The present disclosure relates to a method for synthesis of halide salts.
Among halide salts, there are known organic halide salts, including halide salts of ammonia derivatives as well as inorganic halide salts, including metal-halide salts.
The methods for synthesis of the halide salts, both organic and inorganic, aiming at improving the purity of the obtained products and reducing the consumption of harmful or toxic reagents and solvents, are of constant development. Inter alia, the improved purity of the synthesized halide salts can reduce the post-synthesis treatment procedures, such as extraction, precipitation, filtration, charcoal treatment, distillation, etc.
The halide salts of high purity are used in various sectors of industry. For example, inorganic halide salts-such as lead bromide, as well as organic halide salts such as ammonium halide derivatives, e.g., methylammonium iodide (MAI), are used for synthesizing perovskites for photo-active materials used inter alia for the production of solar cells.
Moreover, various methods of synthesizing halide salts are known from the patent literature.
A publication o EP application EP3719001 describes a method for synthesis of organic iodides of general formula RxNI; the method consists in synthesizing hydrogen iodide (HI) in situ by mixing molecular iodine with formic acid in the molar ratio of 12: COOH no less than 1.01:1; next introducing, into the synthesizes HI, a compound being a donor of organic cation: RxN+, providing the molar ratio of RxN+:I2 of no less than 1.01:1, and next maintaining the reaction mixture at a temperature of not less than 20° C. to obtain the reaction product being the salt with the general formula RxNI. Synthesizing HI at the first step of the reaction product and maintaining certain ratios of the reactants prevent the formation of by-products being formates of respective organic cations ([RxN+][HCOO−]), whose donors are added to the reaction mixture. This way the obtained product can be purified in a simple, low-cost manner.
A publication of European patent EP2072496 describes a method for obtaining pure halide quaternary ammonium salt by reducing the amount of a protonic acid salt of a tertiary amine in the quaternary ammonium salt. The method consists in adding an oxide or hydroxide of metal to the quaternary ammonium salt contaminated with a protonic acid salt of a tertiary amine, and next removing the tertiary amine and water by distillation or heating while introducing nitrogen, argon or air, and metal salt produced by filtration or column purification.
In the processes for producing the halide salts belonging to the group of quaternary amine derivatives, typically, the synthesis involves reacting an acid with a respective halide. However, in the course of such synthesis, a part of tertiary amine of basis character (an organic basis), can left unreacted, and thereby can react with the acid to produce a protonic acid salt, permitting the acid salt to remain in the main product of quaternary ammonium salt as the contamination. Further, deacidification of the product solutions is necessary since complete removal of organic bases is possible only after said salts of the tertiary amine have been decomposed.
Further, preparing heavy metal halide salts may involve reacting two soluble metal salts, e.g. heavy metal nitrate with alkali metal halide, to form one soluble salt and one insoluble salt with may be removed by precipitation. For instance, lead nitrate solution and potassium iodide solution can react to produce solid lead iodide, leaving soluble potassium nitrate in the solution. However, the precipitate is typically contaminated with the soluble salt, thus, it may require further purification by washing and filtration procedures.
As follows from the above, many attempts have been taken to address the problem with the purity of the synthesized halide salts. However, despite the various approaches of modifying the synthesis pathway, the known methods do not provide the satisfactory effect of purity of the synthesized halide salts, due to incomplete conversion of the substrates, necessity of using certain substrates in excess, or the presence of by-products in the post-reaction mixture. Thereby, the application of labor-intensive and time-consuming post-treatment procedures, which generate additional costs and chemical wastes, are typically required to obtain the halide salts of required purity.
There is a need to provide a method for the synthesis of halide salts providing improved purity of the obtained products, thereby, limiting the required post-treating procedures.
In one aspect of the present disclosure, there is provided a method for synthesis of halide salts of the general formula (I):
Zn+X−n Formula I
X− represents a halogen anion, and
Zn+ represents a cation having a valency n,
the method comprising reacting a first reactant being formate salt of the general formula (II):
Zn+(COOH−)n Formula II
with a second reactant being a diatom halogen: X2.
Preferably, said diatom halogen X2 is selected from Br2 and I2.
Preferably, said cation (Zn+) is an inorganic cation of a metal selected from the group consisting of Cs+, Ag+, Pb2+, Sn2+, Bi3+, and Sn4+.
Preferably, said cation (Zn+) is Pb2+.
Alternatively preferably, said cation (Zn+) is an organic cation of the general formula (III), (IV), or (V):
Preferably, the organic substituent independently for each of R, R1, R2, R3, and R4, is selected from C1-C16 alkyl, C6 aryl or C10 aryl, C7-26 aralkyl, or heterocycle substituent.
Preferably, the organic substituent independently for each of R, R1, R2, R3, and R4, is selected from:
Preferably, the organic substituent independently for each of R, R1, R2, R3 and R4, is selected from:
Preferably, said cation (Zn+) is the organic cation of the formula (VI), (VII), or (VIII):
Preferably, the method comprises heating the reactants to the temperature of 25 to 130° C. until obtaining the halide salt.
Preferably, reacting of the reactants is carried out in the absence of a solvent.
Alternatively preferably, reacting of the reactants is carried out in the presence of a solvent.
Preferably, the solvent is selected from the group consisting of water, and acetone.
Preferably, the solvent is selected from the group consisting of water, alcohols, and acetonitriles.
Preferably, the method further comprises recrystallizing the obtained halide salt.
Further aspects and features of the present invention are described in the following description of the drawings.
Aspects and features of the present invention will become apparent by describing, in detail, exemplary embodiments of the present invention with reference to the attached drawings, in which:
Reference will now be made to embodiments, examples of which are illustrated in the accompanying drawings. Aspects and features of the embodiments will be described with reference to the accompanying drawings. The present invention, however, may be embodied in various different forms and should not be construed as being limited only to the illustrated embodiments. Rather, these embodiments are provided as examples so that this disclosure will be thorough and complete, and will fully convey the aspects and features of the present invention to those skilled in the art. It shall be understood that not all of the features shown in the embodiments are essential and the scope of the protection is defined not by means of literally shown embodiments, but by the features provided in the claims.
The method for synthesis of halide salts according to the present disclosure involves reacting a formate salt of the general formula Zn+(HCOO)n with a diatom halogen: X2, preferably Br2 or 12 as schematically shown in
The reaction may occur with providing the stoichiometric ratio of the substrates. However, if one of the substrates, either the formate salt (Zn+(COOH−)n) or the halide (X2) is provided in excess, the reaction proceeds until total consumption of the other-deficient substrate. Thereby, no particular limitation for a ratio of these two substrates is required to carry out the synthesis of the halide salts, e.g. the halogen X2 can be added in the amount ranging from 0.5 to 1,2 molar equivalents of the formate salt Zn+(HCOO)n.
To maintain a reasonable reaction time, preferably the reactants: Zn+(COOH−)n and X2 are heated to the temperature of at least 25° C., and preferably to the temperature of at least 60° C. or more, and more preferably the reactants are heated to a temperature between 25 and 130° C., and preferably between 6° and 130° C. For example, the mixture of Zn+(COOH−)n and X2 can be heated to a temperature such as 25° C., 30° C., 40° C., 50° C., 60° C., 70° C., 75° C., 80° C., 85° C., 90° C., or 95° C., and most preferably 70° C., to obtain the halide salt. During heating the mixture of reactants: Zn+(COOH−)n and X2 can be agitated, e.g. stirred or shacked—to provide an increased level of molecules interactions. However, in the case of smaller amounts of the reactants, e.g., in the order of milligrams/milliliters, agitation is not necessarily required. Agitation of the reactants is preferably carried out throughout all the reaction duration. Agitating can be preferably performed from a few seconds to a few hours, and preferably from 1 minute to 4 hours, e.g., from 30 minutes to 1 hour.
Furthermore, the optimum synthesis conditions and times of the reaction may vary depending on the reactants used. Unless otherwise specified, solvents or solvent-free conditions, temperatures, pressures, and other reaction conditions may be readily selected by one of ordinary skill in the art to obtain optimum results for a particular reaction. Optionally, the reaction product may be purified by re-crystallization. For instance, the halide salt-being the reaction product can be obtained in pure form, in liquid or solid state-depending on its melting point, by simple removal of a reaction media such as solvent-if present, under reduced pressure and temperature below boiling or sublimation or decomposition point of the obtained halide salt. If the substrates are used in the stoichiometric ratio, both the substrates can be consumed in total, thereby, not contaminating the product, which enables one to achieved improved purity of the obtained halide salt.
In the course of the reaction, no acids such as hydrohalic acids (HX) are synthesized—the pH value of the reaction media, throughout the reaction of formate salt with the halide (X2), remains neutral, ca. pH=7. It is believed that the reaction of the formate salt with the halide: X2 occurs by a free radical mechanism, and the halide: X2 does not interact with protons H+ e.g. supplied with the solvent; it is further suspected that the reduction of halide: X2 by formate salt constitutes a reaction that is privileged notwithstanding the solvent used, because the reaction leads to the halide salts in the solvent-free conditions as well. Is it further suspected that the solvent molecules, if present in the reaction medium, do not interact with the reactants forming intermediate products or transitional states (such as low-energy transitional states).
The method for synthesis according to the present disclosure allows obtaining halide salts according to the general formula (I):
Zn+X−n Formula I
Preferably, the organic cation Zn+ of the halide salt is a derivative of amine, being either aliphatic amine, aromatic amine, aliphatic-aromatic amine, or aryloamine, including, where applicable, primary amine, secondary amine, tertiary amine; or derivative of imine such as e.g., formamidinium cation. The halide salt is obtained from the corresponding formate salt, comprising said organic cation Zn+, as shown schematically in
Preferably, the organic cation (Zn+) is represented by the general formula (III), (IV), or (V):
As mentioned above R, R1, R2, R3, R4 each independently represents hydrogen or an organic substituent, wherein at least one of R1, R2, R3 is not hydrogen; the organic substituent, independently for each of R, R1, R2, R3, and R4, is preferably selected from:
Non-limiting examples of the organic cation Zn+ used in the composition of the formic salt Zn+(HCOO−) to obtain the halide salt Zn+(X−), according to the present invention (
Further, the non-limiting examples of the organic cation Zn+ include the cations represented by the following formula (VI), (VII), or (VIII):
Thus, the developed method involving the reaction shown in
Preferably, the inorganic cation Zn+of the halide salt constitutes a cation of metal Men+, such as Me+, Me2+, Me3+ and Me4+. Non-limiting examples of the inorganic cation Zn+ used as the component of the formic salt Zn+(HCOO−)—to obtain the halide salt Zn+(X−) according to the present invention (
Thus, the developed method involving the reaction shown in
The reaction, depending on the nature of the substrates, can be carried out in solvent-free conditions, for example for the respective formates (Zn+(HCOO−)n) being liquids in ambient conditions.
Alternatively, the reaction can be carried out in a solvent environment—for example for the respective formates (Zn+(HCOO−)n) being solids in ambient conditions, the solvent allows interacting one reactant (Zn+(HCOO−)n) with the other reactant (X2)—as the molecules of the substrates can move in the solvent. Also, it is a common practice to conduct a chemical reaction in a solvent medium, i.a. to improve agitating the mixture of reactants and provide better heat transfer within the reaction chamber. Thereby, the solvent aims at providing respective solubility of the reactants to improve the amounts of molecules interactions to better the product yield. The non-limiting examples of the solvents that can be used according to the present disclosure include polar solvents, non-polar solvents, being either protic or a-protic, organic or inorganic compounds. Further, a mixture of two or more solvent components can be used as the solvent. Non-limiting exemplary embodiments of the solvent, respectively inorganic and organic are water, methanol, ethanol, isopropanol, ethers, e.g. tetrahydrofuran or acetonitrile, or any mixture thereof, such as ethanol-water mixture, ethanol-ether mixture, isopropanol-water mixture, or acetonitrile-water mixture. E.g. alcoholic solvents can be used in pure form or in the form of their mixture with water, e.g. in form of water-alcohol azeotropes, such as a mixture of 95.63 wt % ethanol and 4.37 wt % water. Also, substantially pure ethanol can be used as the organic polar solvent. The amount of solvent used is not particularly limited. For example, the amount of the solvent may range between 5 to 30 parts by volume (v/W), and preferably amount of the solvent may range between 6 to 8 parts by volume (v/W).
The purpose of solvent is to provide desired dissolution of at least one of the reactants, whereby the other reactant (undissolved) remains suspended in the reaction mixture, or to provide the desired dissolution of both the reactants. The use of the solvent thereby allows for desired agitation of the reactants to facilitate their chemical interaction.
The respective formate: (Zn+(HCOO−)n) for synthesis the corresponding halide salt, can be supplied to a reaction chamber in a form of commercially available products, such as, e.g. commercially available ammonium formate, formamidinium formate methylammonium formate. Alternatively, the respective formate: (Zn+(HCOO−)n) can be prepared in situ (in the reaction chamber), e.g., by using known methods. The exemplary scheme for the synthesis of halide salt comprising the organic cation according to the present disclosure, involving in situ preparation of the salt of formic acid is schematically shown in
Reaction 2 can be carried out in solvent-free conditions as well. If both reactions 1 and 2 are conducted as solvent-free, the obtained halide salt is already crystalline; this can be done preferably if one of the substrates is liquid in ambient conditions, or in the temperature of reaction. Furthermore, if the solvent is present, either in Reaction 1 or in Reaction 2, or both reactions, the obtained halide salt, can be obtained by crystallizing the post-reaction mixture.
The orders in Reaction 1 have no particular limitation. For example, the primary/secondary/tertiary/quaternary amine can be reacted with formic acid in the organic or inorganic polar or non-polar solvent. The amount of the amine in Reaction 1 ranges from 0.1 molar equivalents to 2.0 molar equivalents with respect to the formic acid. Furthermore, the ammonium formate salts can be isolated in a liquid or solid state. The addition of formic acid to the amine is preferably performed at a temperature ranging between −40° C. to 80° C., in order to avoid condensation reaction with loss of water and amide formation. The said polar organic or inorganic solvent in Reaction 1 is preferably water, methanol, ethanol, isopropanol, tetrahydrofuran or acetonitrile, and more preferably water. The amount of the said organic solvent is not particularly limited, e.g., it can range between 5 to 30 parts by volume (v/W), such as 6 to 8 parts by volume.
Further, halogen (X2) in Reaction 2 can be added preferably in the amount ranging between 0.5 to 1.2 molar equivalents of the formate salt, for example of 0.5 to 1 molar equivalents. The temperature in the reaction chamber during Reaction 2 is preferably maintained in the range of 60° C. to 130° C., for example, the temperature of Reaction 2 can be maintained at 60° C., 70° C., 75° C., 80° C., 85° C., 90° C., or 95° C., and more preferably 70° C. During Reaction 2 the reactants are agitated. The duration of Reaction 2, depending on the given formate salt, may range, e.g., from 1 minute to 4 hours, for example, 30 minutes to 1 hour. The obtained halide salt can be obtained in pure form in liquid or solid state by simple removal of the reaction media, such as solvent, under reduced pressure and temperature below boiling or sublimation or decomposition point of the obtained halide salt.
CH3NH3+I−
As a start, 25.0 ml of formic acid was added slowly under cooling (10° C.) to 56.1 ml of methylamine (40 wt % in H2O). The resulting solution was heated to 40° C. and 82.3 g of iodine (I2) was added gradually. Afterward, the product was heated to 110° C. for the time necessary to remove the water. The formed solid was taken up with a 50 ml of hot ethanol and subsequently precipitated in an excess of cold diethyl ether. Afterward, crystals were collected by filtration; the obtained crystals were washed with diethyl ether, and dried in vacuum oven at 60° C., to yield 85.79 g of methylammonium iodide (83% yield).
1H NMR (300 MHZ, DMSO-d6), d: 2.37 (s, 3H) 7.49 (s, 3H). 13C NMR (75 MHZ, DMSO-d6), d: 25.00 (ppm).
CH3NH3+I−
6 g of methylammonium formate was heated at 100° C. Under vigorous stirring, 9.9 g of iodine (I2) was added gradually. The following precipitate was dissolved in small amounts of hot ethanol and subsequently precipitated in an excess of cold diethyl ether. Afterwards, the crystals were collected by filtration; the crystals were washed with diethyl ether and dried in vacuum oven at 60° C. to yield 11 g of methylammonium iodide (89% yield).
CH3NH3+Br−
6.86 ml of formic acid was added slowly under cooling (10° C.) to 15.46 ml of methylamine (40 wt % in H2O). The resulting solution was further cooled and 1.47 ml (4.6 g) of bromine (Br2) was added gradually. Afterwards the product was heated to 110° C. to remove the water. The formed solid was redissolved with a few 50 ml of hot ethanol and subsequently precipitated in an excess of cold diethyl ether. Afterward, crystals were collected by filtration; the crystals were washed with diethyl ether, and dried in vacuum oven at 60° C., to yield 15.82 g of methylammonium bromide (79% yield). 1H NMR (300 MHZ, DMSO-d6), (s, 3H). 13C NMR (75 MHZ, DMSO-d6) (ppm).
CH3NH3+Br−
6 mL of methylammonium formate was cooled at 10° C. Under vigorous stirring, 2 mL of bromine (Br2) were slowly added. The following precipitate was dissolved in small amounts of hot ethanol and subsequently precipitated in an excess of cold diethyl ether. Afterwards, the crystals were collected by filtration; the crystals were washed with diethyl ether and dried in vacuum oven at 60° C. to yield 7.2 g of methylammonium bromide (83% yield).
5.0 ml of formic acid was added to 6.57 g of formamidine acetate at room temperature. After the solid was completely dissolved, 8.0 g of iodine (I2) was added gradually. Afterwards the product was heated to 120° C. to remove the water. The formed solid was redissolved with 50 ml of hot ethanol and subsequently precipitated in an excess of cold diethyl ether. Afterward, crystals were collected by filtration; the crystals were washed with diethyl ether, and dried in vacuum oven at 60° C., to yield 7.28 g of formamidinium iodide (91% yield).
1H NMR (300 MHZ, DMSO-d6), d: - - - (d, 4H) - - - (quint, 1H). 13C NMR (75 MHz, DMSO-d6), d (ppm).
10 g of formamidine formate was heated at 100° C. Under vigorous stirring, 13.5 g of iodine (I2) was added gradually. The following precipitate was dissolved in small amounts of hot ethanol and subsequently precipitated in an excess of cold diethyl ether. Afterwards, the crystals were collected by filtration; the crystals were washed with diethyl ether and dried in vacuum oven at 60° C. to yield 14.7 g of formamidinium iodide (80% yield).
(CH3)4N+I−
4.80 g of tetramethylammonium hydroxide pentahydrate was weighed and dissolved in 8.0 ml of water. At 10° C., 1.0 ml of formic acid was added into the solution first. Reaction was left at 25° C. for 10 hours. Afterward, 3.36 g of iodine was added. The mixture was agitated for 12 hours at 70° C. The reaction solution was cooled to 25° C. Afterward, crystals as products were collected by filtration, washed with diethyl ether, and air-dried at 50° C., to afforded 5.01 g of title compound (94% yield).
1H NMR (600 MHZ, DMSO-d6), d: 3.20 (s, 12H). 13C NMR (150 MHz, D2O), d: 55.85. d (ppm).
2.10 g of pyridine was weighed and mixed with 10 ml of water. At 10° C., 1.0 ml of formic acid was added into the solution first. Reaction was left at 25° C. for 10 hours. Afterward, 3.36 g of iodine was added. The mixture was agitated for 12 hours at 70° C. The reaction solution was cooled to 25° C. Afterward, 10 ml of ethanol was added, and agitating was performed for 10 minutes, then cold diethyl ether was added. Crystals as products were collected by filtration; the crystals were washed with diethyl ether, and air-dried at 50° C., to afforded 4.60 g of pyridinium iodide (86% yield).
2.70 g of imidazole was weighed and mixed with 12 ml of water. At 10° C., 2.0 ml of formic acid was added into the solution first. Reaction was left at 25° C. for 10 hours. Afterward, 6.72 g of iodine (I2) was added. The mixture was agitated for 12 hours at 70° C. The reaction solution was cooled to 25° C. Afterward, 15 ml of ethanol was added, and agitating was performed for 10 minutes, then cold diethyl ether was added. Crystals as products were collected by filtration; the crystals were washed with diethyl ether, and air-dried at 50° C., to afforded 9.88 g of imidazolium iodide (95% yield).
2.14 g of triethylamine was weighed and dissolved in 7 ml of water. At 10° C., 800 ml of formic acid was added into the solution first. Reaction was left at 25° C. for 10 hours. Afterward, 2.69 g of iodine (I2) was added. The mixture was agitated for 12 hours at 70° C. The reaction solution was cooled to 25° C. Afterward, 9 ml of ethanol was added and agitating was performed for 10 minutes. Crystals as products were collected by filtration; the crystals were washed with diethyl ether, and air-dried at 50° C., to afforded 4.23 g of triethylammonium iodide (87% yield).
2.47 g of aniline was weighed and dissolved in 8 ml of water. At 10° C., 1 ml of formic acid was added into the solution first. Reaction was left at 25° C. for 10 hours. Afterward, 3.36 g of iodine (I2) was added. The mixture was agitated for 12 hours at 70° C. The reaction solution was cooled to 25° C. Afterward, 10 ml of ethanol was added and agitating was performed for 10 minutes, then cold diethyl ether was added. Crystals as products were collected by filtration; the crystals were washed with diethyl ether, and air-dried at 50° C., to afforded 3.73 g of aniline hydroiodide (64% yield).
2.13 g of benzylamine was weighted and dissolved in 8.0 ml of water. At 10° C., 750 ml of formic acid was added into the solution first. Reaction was left at 25° C. for 10 hours. Afterward, 2.52 g of iodine (I2) was added. The mixture was agitated for 12 hours at 70° C. The reaction solution was cooled to 25° C. Afterward, 10 ml of ethanol was added and agitating was performed for 10 minutes, then cold diethyl ether was added. Crystals as products were collected by filtration, washed with diethyl ether, and air-dried at 50° C., to afforded 5.54 g of benzylamine hydroiodide (89% yield).
1.50 g of glycine was weighed and dissolved in 16 ml of water. At 50° C., 2.0 ml of formic acid was added into the solution first. Then reaction was left at 50° C. for 10 hours. Afterward, 6.72 g of iodine (I2) was added. The mixture was agitated for 12 hours at 70° C. The reaction solution was cooled to 25° C. Afterward, 30 ml of ethanol was added and agitating was performed for 10 minutes, then cold diethyl ether was added. Crystals as products were collected by filtration; the crystals were washed with diethyl ether, and air-dried at 50° C., to afforded 4.63 g of glycine hydroiodide (43% yield).
1.78 g of β-alanine was weighed and dissolved in 13 ml of water. At 25° C., 2.0 ml of formic acid was added into the solution first. Reaction was left at 25° C. for 10 hours. Afterward, 6.72 g of iodine was added. The mixture was agitated for 12 hours at 70° C. The reaction solution was cooled to 25° C. Afterward, 25 ml of ethanol was added, and agitating was performed for 10 minutes, then cold diethyl ether was added. Crystals as products were collected by filtration, washed with diethyl ether, and air-dried at 50° C., to afford 9.68 g of 3-aminopropionic acid hydroiodide (84% yield).
1.78 g of sarcosine was weighed and dissolved in 13 ml of water. At 25° C., 2.0 ml of formic acid was added into the solution first. Reaction was left at 25° C. for 10 hours. Afterward, 6.72 g of iodine (I2) was added. The mixture was agitated for 12 hours at 70° C. The reaction solution was cooled to 25° C. Afterward, 30 ml of ethanol was added, and agitating was performed for 10 minutes, then cold diethyl ether was added. Crystals as products were collected by filtration, washed with diethyl ether, and air-dried at 50° C., to afford 9.60 g of N-methylglycine hydroiodide (83% yield).
5 g lead (II) acetate were dissolved in 10 ml of water. Subsequently, 10 mL of formic acid were added, resulting in a colorless precipitate. The intermediate product was filtrated and washed with cold water. Subsequently, the wet intermediate product was dissolved in 170 mL of hot water. 20 mL of acetone and 4 g of iodine (I2) were added gradually to the solution under vigorous stirring. The mixture was further agitated for 30 minutes and crystallization of the lead (II) iodide (6 g, 85% yield) was performed in the refrigerator over night.
5 g lead (II) acetate were dissolved in 10 ml of water. Subsequently, 10 mL of formic acid were added, resulting in a colorless precipitate. The intermediate product was filtrated and washed with cold water. Subsequently, the wet intermediate product was dissolved in 170 mL of hot water. 20 mL of acetone and 0.8 mL of bromine were slowly added to the solution under vigorous stirring. The mixture was further agitated for 30 minutes and crystallization of the colorless lead (II) bromide (3.5 g, 62% yield) was performed in the refrigerator over night.
Number | Date | Country | Kind |
---|---|---|---|
22163288.8 | Mar 2022 | EP | regional |
Filing Document | Filing Date | Country | Kind |
---|---|---|---|
PCT/EP2023/056991 | 3/20/2023 | WO |