamine and triisopropanolamine, alicyclic amines such as cyclohexylamine and dicyclohexylamine, aromatic amines such as benzylamine and metaxylenediamine, ethylene oxide adducts of these amines, formamidines, guanidines, amidines and heterocyclic amines such as diazabicycloundecene, diazabicyclononene, piperidine, morpholine, piperazine, pyrimidine, pyrrole, imidazole, imidazoline, triazole, thiazole, pyridine and indole. The basic compound is preferably gaseous ammonia or aqueous ammonia.

[0043] The amount of basic compound added in this optional neutralization step is preferably 0.1 to 10 equivalents, preferably 0.5 to 5 equivalents, more preferably 0.5 to 3 equivalents based on the amount of onium salt to be neutralized.

[0044] During this optional neutralization step the temperature may vary from 0° C. to 100° C., from 15° C. to 60° C. or from 20° C. to 40° C. The optional neutralization step may be carried out at the same temperature as step b).

[0045] After step b) but before step c), the process according to the invention may comprise a step comprising crystallizing the onium salt of FSI.

[0046] Such an optional crystallization reaction may be carried out in the reaction medium obtained after step b). Alternatively, the method may comprise a further step comprising concentrating the onium salt of FSI in the reaction medium, typically by evaporating a portion of the organic solvent of the reaction medium, by heating, reducing pressure or both. According to one embodiment, the concentration step may comprise distillation of the solvent at a temperature comprised between 0° C. and 120° C., preferably between 5° C. and 80° C., more preferably between 10° C. and 70° C. The pressure may vary depending on the nature of the solvent, typically between atmospheric pressure and 10° C. -2 The pressure can be adjusted between 1 mbar and 500 mbar, preferably between 5 mbar and 100 mbar. The distillation can be carried out by any typical means known to the skilled person in a continuous process mode or in a discontinuous / batch mode, such as continuous batch solvent evaporation, batch distillation, short path continuous flow distillation or thin film evaporator.

[0047] The optional crystallization of the onium salt can be obtained by adding at least one precipitating solvent. At least one precipitating solvent is added to the reaction mixture containing the salt. The precipitating solvent may be preferably selected from among organic solvents which have a high solubility in the organic solvent of the reaction mixture and which are poor solvents for the onium salt of the bis(fluorosulfonyl)imide. Said precipitating solvent may be selected from the group consisting of halogenated solvents such as dichloromethane, dichloroethane, chloroform and carbon tetrachloride, substituted aromatic hydrocarbon solvents such as chlorobenzene, dichlorobenzene and toluene, and alkane solvents such as cyclohexane, hexane, heptane and Isopar™. The precipitating solvent may preferably be selected from dichloromethane and dichloroethane. The volume ratio between the precipitating solvent and the organic solvent of the reaction mixture may be comprised between 0.1 and 50, preferably between 0.2 and 20, more preferably between 0.5 and 15, even more preferably between 1 and 10. Optionally, water can be added to the reaction mixture before adding the precipitating solvent, in a content that may be between 0.01% and 20% by weight, preferably between 0.1% and 10% by weight, more preferably between 1% and 5% by weight, based on the total weight of the reaction mixture.

[0048] In addition, the temperature of the reaction mixture containing the salt may be reduced to a value comprised between the solvent boiling point and -20°C, for example between 70°C and -10°C, for example between 30°C and 0°C. It may be preferable to keep the pressure constant during the reduction of the temperature. However, a simultaneous reduction of the pressure is not excluded. This may lead to evaporation of part of the organic solvent of the reaction mixture. The pressure may be reduced to between atmospheric and 10°C. -2 It can be down to a value comprised between 1 mbar and 500 mbar, and more preferably between 5 mbar and 100 mbar.

[0049] According to one embodiment of the invention, the method comprises a step of crystallizing the onium salt before step b) in which the addition of the precipitating solvent is carried out, without lowering the temperature of the reaction mixture containing the salt. According to another embodiment, the method comprises a step of crystallizing the onium salt before step b) in which the addition of the precipitating solvent is carried out, while lowering the temperature of the reaction mixture containing the salt. The precipitating solvent is preferably added first and then the temperature is lowered. However, it is not excluded to proceed in the other way or to carry out the two actions simultaneously.

[0050] After step b), but before step c), the method according to the invention may include a separation step. This optional separation step may be carried out by any typical separation means known to the skilled artisan, such as filtration (e.g. under pressure or vacuum) or decantation. The mesh size of the filtration medium may be, for example, 2 μm or less, 0.45 μm or less, or 0.22 μm or less. The separated product may be washed one or more times with a suitable solvent. The crystallization and separation steps may be carried out once or may be repeated two or more times as necessary to improve the purity of the separated crystallized salt. Such an intermediate separation step may be carried out after the optional neutralization step described above and before step c).

[0051] After step b) but before step c), the process according to the invention may comprise a step of drying the onium salt of FSI, for example drying the ammonium salt of FSI. For example, the separated crystallized salt is dried to obtain a pure dry product. The drying step may be carried out by any means known to the skilled person, typically under reduced pressure and / or by heating and / or by a stream of inert gas, typically a stream of nitrogen.

[0052] The onium salt of FSI obtained at the end of step b) of the process according to the invention is characterized by a high purity, which onium salt is preferably a bis(fluorosulfonyl)imide (NH 4 FSI) ammonium salt.

[0053] Step c) of the process according to the invention comprises reacting the onium salt of FSI obtained from step b) with an alkali salt to obtain the alkali salt of FSI.

[0054] The onium salt of FSI obtained after step b) can then again take part in further reactions. In fact, the process according to the invention comprises a step c) which comprises reacting the onium salt of FSI with an alkali salt to obtain the alkali salt of FSI.

[0055] When the alkali salt is associated with lithium ions, step c) corresponds to a lithiation step, which advantageously results in the lithium salt of bis(fluorosulfonyl)imide (LiFSI).

[0056] The onium salt of FSI obtained after step b) can be used as it is or can be solubilized in a solvent. According to one embodiment, the onium salt of FSI is solubilized in an aprotic organic solvent, preferably an organic solvent which may be selected from: cyclic and acyclic carbonates, such as ethylene carbonate, propylene carbonate, butylene carbonate, dimethyl carbonate, ethyl methyl carbonate, diethyl carbonate, cyclic and acyclic esters, such as gamma-butyrolactone, gamma-valerolactone, methyl formate, methyl acetate, methyl propionate, ethyl acetate, ethyl propionate, isopropyl acetate, propyl propionate, butyl acetate, cyclic and acyclic ethers, such as diethyl ether, diisopropyl ether, methyl tert-butyl ether, dimethoxymethane, 1,2-dimethoxyethane, tetrahydrofuran, 2-methyltetrahydrofuran, 1,3-dioxane, 4-methyl-1,3-dioxane, 1,4-dioxane, amide compounds, such as N,N-dimethylformamide, N-methyloxazolidinone, sulfoxide and sulfone compounds, such as sulfolane, 3-methylsulfolane, dimethylsulfoxide, - cyano, nitro, chloro or alkyl substituted alkanes or aromatic hydrocarbons, such as acetonitrile, valeronitrile, adiponitrile, benzonitrile, nitromethane, nitrobenzene.

[0057] According to a preferred embodiment, the solvent is selected from the group consisting of ethyl acetate, isopropyl acetate, butyl acetate, ethylene carbonate, dimethyl carbonate, ethyl methyl carbonate, propylene carbonate, valeronitrile and acetonitrile.

[0058] The alkali salt of FSI obtained after step c) is an alkali metal salt, preferably a lithium salt, a sodium salt or a potassium salt. Preferably, the alkali metal salt is a lithium salt, and the alkali metal salt of bis(fluorosulfonyl)imide obtained by the process according to the invention is the lithium salt of bis(fluorosulfonyl)imide (LiFSI).

[0059] Examples of alkali salts include alkali hydroxides, alkali hydroxide hydrates, alkali carbonates, alkali hydrogen carbonates, alkali chlorides, alkali fluorides, alkoxide compounds, alkyl alkali compounds, alkali acetates and alkali oxalates. Preferably, alkali hydroxides or alkali hydroxide hydrates are used in step c). When the alkali metal salt is a lithium salt, the lithium salt can be lithium hydroxide LiOH, lithium hydroxide hydrate LiOH.H. 2 O, Lithium carbonate Li 2 CO 3 , Lithium hydrogen carbonate LiHCO 3 , Lithium chloride LiCl, Lithium fluoride LiF, CH 3 Alkoxide compounds such as Oli and EtOLi, alkyllithium compounds such as EtLi, BuLi and t-BuLi, lithium acetate, CH 3 COOLi and lithium oxalate Li 2 C 2 O4. Preferably, lithium hydroxide LiOH or lithium hydroxide hydrate LiOH·H 2 O is used in step c).

[0060] The alkali salt may be added in step c) as a solid, a pure liquid or an aqueous or organic solution.

[0061] The molar ratio of alkali salt to onium salt of FSI used in step c) may vary from 0.2:1 to 10:1, from 0.5:1 to 5:1, or from 0.9:1 to 2:1.

[0062] Step c) may be carried out at a temperature between 0° C. and 50° C., for example between 15° C. and 35° C., preferably at about room temperature.

[0063] Step c) may be carried out at atmospheric pressure or at sub- or superatmospheric pressure, for example from 5 mbar to 1.5 bar, preferably from 5 mbar to 100 mbar.

[0064] Further additional steps may be carried out after step c). For example, the process according to the invention may comprise a separation step after step c). As described above with respect to the onium salt obtained after step b), this optional separation step may be carried out by any typical separation means known to those skilled in the art, such as filtration (for example under pressure or under vacuum) or decantation. As another example, the process according to the invention may comprise an additional step of contacting the reaction medium with an inert gas stream to remove ammonia.

[0065] When the alkali salt used in step (c) is an aqueous solution, the reaction medium may be a biphasic (aqueous / organic) solution. In this case, to recover the alkali salt of the bis(fluorosulfonyl)imide, the process may include a phase separation step during which the aqueous phase is removed and the alkali salt of the bis(fluorosulfonyl)imide is recovered in the organic phase. Additional steps may include filtration, concentration, extraction, recrystallization, purification by chromatography, drying and / or formulation.

[0066] All raw materials used in the process according to the invention, including solvents and reactants, can preferably exhibit very high purity standards, preferably with a content of metal elements such as Na, K, Ca, Mg, Fe, Cu, Cr, Ni, Zn of less than 10 ppm, more preferably less than 5 ppm or even less than 2 ppm.

[0067] Some or all steps of the method according to the invention are advantageously carried out in equipment capable of withstanding the corrosion of the reaction medium. For this purpose, materials are selected for the parts in contact with the reaction medium that are corrosion resistant, such as alloys based on molybdenum, chromium, cobalt, iron, copper, manganese, titanium, zirconium, aluminum, carbon and tungsten sold under the Hastelloy® brand or alloys of nickel, chromium, iron and manganese with the addition of copper and / or molybdenum sold under the names Inconel® or Monel®, more particularly Hastelloy C276 or Inconel 600, 625 or 718 alloys. Austenitic steels may also be selected, more particularly stainless steels such as 304, 304L, 316 or 316L stainless steels. Steels are used that have a nickel content of at most 22% by weight, preferably between 6% and 20% by weight, more preferably between 8% and 14% by weight. The nickel content of 304 and 304L steels varies between 8% and 12% by weight, and that of 316 and 316L steels varies between 10% and 14% by weight. More particularly, 316L steel is chosen. Equipment made of or coated with polymeric compounds that are resistant to the corrosion of the reaction medium may also be used. In particular, materials such as PTFE (polytetrafluoroethylene or Teflon) or PFA (perfluoroalkyl resins) may be mentioned. Glass equipment may also be used. It would not be outside the scope of the invention to use equivalent materials. Other materials that may be suitable for contacting the reaction medium may also be mentioned, such as graphite derivatives. The material for the filtration must be compatible with the medium used. Fluorinated polymers (PTFE, PFA), loaded fluorinated polymers (Viton™) as well as polyester (PET), polyurethane, polypropylene, polyethylene, cotton and other compatible materials may be used.

[0068] A second object of the present invention are alkali metal salts of bis(fluorosulfonyl)imides (alkali metal salts of FSI). Such salts can be obtained, for example, by the process of the present invention. The process described herein involves, in step b), hydrogen fluoride (HF), which can be very harmful to the product, especially if the product is intended to be incorporated into a battery composition, such as an electrolyte. It is therefore very important to minimize the residual content of such hydrogen fluoride in the final product as much as possible.

[0069] The inventors have been able to show that the HF content in the alkali metal salts of FSI obtained by the process of the invention can be reduced to less than 50 ppm, as determined for example by titration (or acid-base titration) using an aqueous NaOH solution in combination with a pH electrode and a potentiometer. The alkali metal salts of FSI of the invention are thus characterized in that their HF content is less than 50 ppm, less than 40 ppm, less than 30 ppm, less than 20 ppm or even less than 10 ppm.

[0070] The alkaline salts of FSI according to the invention advantageously exhibit at least one (and preferably all) of the following characteristics: - 19 A purity of at least 98% by weight, for example 99% to 100% by weight or 99.50 to 100% by weight, as determined by F NMR; - a solvent content determined by GC (alternatively headspace GC) of less than 20% by weight, less than 10% by weight, less than 1% by weight, preferably between 0% and 1% by weight, - a water content of less than 500 ppm, less than 100 ppm, less than 50 ppm or even less than 20 ppm as determined, for example, by Karl Fischer water titration performed in a glove box.

[0071] The alkaline salts of FSI according to the invention advantageously exhibit at least one (and preferably all) of the following characteristics: - a chloride (Cl-) content of less than 100 ppm, preferably less than 50 ppm, more preferably less than 10 ppm or more preferably less than 2 ppm; - a fluoride (F-) content of less than 100 ppm, preferably less than 50 ppm, more preferably less than 40 ppm, more preferably less than 30 ppm, more preferably less than 20 ppm; - less than 100 ppm, preferably less than 50 ppm, more preferably less than 10 ppm or more preferably less than 2 ppm sulfate (SO 4 2- ) content.

[0072] The fluoride and chloride content can be measured, for example, by argentometric titration using an ion selective electrode (or ISE). Alternatively, the sulfate content can be measured by ion chromatography or turbidimetry.

[0073] Preferably, it can exhibit at least one (preferably all) of the following metal element contents: - an iron (Fe) content of less than 100 ppm, preferably less than 50 ppm, more preferably less than 10 ppm; - a chromium (Cr) content of less than 100 ppm, preferably less than 50 ppm, more preferably less than 10 ppm; - a nickel (Ni) content of less than 100 ppm, preferably less than 50 ppm, more preferably less than 10 ppm; - a zinc (Zn) content of less than 100 ppm, preferably less than 50 ppm, more preferably less than 10 ppm; - a copper (Cu) content of less than 100 ppm, preferably less than 50 ppm, more preferably less than 10 ppm; - a copper (Cu) content of less than 100 ppm, preferably less than 50 ppm, more preferably less than 10 ppm; - a manganese (Mg) content of less than 100 ppm, preferably less than 50 ppm, more preferably less than 10 ppm; - a sodium (Na) content of less than 100 ppm, preferably less than 50 ppm, more preferably less than 10 ppm; - a potassium (K) content of less than 100 ppm, preferably less than 50 ppm, more preferably less than 10 ppm; - A (Pb) content of less than 100 ppm, preferably less than 50 ppm, more preferably less than 10 ppm.

[0074] The elemental impurity content can be measured, for example, by ICP-AES (inductively coupled plasma), and more specifically, the Na content can be measured by AAS (atomic absorption spectroscopy).

[0075] In some embodiments, the alkali salt of the FSI of the present invention is an alkali metal salt, preferably a bis(fluorosulfonyl)imide, Li + (FSO 2 ) 2 N - (LiFSI). The lithium salt of bis(fluorosulfonyl)imide may be characterized by the following impurity profile: - 19 A purity of at least 99.90% by weight, ranging from 99.90% by weight to 100% by weight, as determined by F NMR; and - Water content less than 50 ppm as determined by Karl Fischer water titration.

[0076] A third object of the present invention is a method for producing an onium salt of a bis(fluorosulfonyl)imide (FSI), comprising the steps of: a) reacting bis(chlorosulfonyl)imide (or a salt thereof) with onium chloride to produce an onium salt of bis(chlorosulfonyl)imide (onium salt of CSI), which is carried out in the absence of a solvent or in the presence of less than 5% by weight of a solvent based on the total weight of the reaction mixture involved in step a) in molten bis(chlorosulfonyl)imide (or a salt thereof); b) reacting the onium salt of CSI with anhydrous hydrogen fluoride in at least one organic solvent to produce the onium salt of bis(fluorosulfonyl)imide (the onium salt of FSI); The method includes:

[0077] According to this aspect of the invention, an onium salt of a bis(fluorosulfonyl)imide, such as NH 4FSI is prepared and isolated. The method for producing such salts comprises at least two steps, namely steps a) and b), which correspond to steps a) and b) of the method described in the first object of the present invention. All disclosures made regarding these two steps apply to the method described in the third object of the present invention.

[0078] According to the present invention, the method for producing an onium salt of FSI, such as an ammonium salt of FSI, may include additional steps as described above. For example, the method may include one or more of the following additional steps: - adding to the reaction medium a basic compound which corresponds to the neutralization or precipitation of the onium salt; - a step of crystallizing an onium salt of a bis(fluorosulfonyl)imide or a number of steps of crystallizing an onium salt, e.g. under different conditions, a step of separation, for example by filtration (for example under pressure or under vacuum) or decantation, - drying the onium salt of the bis(fluorosulfonyl)imide, for example drying the ammonium salt of the bis(fluorosulfonyl)imide.

[0079] Preferably, the method for producing an onium salt of FSI of the present invention comprises in step a) providing that the onium chloride is ammonium chloride NH 4 In this case, the method of the present invention is a method for producing the ammonium salt of FSI, which is bis(fluorosulfonyl)imide (NH 4 This is a method for producing ammonium salts of FSI. a) Bis(chlorosulfonyl)imide (or its salt) is reacted with ammonium chloride to obtain bis(chlorosulfonyl)imide (NH 4 forming an ammonium salt of bis(chlorosulfonyl)imide (or a salt thereof) in the absence of a solvent or in the presence of less than 5% by weight of a solvent based on the total weight of the reaction mixture involved in step a), in molten bis(chlorosulfonyl)imide (or a salt thereof); b) NH in at least one organic solvent 4reacting CSI with anhydrous hydrogen fluoride to form an onium salt of bis(fluorosulfonyl)imide (the onium salt of FSI); Includes.

[0080] A fourth object of the present invention is the onium salts of bis(fluorosulfonyl)imides (FSI). Such salts can be obtained, for example, by the process of the present invention. The process described herein involves, in step b), hydrogen fluoride (HF), which can be very harmful to the product, especially if the product is intended to be incorporated into a battery composition, such as an electrolyte. It is therefore very important to minimize as much as possible the residual content of such hydrogen fluoride in the final product. The inventors have been able to show that the HF content in the onium salts of bis(fluorosulfonyl)imides obtained by the process of the present invention can be reduced to less than 50 ppm, determined, for example, by titration (or acid-base titration) using an aqueous NaOH solution in combination with a pH electrode and a potentiometer. The onium salts of bis(fluorosulfonyl)imides of the present invention are therefore characterized in that their HF content is less than 50 ppm, less than 40 ppm, less than 30 ppm, less than 20 ppm or even less than 10 ppm.

[0081] The onium salts of bis(fluorosulfonyl)imides of the present invention advantageously exhibit at least one (and preferably all) of the following characteristics: - 19 a purity of at least 98% by weight, e.g., 99% to 100% by weight or 99.50 to 100% by weight, as determined by F NMR; - a solvent content determined by GC of less than 20% by weight, less than 10% by weight, less than 1% by weight, preferably between 0% and 1% by weight, - a water content of less than 500 ppm, less than 100 ppm, less than 50 ppm or even less than 20 ppm as determined, for example, by Karl Fischer water titration.

[0082] The onium salts of FSI according to the invention advantageously exhibit at least one (and preferably all) of the following characteristics: - a chloride (Cl-) content of less than 100 ppm, preferably less than 50 ppm, more preferably less than 10 ppm or more preferably less than 2 ppm; - a fluoride (F-) content of less than 100 ppm, preferably less than 50 ppm, more preferably less than 40 ppm, more preferably less than 30 ppm, more preferably less than 20 ppm; - less than 100 ppm, preferably less than 50 ppm, more preferably less than 10 ppm or more preferably less than 2 ppm sulfate (SO 4 2-) Content.

[0083] The fluoride and chloride content can be measured by argentometric titration using an ion selective electrode (or ISE), while the sulfate content can be measured by ion chromatography or turbidimetry.

[0084] Preferably, it can exhibit at least one (preferably all) of the following metal element contents: - an iron (Fe) content of less than 100 ppm, preferably less than 50 ppm, more preferably less than 10 ppm; - a chromium (Cr) content of less than 100 ppm, preferably less than 50 ppm, more preferably less than 10 ppm; - a nickel (Ni) content of less than 100 ppm, preferably less than 50 ppm, more preferably less than 10 ppm; - a zinc (Zn) content of less than 100 ppm, preferably less than 50 ppm, more preferably less than 10 ppm; - a copper (Cu) content of less than 100 ppm, preferably less than 50 ppm, more preferably less than 10 ppm; - a copper (Cu) content of less than 100 ppm, preferably less than 50 ppm, more preferably less than 10 ppm; - a manganese (Mg) content of less than 100 ppm, preferably less than 50 ppm, more preferably less than 10 ppm; - a sodium (Na) content of less than 100 ppm, preferably less than 50 ppm, more preferably less than 10 ppm; - a potassium (K) content of less than 100 ppm, preferably less than 50 ppm, more preferably less than 10 ppm; - A (Pb) content of less than 100 ppm, preferably less than 50 ppm, more preferably less than 10 ppm.

[0085] The elemental impurity content can be measured by ICP-AES (Inductively Coupled Plasma), more specifically, the Na content can be measured by AAS (Atomic Absorption Spectroscopy).

[0086] In some embodiments, the onium salt of a bis(fluorosulfonyl)imide of the present invention is an ammonium salt of a bis(fluorosulfonyl)imide. The ammonium salt of a bis(fluorosulfonyl)imide may be characterized by the following impurity profile: - 19 A purity of at least 99.90% by weight, ranging from 99.90% by weight to 100% by weight, as determined by F NMR; and - Water content less than 50 ppm as determined by Karl Fischer water titration.

[0087] A fifth aspect of the invention is the use of an alkali salt of a bis(fluorosulfonyl)imide as described above, preferably lithium bis(fluorosulfonyl)imide, in a battery electrolyte which can then be used in the manufacture of a battery or battery cell by placing it between a cathode and an anode in a manner known per se.

[0088] To the extent that the disclosures of any patents, patent applications, and publications incorporated herein by reference conflict with the statements of this application to the extent that the terms may be unclear, the statements of this application shall control. EXAMPLES

[0089] The present disclosure will now be described in more detail with reference to the following examples, the purpose of which is merely illustrative and is not intended to limit the scope of the present disclosure.

[0090] Example 1: Formation of bis(fluorosulfonyl)imide ammonium salt Step a)—Formation of bis(chlorosulfonyl)imide ammonium salt A three-necked 250 mL glass flask was equipped with a thermometer, a mechanically stirred 4-blade shaft, and a screw-type solid addition head, and the flask was connected to a KOH-scrubber via PTFE tubing. The system was flushed with argon for 30 min before use. Bis(chlorosulfonyl)imide (52.6 g, 243 mmol) was dissolved in a glove box and transferred to the flask via cannula under argon, then preheated to about 50 °C. Anhydrous ammonium chloride (13 g, 243 mmol) was placed in the solid addition screw-type glass apparatus and added gradually over 0.5 h under argon removal and constant stirring. After addition was complete, the slurry was heated at 60 °C for 1 h with vigorous stirring until no solid particles remained and gas evolution ceased, then at 75-80 °C for 2 h. HCl was neutralized in a KOH-scrubber, and the chlorine content was recovered by ion chromatography. The bis(chlorosulfonyl)imide ammonium salt was isolated (55.6 g, >99% yield) and then dissolved in 1,4-dioxane (150 g) under mechanical stirring for 15 minutes at 25° C. The resulting solution of bis(fluorosulfonyl)imide ammonium salt was used directly in the next step.

[0091] Step b) - Formation of bis(fluorosulfonyl)imide ammonium salt: Fluorination of bis(chlorosulfonyl)imide ammonium salt A previously prepared mixture of bis(chlorosulfonyl)imide ammonium salt (55.6 g) in 1,4-dioxane (250 g) was introduced under argon into a Hastelloy 0.5 L autoclave equipped with a magnetically coupled 4-blade stirring shaft and 4 baffles. Anhydrous HF (24 g, 5 eq.) was slowly introduced into the system under stirring at room temperature over 1 h. The pressure was increased and stabilized over 6 h. After 18 h, the excess HF was removed with nitrogen over 12 h, then the mixture was filtered under argon. The solid crude NH 4FSI (45.3 g, 95%) was dried at room temperature for 12 h. 19 Analysis by F NMR showed a purity of >99%.

[0092] Example 2: Formation of bis(fluorosulfonyl)imide lithium salt 29.7 g of the dried solid obtained from Example 1 was solubilized in 300 g of butyl acetate. 2 6.9 g of aqueous O solution was added. The resulting two-phase mixture was stirred at room temperature for 5 hours and then decanted. The organic phase was collected and placed in a thin-film evaporator at 60° C. under reduced pressure (0.1 bar). The resulting lithium bis(fluorosulfonyl)imide (LiFSI) had a purity of more than 99.99% by weight, a HF (residual acidity) content of less than 5 ppm, a chlorine and fluorine content of less than 20 ppm, a metal element content of less than 5 ppm, and a SO 4 2- and FSO 3 - Impurities such as NH were not detected (detection limit). The overall yield of LiFSI was 90% (NH 4 Based on FSI).

Claims

1. 1. A method for producing an onium salt of a bis(fluorosulfonyl)imide, comprising the steps of: a) reacting a bis(chlorosulfonyl)imide or a salt thereof with an onium chloride to produce an onium salt of the bis(chlorosulfonyl)imide (onium salt of CSI), which is carried out in the absence of a solvent or in the presence of less than 5 wt. % of a solvent based on the total weight of the reaction mixture involved in step a) in molten bis(chlorosulfonyl)imide (or a salt thereof); b) reacting the onium salt of CSI with anhydrous hydrogen fluoride in at least one organic solvent to produce the onium salt of bis(fluorosulfonyl)imide (the onium salt of FSI); The method includes:

2. In step a), the onium chloride is ammonium chloride (NH ４ 2. The method of claim 1, wherein said compound is selected from the group consisting of aryl, ... and aryl groups.

3. 1. A process for producing an alkali salt of a bis(fluorosulfonyl)imide, comprising the steps of: c) reacting the onium salt of FSI obtained in claim 1 with an alkali salt to obtain an alkali salt of bis(fluorosulfonyl)imide (alkali salt of FSI) The method includes:

4. 2. The process according to claim 1, wherein step b) is carried out at a temperature ranging between 30° C. and the boiling point of the organic solvent.

5. The process according to any one of claims 1 to 4, wherein step b) is carried out under reduced pressure.

6. 5. The method according to claim 1, wherein in step b), the onium salt of CSI is dissolved in the organic solvent before the addition of the anhydrous hydrogen fluoride.

7. 5. The method according to claim 1, wherein in step b), the molar ratio of the onium salt of CSI to the anhydrous hydrogen fluoride is in the range of 0.001:1 to 20:

1.

8. 5. The method according to claim 1, wherein in step b) the solvent is an anhydrous organic solvent having a water content of less than 5,000 ppm.

9. In step a), the ammonium chloride NH ４ 3. The method of claim 2, wherein Cl is in powder form.

10. 5. The method according to claim 1, wherein in step a) the molar ratio of the onium chloride to the bis(chlorosulfonyl)imide (or a salt thereof) is in the range of 0.001:1 to 20:

1.

11. 4. The method according to claim 3, wherein the alkali salt in step c) is selected from alkali metal hydroxides, alkali metal hydroxide hydrates, alkali metal carbonates, alkali metal hydrogen carbonates, alkali metal chlorides, alkali metal fluorides, alkali metal alkoxide compounds, alkyl alkali metal compounds, alkali metal acetates and alkali metal oxalates.

12. An alkali metal salt of bis(fluorosulfonyl)imide (alkali metal salt of FSI) obtainable by the process according to any one of claims 1 to 4, characterized in that its HF content, determined by titration, is less than 50 ppm.

13. 13. Use of an alkali metal salt of FSI according to claim 12 in a battery electrolyte solution.

14. An onium salt of a bis(fluorosulfonyl)imide (onium salt of FSI) obtainable by the process according to claim 1 or 2.

15. 15. The onium salt of FSI of claim 14 having an HF content of less than 50 ppm as determined by titration using aqueous NaOH in combination with a pH electrode and a potentiometer.