Title of Invention

A PROCESS FOR CRYSTALLIZING THE COMPOUND OF THE FORMULA 1

Abstract

The invention relates to a process for obtaining n-(4-trifluoromethylphenyl)-5-methyl-isoxazole-4-carboxamide in crystalline form,which is essentially free of products. For this purpose,n-(4-trifluoromethylphenyl)-5-methylisoxazole-4-carboxamide is transferred into an organic solvent or into mixtures of organic solvents and water,the amount of byproduct in the solution is determined by quantitative analysis and an equimolar amount of a base is added.n-(4-Trifloromethylphenyl)-50methylisoxazole-4-carboxamide is isolated from the resulting solution by crystallization.

Full Text

Description Process for crystallizing N-(4-trifluoromethylphenyl)-5-methylisoxazole-4-carboxamide The invention relates to a process for obtaining N-(4-trifluoromethylphenyl)-5-methyl-isoxazole-4-carboxamide in crystalline form, which is essentially free of byproducts. The compound of the formula I is known per se and is also referred to as N-(4-trifluoromethylphenyl)-5-methyl-isoxazole-4-carboxamide or leflunomide (HWA486). The compound of the formula I can be obtained by the method described in European Patent EP 0 013 376 B1 or the equivalent US Patent US 4,284,786. In said patents, processes for crystallization from toluene are also described. The disadvantage of the known processes for obtaining compounds of the formula I is that byproducts such as N-(4-trifluoromethylphenyl)-2-cyano-3-hydroxy-crotonamide (compound 2 below) essentially cannot be separated by crystallization from solutions containing the compound of the formula I and the compound 2. The compound 2 is described, for example, in European Patent EP 0 217 206 B1 and the equivalent US Patent US 4,965,276. The object of the invention is to provide, by modifying the process conditions, a compound of the formula I in high yields which is essentially free of N-(4-trifluoromethylphenyl)-2-cyano-3-hydroxycrotonamide. The object is achieved by transferring the compound of the formula I, containing the compound 2 as byproduct, into an organic solvent or into mixtures of organic solvent and water, determining the amount of the compound 2 in the solution by an appropriate method of analysis and adding an approximately equimolar amount of a base, for example NaHCOa or KHCO3, and separating the compound of the formula I by crystallization from the solution obtained. The invention therefore relates to a process for obtaining the compound of the formula I from a solution containing water, at least one organic solvent, the compound of the formula I and N-(4-trifluoromethylphenyl)-2-cyano-3-hydroxycrotonamide, which comprises a) quantitatively determining the amount of N-(4-trifluoromethylphenyl)-2-cyano- 3-hydroxycrotonamide in the solution, b) adding the amount of a base which corresponds to from 50 mol% to 150 mol% of the amount determined in a), c) crystallizing the compound of the formula I and d) separating the resulting crystals of the compound of the formula I from the solution. As a result of adding the base, N-{4-trifluoromethylphenyl)-2-cyano-3-hydroxycrotonamide remains in the solution and is not separated off together with the compound of the formula I during the crystallization. Smaller or larger amounts than the amount of added base defined under b) lead to increased byproduct formation and reduce the yield of the compound of the formula I. For obtaining the compound of the formula I, for example, the compound of the formula I is dissolved in a solvent. Suitable solvents are, for example, water-miscible solvents, such as (CrC4)-alcohols, e.g. methanol, ethanol, propanol, isopropanol, butanol or iso butanol, but also ketones, such as acetone or methyl ethyl ketone. Water is then added. Mixtures of organic solvents with water, for example of about 40% to 90% of isopropanol, have also proven useful. The dissolution process is preferably carried out at elevated temperature up to the boiling point of the respective solvent. In the solution obtained, the amount of N-(4-trifluoromethylphenyl)-2-cyano-3-hydroxycrotonamide is determined. Suitable methods of determination are customary quantitative methods of measurement, such as high pressure liquid chromatography (HPLC) or alkalimetric titration. A sample is taken from the solution, and the amount of compound 2 is determined in a standard apparatus. The base is then added to the solution. With the addition of 70 mol% to 130 mol%, based on the determined amount of N-(4-trifluoromethylphenyl)-2-cyano-3-hydroxycrotonamide (compound 2), good results are obtained by HPLC. If the amount of compound 2 is determined by alkalimetric titration, amounts of 95 mol% to 105 mol% are advantageous. The quantitatively determined amount of the compound 2 is taken in each case as 100%, and the corresponding molar amount of the base added in each case is determined. It is preferable to add 85 mol% to 120 mol%, particularly preferably 100 mol% to 115 mol%, very particularly preferably 108 mol% to 112 mol%. The base may be added in dissolved or in solid form; the addition in dissolved form is preferred. The order in which the components water, solvent, compound of the formula I and base are dissolved also differs from the abovementioned order. For example, the base may also be added before the addition of the solvent, water before the addition of the solvent, or the base is not added until the solution has been heated up. Suitable bases are, for example, organic bases, such as mono-, di- or trialkylamine, e.g. trimethylamine, triethyiamine, tripropylamine, tributylamine, triisobutylamine, trimethylamine, trihexylamine, dibutylmethylamine. dimethylamine or diethylamine, the alkylamines being unsubstituted or monosubstituted to disubstituted by phenyl or benzyl, aromatic amines, such as aniline and substiututed anilines, unsubstituted and substituted heterocyclic amines, such as pyridine, piperidine, pyrrole, indole, pyrazine, pyrimidine, morpholine, pyrazoles or imidazole, e.g. alkyl pyridine. Further suitable bases are inorganic bases, such as sodium bicarbonate (NaHCOs). sodium carbonate (Na2C03), potassium bicarbonate (KHCO3), potassium carbonate (K2CO3), sodium hydrogen phosphate (Na2HP04), sodium dihydrogen phosphate (NaH2P04), trisodium phosphate (NaaPOA). potassium hydrogen phosphate (K2HPO4), potassium dihydrogenphosphate (KH2PO4) or tripotassium phosphate (K3PO4), preferably NaHCOa. The solution or suspension obtained is heated and is kept at the boiling point for some time in order to ensure complete solution of the compound of the formula I. Thereafter, the optionally filtered solution is cooled so slowly that crystals of the compound of the formula I form. Cooling preferably takes place to the final temperatures of 20 to -10X, in particular to temperatures of to -5°C, very particularly preferably to temperatures of 10 to SX, The crystals are isolated and optionally washed with isopropanol and then with water. The substance is dried at elevated temperature, preferably at 60°C, under reduced pressure or at atmospheric pressure. Other crystallization methods, such as evaporative crystallization or displacement crystallization, are also possible. A preferred process comprises dissolving the compound of the formula I in 80% strength isopropanol at the boiling point of isopropanol under atmospheric pressure or reduced pressure, carrying out the determination of the amount of N-(4-trifluoromethylphenyl)-2-cyano-3-hydroxycrotonamide by HPLC, adding the equimolar amount of base and then cooling the hot solution slowly so that the crystallization takes place at temperatures of more than 40°C, preferably from 40°C to 85°C, particularly preferably from 45°C to 80°C, in particular from SOX to 70°C, The crystals which have separated out are then washed several times with isopropanol and dried under reduced pressure. The crystallization can be effected without seeding with crystals of the compound of the formula I or preferably in the presence of crystals of the compound of the formula I, which are introduced into the solution by seeding. Seeding can also be effected several times at various temperatures. The amount of the seed material depends on the amount of the solution and can readily be determined by a person skilled in the art. A particularly preferred process for obtaining the compound of the formula I from a solution containing water, at least one organic solvent, the compound of the formula I and N-(4-trifluoromethylphenyl)-2-cyano-3-hydroxycrotonamide comprises a) determining the amount of N-(4-trifluoromethylphenyl)-2-cyano-3-hydroxy-crotonamide in the solution by alkalimetric titration, b) adding the approximately equimolar amount of a base, c) heating the solution obtained to a temperature from 4rC up to the boiling point of the organic solvent, d) diluting the resulting solution with water or distilling off the organic solvent so that the organic solvent and the water are preferably present in a ratio of from 4:1 to 0.3:1 and d) carrying out the crystallization at temperatures above 40°C. Preferably, the solution obtained is filtered after process step b). The abovementioned bases are suitable; sodium bicarbonate, sodium carbonate and potassium bicarbonate are particularly preferred. Good results are obtained with the addition of 90 mol% to 110 mol% of the base, based on the determined amount of compound 2. determined by alkalimetric titration. The quantitatively determined amount of the compound 2 is taken in each case as 100%, and the corresponding molar amount of the base added in each case is then determined. It is preferable to add from 95 mol% to 105 mol%, particularly preferably from 98 mol% to 102 mol%. Advantageous mixtures contain organic solvent and water in the ratio of 1:1 to 8:1, preferably of 2:1 to 6:1, in particular of 3:1 to 5:1. The preparation of the solution is preferably carried out at elevated temperature, in particular at temperatures of 41X up to the boiling point of the respective solvent. The heated solution is, for example, kept at the boiling point for some time in order to ensure complete dissolution of the compound of the formula I. The dissolution process can also be carried out at super atmospheric pressure. The solution is then filtered. The filter used has a pore diameter of about 0,1 |im to 200 lam . Water, which advantageously has the same temperature as the filtered solution, is then added to the filtered solution, or the organic solvent is distilled off. The solutions obtained advantageously contain the organic solvent and water in the ratio of 4:1 to 0.3 :1, preferably of 2:1 to 0.6:1, particularly preferably of 1,6:1 to 0.8:1. Cooling is then carried out slowly to a minimum temperature of 40X. The crystals are isolated and washed with isopropanol and then with water. Drying of the substance is advantageously effected at elevated temperature, preferably at 60'C, under reduced pressure or atmospheric pressure. A particularly preferred process comprises dissolving the compound of the formula I in a mixture of isopropanol and water in the ratio of 4:1 to 5:1 and at the boiling point of isopropanol under atmospheric pressure or reduced pressure and filtering the solution. Water at the same temperature as the hot solution is then added to said solution in an amount such that a ratio of isopropanol to water of 2:1 to 0.8:1 is present. The crystallization is then carried out at temperatures of more than 40°C, preferably of 40°C to 85°C, particularly preferably of 45°C to BOX. in particular of SO^^C to 70°C. The crystals which have separated out are then washed several times with isopropanol and dried under reduced pressure. The purity of better than 99.9% and residual content of von N-(4-trifluoromethylphenyl)-2-cyano-3-hydroxy-crotonamide of less than 0.05%, determined by high pressure liquid chromatography (HPLC), are advantageous in the recovery, according to the invention, of the compound of the formula I. Example 1 Stability of leflunomide to sodium bicarbonate in experiment a), 40 g of the compound of the formula I were dissolved in 80 ml of isopropanol and 63 ml of water (ratio isopropanol to water 1.27:1) and stirred for 1 hour (h) at 84X, Thereafter, a sample was taken and was quantitatively analyzed by HPLC. 0.62 g, 5 mol% based on the compound of the formula I, of NaHCOs was then added and stirring was continued for 5 h at 84°C. In experiment b). a ratio of isopropanol to water of 4:1 was used and the experiment was carried out analogously to a), except that the temperature was SOX. The formation of N-(4-trifluoromethylphenyl)-2-cyano-3-hydroxycrotonamide (compound 2) was monitored by HPLC measurement as a function of time. The results of the HPLC measurement and pH of the individual measurements are summarized in Tables 1 and 2, Table 1 shows the formation of the compound 2 in the absence of sodium bicarbonate, while Table 2 shows the formation of the compound 2 in the presence of sodium bicarbonate. In experiment a) (Table 1), a pH of 4.0 was measured in the starting solution, and the value was unchanged even after 1 h. The amount of compound 2 increased in this time from 0.026 percent by area (% by area) to 0.082% by area. In experiment b) (as Table 1), no determination of the pH or of the amount of compound 2 was carried out. n.d. means not determined In experiment a) (Table 2), a pH of 8.5 was measured in the solution directly after the addition of sodium bicarbonate, and the pH decreased to 4.3 in the course of 5 hours. The formation of the compound 2 after the addition of sodium bicarbonate took place very rapidly. Immediately after the addition of sodium bicarbonate, 3.4% by area of the compound 2 were detectable, and as much as 6.6% by area after 30 minutes (min). After 5 h, an amount of 7.2% by area was reached. In experiment b), the formation of the compound was comparably rapid. An amount of 5.6% by area of the compound 2 was reached after 5 h. The results clearly show that an excess of sodium bicarbonate essentially leads to the formation of the compound 2. Because, depending on the batch for the preparation of the compound I, the content of the compound 2 may vary, it is important to determine the required amount of sodium bicarbonate beforehand by quantitative analysis the amount of compound 2. This is carried out, for example, by HPLC or alkalimetric titration. Quantitative HPLC determination Apparatus: Liquid chromatograph (Waters 2690 with PDA detector 996) Column: Material: stainless steel Length: 125 mm Internal diameter: 4 mm Stationary phase: Lichrospher®100 RP 18 end capped, particle size 5 pm Mobile phase: acetonitrile 350 parts by volume water 650 parts by volume triethylamine 5 parts by volume pH was adjusted to 4.0 with 85% phosphoric acid. Injected volume: 10 pi Flow rate: 1.0 ml/min Detection: UVA/is. 210 nm Run time: 40 min Test solution: About 20,0 mg of the substance to be investigated were dissolved in 4 ml of acetonitrile and made up to 20.0 ml with mobile phase. Calculation: The content of compound 2 was calculated by calculating the arithmetic mean of all injections. A ' 100 = content of compound 2 in % B A = peak area of compound 2 in the chromatogram of the test solution, B = sum of the peak areas in the chromatogram of the test solution. System test: System test solution: 20 mg of 4-trifluoromethylaniline (4-TFMA) are diluted to 10.0 ml with mobile phase (SS1). 30 mg of compound 2 and 10 mg of 3-TFMP-isomer were weighed in. 1.0 ml of the solution SSI and 5 ml of acetonitrile were added. The mixture obtained was made up to 100.0 ml with mobile phase (SS2) and shaken until the solution was clear. 100 mg of the compound of the formula I (leflunomide reference standard) were dissolved in 2 ml of acetonitrile, 1.0 ml of SS2 was added and the solution was made up to 100.0 ml with mobile phase (SS3). SS3 had the following concentration: 1 mg/ml of leflunomide; 0.003 mg/ml of compound 2; 0.0001 mg/ml of 3-TFMP-isomer; 0.0002 mg/ml of 4-TFMA. Selectivity: The chromatogram of the standard solution SS3 had to meet the following requirements: Compound 2 Relative retention time: about 0.13 to 0.23 4-TFMA Relative retention time: about 0.36 to 0.44 Leflunomide Absolute retention time: about 22 to 35 Abbreviations; 4-TFMA: 4-Trifluoromethylaniline 3-TFMP: N-(3 Trifluoromethyiphenyl)-5-methylisoxazole-4-carboxamide Alkalimethc titration Apparatus: Titration with automatic end point detection (e.g. Metrohm Titroprocessor 716) Electrode: combined glass electrode (e.g. Mettler Toledo DG 112-SC) Factor of the standard solution: 0.05 g of succinic acid was dissolved in 50 ml of water and titrated with 0.1 N sodium hydroxide solution. Procedure: 1.0 g of the substance to be tested was dissolved in 50 ml of methanol and immediately titrated with 0.1 N sodium hydroxide solution. Calculation (factor of 0.1 N sodium hydroxide solution): C = Consumption of 0.1 N sodium hydroxide solution (1 ml of 0.1 N sodium hydroxide solution is equivalent to 59.05 mg succinic acid) W = Weight of succinic acid taken, in g Calculation: C = Consumption of 0,1 N sodium hydroxide solution, in ml F = Factor of 1 N hydrochloric acid W = Weight of the substance to be tested in g Example 2 Crystallization in the presence of NaHCOs 16 kg of the compound of the formula I (leflunomide) were dissolved in 28 liters (I) of isopropanol and water so that the total amount of water was 9 I. The amount of the compound 2 in the solution obtained was then determined by alkalimetric titration . The equimolar amount of sodium bicarbonate was calculated and was added in solid form to the solution (cf. Table 3). Thereafter, heating to 78X to 82^ was carried out, stirring was effected for 25 min at this temperature and filtration was then effected through a suction filter into a vessel likewise already heated to the same temperature. The suction filter was then rinsed with the amount of isopropanol which, together with isopropanol used, gave an isopropanol/water ratio of 4:1 (in this case about 4 I). 32 I of water, likewise preheated to from 78X to 82°C, was then added (gave an isopropanol/water ratio of 0.8:1). The solution became turbid and was then cooled to about 65°C in 20 min. kept at this temperature for about 40 min, then cooled to about 40°C in 70 min and stirred for a further 20 min. The crystalline compound of the formula I was isolated by centrifugation. Table 3 summarizes the results of three different crystallizations. An average yield of 79.4% of theory with only very small deviations within the individual batches was achieved (± 0.6%), a purity of on average 99.93% (HPLC, % by area) being obtained. The amount of the compound 2 in the individual batches according to HPLC determination was from 0.02% by area to 0.04% by area. Example 3 Crystallization in the presence of NaHCOs 50 g of the compound of the formula I, containing 0.46% of the compound 2 - the determination of the amount of the compound 2 was carried out by HPLC measurement - were added to 25 ml of isopropanol and 25 ml of water; 28.65 mg of NaHCOa were then added and the suspension obtained was stirred at room temperature of about 2rC for 15 to 30 minutes. Thereafter, 76. ml of isopropanol and 1 g of active carbon were added, heating was carried out to SOX and filtration was effected through a suction filter. The filtrate obtained was cooled to 60X, seeded with a few crystals of the compound of the formula I and then cooled to 0°C to 5X. The crystals obtained were filtered off with suction and washed with 37.5 ml of isopropanol and 3 times with 125 ml of water. The yield was 77% of the compound of the formula I and the purity was more than 99.9% according to HPLC measurement. The content of the compound 2 according to HPLC measurement was less than 0.01%, based on the compound of the formula I as 100%. Example 4 Comparative Example for crystallization without sodium bicarbonate 50 g of the compound of the formula I, containing 1.7% of the compound 2 - the determination of the amount of the compound 2 was carried out by HPLC measurement - were suspended in 93.75 ml of isopropanol and 25 ml of water. After the addition of 1 g of active carbon, the suspension obtained was heated to 84°C and filtered through a suction filter. The filtered solution was washed with 6.25 ml of isopropanol. The solution was cooled to room temperature of about 21 in the course of 2 hours. Thereafter, the solution was cooled to O^C in the course of 30 minutes and this temperature was maintained for 2 hours until the solution was filtered through a suction filter. The filter cake obtained was washed with two 6.25 ml portions of water. The crystals of the compound of the formula I were dried at 50°C under reduced pressure. Yield: 41.8 g of the compound of the formula I, purity 99.1% according to HPLC measurement. The content of the compound 2 was determined by HPLC measurement as 0.86%, based on the compound of the formula I as 100%. Patent claims: 1. A process for obtaining the compound of the formula I from a solution containing water, at least one organic solvent, the compound of the formula I and N-(4-trifluoromethylphenyl)-2-cyano-3-hydroxycrotonamide, which comprises a) Quantitatively determining the amount of N-(4-trifluoromethylphenyl)-2-cyano-3-hydroxycrotonamide in the solution, b) adding the amount of a base which corresponds to from 50 mol% to 150 mol% of the amount of N-(4-trifluoromethylphenyl)-2-cyano-3-hydroxycrotonamide determined in a), c) crystallizing the compound of the formula I and d) separating the resulting crystals of the compound of the formula I from the solution. 2. The process as claimed in claim 1, wherein the base used is an organic base such as mono-, di- ortrialkylamine, e.g. trimethylamine, triethylamine, tripropylamine, tributylamine, triisobutylamine, trimethylamine, trihexylamine, dibutylmethylamine, dimethylamine or diethylamine, the alkylamines being unsubstituted or monosubstituted to trisubstituted by phenyl or benzyl, or an aromatic amine, such as aniline or a substituted aniline or an unsubstituted or substituted heterocyclic amine, such as pyridine, piperidine, pyrrole, indole, pyrazine, pyrimidine, morpholine, pyrazole or imidazole, e.g. (CrC4)- alkyl pyridine, or an inorganic base, such as sodium bicarbonate, sodium carbonate, potassium bicarbonate, potassium carbonate, ammonium bicarbonate, sodium hydrogen phosphate, sodium dihydrogen phosphate, trisodium phosphate, potassium hydrogen phosphate, potassium dihydrogen phosphate ortripotassium phosphate, preferably sodium bicarbonate. The process as claimed in claim 1 or 2, wherein the solvents used are water-miscible solvents, such as (CrC4)-alcohols, e.g. methanol, ethanol, propanol, isopropanol. butanol or is butanol, in particular isopropanol, but also ketones, such as acetone or methyl ethyl ketone, or mixtures of the solvents or mixtures of the solvents with water-immiscible solvents, such as ethyl acetate, toluene or dichloromethane. The process as claimed in one or more of claims 1 to 3, wherein crystallization takes place at temperatures of more than 40°C, preferably of 41 ^'C to 80°C, in particular of SOX to 70X. The process as claimed in one or more of claims 1 to 4, wherein the amount of added base corresponds to from 100 mol% to 115 mol%, very particularly preferably from 108 mol% to 112 mol%, of the amount of N-(4-trifluoromethylphenyl)-2-cyano-3-hydroxycrotonamide determined by quantitative high pressure liquid chromatography in process step a) in claim 1. The process as claimed in one or more of claims 1 to 5, wherein the amount of added base corresponds to from 90 mol% to 110 mol%, preferably from 95 mor/o to 105 mol%, particularly preferably from 98 mol% to 102 mol%, of the amount of N-(4-trifluoromethylphenyl)-2-cyano-3-hydroxycrotonamide determined by alkali metric titration in process step a) in claim 1. The process as claimed in one or more of claims 1 to 6, wherein the crystallization is carried out in the presence of added crystals of the compound of the formula I. The process as claimed in one or more of claims 1 to 7, wherein the solution obtained is filtered after process step b) according to claim 1. The process as claimed in one or more of claims 1 to 8, wherein the mixture of organic solvent in water according to process step b) is heated to a temperature of 40X to 85X. 10. The process as claimed in one or more of claims 1 to 9, wherein the ratio of organic solvent to water in process step a) is from 1 :1 to 8 :1, preferably from 2 :1 to 6 : 1, in particular from 3 : 1 to 5 :1. 11. The process as claimed in one or more of claims 1 to 10, wherein the ratio of organic solvent to water in process step c) is from 4 :1 to 0.3 : 1, in particular from 2 : 1 to 0.6 :1, preferably from 1.6 : 1 to 0.8 :1.

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