Process for the preparation of optically active methionine amide

Abstract: The invention relates to a process for the preparation of optically active methionine amide according to which a mixture of D- and L-methionine amide or the Schiff bases thereof is at least partly converted, optionally in the presence of 0.5-4 equivalents of an aldehyde, relative to the amount of methionine amide, and water, in the presence of an organic solvent, using less than 1.2 equivalents of L- or D-mandelic acid, respectively, relative to the amount of D- or L-methionine amide, respectively, or the Schiff bases thereof, present in the mixture of D- and L-methionine amide or the Schiff bases thereof, into a salt of methionine amide and mandelic acid, a portion consisting substantially of one of the diastereoisomers of said salt is separated from the reaction mixture obtained and the salt is converted into the optically active methionine amide in a manner known per se. A high degree of optical purity is obtained. This process can be advantageously combined with a preparation of D,L-methionine amide from D,L-methionine nitrile by returning the residual methionine amide obtained after separation of the diastereomeric salt and recovery of the mandelic acid to the preparation of D,L-methionine amide where racemisation of the recycled methionine amide takes place in situ. In this manner a high overall efficiency is obtained in spite of a relatively low efficiency of conversion into the diastereoisomeric salt, relative to the amount of D- and L-methionine amide, or the Schiff bases thereof, used.

Description: The invention relates to a process for the preparation of optically active methionine amide according to which, in the presence of water and an organic solvent, using an optically active carboxylic acid, a mixture of the Schiff bases of D- and L-methionine amide is at least partly converted into a salt of the methionine amide and the carboxylic acid, a portion consisting substantially of one of the diastereoisomers of said salt is separated from the reaction mixture obtained and the salt is converted into the optically active methionine amide in a manner known per se. Such a process is known from EP-A-442584, which describes an asymmetrical transformation of amino acid amides with the aid of optically active carboxylic acids. The asymmetrical transformation of methionine amide with the aid of 2-pyrrolidone-5-carboxylic acid is mentioned as an example. Although the optically active methionine amide is obtained with a large enantiomeric excess (ee), the described resolution of methionine amide involves a number of practical drawbacks. In particular the crystal properties of the salt of methionine amide and 2-pyrrolidone-5-carboxylic acid formed as an intermediate are relatively poor, resulting in relatively poor filterability and processability in general. Moreover, the 2-pyrrolidone-5-carboxylic acid is not easily recoverable. The aim of the invention is to remove the aforementioned practical drawbacks without reducing the enantiomeric excess of the methionine amide obtained. This is achieved according to the invention by using L- or D-mandelic acid as optically active carboxylic acid in an amount smaller than 1.2 equivalents relative to the amount of Schiff base of D- or L-methionine amide, respectively, present in the mixture of Schiff bases of D- and L-methionine amide, and also using an amount of water that is at least equimolar relative to the amount of mandelic acid. It has been found that the crystal properties of the diastereoisomeric methionine amide/mandelic acid salt are better than those of the corresponding methionine amide-2-pyrrolidone-5-carboxylic acid salt, which means that the methionine amide/mandelic acid salt has better filterability and processability in general. It has, however, also been found that when the process described in EP-A-442584 was followed, using L- or D-mandelic acid as the optically active carboxylic acid and a racemic mixture of L- and D-methionine amide as the amino acid amide, the optically active carboxylic acid and the amino amide being used in virtually equimolar amounts according to EP-A-442584, it was not possible to separate L- and D-methionine amide. However, the applicant has found that when use was made of less than an equimolar amount of L-or D-mandelic acid, relative to the total amount of Schiff bases of both D- and L-methionine amide, namely less than 1.2 equivalents of L- or D-mandelic acid, relative to the amount of Schiff base of D or L-methionine amide, respectively, present in the mixture of Schiff bases of D- and L-methionine amide, it was possible to separate L- and D-methionine amide. Preferably use is made of 0.8-1.1 equivalents of L- or D-mandelic acid, respectively, relative to the amount of Schiff base of D or L-methionine amide, respectively, present in the mixture of Schiff bases of D- and L-methionine amide. A lower mandelic acid/methionine amide ratio presents the drawback of a lower degree of conversion while a higher ratio affects the ee obtained in the product. With the process according to the invention an enantiomeric excess of more than 95%, in particular more than 98%, more in particular more than 99%, can be obtained. Instead of a mixture of the Schiff bases of L- and D-methionine amide, it is of course also possible to use a mixture of L- and D-methionine amide and an aldehyde, in which case, it is assumed, the Schiff base of methionine amide is formed in situ in an equilibrium reaction. In view of the fact that 1 equivalent of water, relative to the amount of Schiff base formed, is released in the formation of the Schiff base, no extra water need to be added to the reaction mixture in that case. The mixture of L- and D-methionine amide or their Schiff bases may be a racemic mixture of the two enantiomers or may concern any other ratio of the two enantiomers. In practice use will usually be made of a racemic or virtually racemic mixture of L- and D-methionine amide, for example a mixture of D- and L-methionine amide with an ee value of less than 20%. As optically active mandelic acid use is usually made of optically active mandelic acid with an ee value of more than 95%, preferably more than 98%, in particular more than 99%. The invention also relates to the new diastereoisomeric LD and DL salts of mandelic acid and methionine amide that are obtained as intermediates. Examples of aldehydes that may be used in the process according to the invention are aromatic aldehydes such as benzaldehyde, anisaldehyde, o-, p- or m-nitrobenzaldehyde, o-, p- or m-chlorobenzaldehyde or aliphatic aldehydes such as isobutyraldehyde or isovaleraldehyde. Preferably, benzaldehyde is used. The amount of aldehyde to be added is 0.5-4.0 equivalents relative to the amount of methionine amide, preferably 1-2 equivalents. Suitable examples of organic solvents for the process according to the invention are chlorinated hydrocarbons, such as dichloromethane, dichloroethane and chloroform, aromatic hydrocarbons, such as toluene, xylene and benzene, ethers, such as methyl tert.-butyl ether, dioxane, tetrahydrofuran and anisole, esters, such as butylacetate and ethylacetate, ketones, such as acetone, butanone and methyl isobutyl ketone, carboxylic acids, aldehydes or mixtures of said substances. It is clear that the solvent must be chosen so that it does not enter into irreversible chemical reacts with the methionine amide, the optically active mandelic acid or the aldehyde. Preferably a mixture of an apolar solvent that is immiscible with water and a small amount of a polar solvent, for example a lower alcohol such as methanol or ethanol, is used as the solvent. Suitable examples of such mixtures are methyl tert.-butyl ether (MTBE) and methanol, toluene and methanol, and methyl isobutyl ketone (MIBK) and methanol. The pressure at which the process according to the invention is carried out is not critical; it is for example 0.01-1 MPa. Preferably the process is carried out at atmospheric pressure. The temperature may vary within wide limits; usually it is between 20°C and 90°C. The optimum temperature at which the process according to the invention is carried out is partly dependent on a weighing up of, on the one hand, the advantage of a higher reaction rate at higher temperatures and, on the other, the advantage of a lower solubility of the diastereoisomeric salt at a lower temperature. The reaction time is usually 0.1-8 hours, preferably 0.1-2 hours. The slurry concentration of the diastereoisomeric salts at the end of the reaction is usually about 5-30 wt.%, preferably 10-20 wt.%. The optically active methionine amide can be obtained from the separated diastereoisomeric salt by dissolving the salt in a mixture of water and a virtually equimolar amount of mineral acid such as hydrochloric acid, sulphuric acid, nitric acid or phosphoric acid, and extracting the optically active mandelic acid with the aid of an extraction agent. Suitable extraction agents are for example ethers, alcohols, ketones or esters such as methyl tert.-butyl ether, methyl isobutyl ketone, ethyl acetate, butyl acetate or amyl alcohol. The optically active methionine amide obtained can be converted into the corresponding amino acid in a known manner, for example via hydrolysis with the aid of an excess amount of diluted mineral acids such as hydrochloric acid, sulphuric acid, nitric acid or phosphoric acid. The hydrolysis is preferably carried out at 60-100°C, in particular at 85-95°C. Optically active methionine is used in for example infusions. The diastereoisomeric salt of the reaction mixture is usually separated before the hydrolysis and further treatment. Mixtures of D- and L-methionine amide can be obtained in a manner known per se. Preferably, the process according to the invention is used in combination with a process according to which the Schiff bases of D,L-methionine amide are prepared by reacting D,L-methionine nitrile with at least 1 equivalent of an aldehyde or ketone, for example benzaldehyde, and a base, preferably a strong base, in an organic solvent, as described in GB-A-1548032. Under these conditions racemisation of the Schiff base of methionine amide was found to take place. An excellently suitable embodiment of the process according to the invention is hence obtained by returning the filtrate containing the residual Schiff base of methionine amide, obtained after crystallisation and filtration of the diastereoisomeric methionine amide/mandelic acid salt and removal of the residual optically active mandelic acid by means of for example basic water extraction, to the D,L-methionine amide preparation reaction. Moreover, the optically active mandelic acid obtained can be re-used. An added advantage is that the optical purity of the mandelic acid increases gradually in the subsequent cycles. The relatively low degree of conversion with respect to the amount of methionine amide or the Schiff base thereof in the formation of the methionine amide/mandelic acid salt in the reaction according to the invention, as a result of the use of less than an equimolar amount of L- or D-mandelic acid, is in this manner compensated for completely. The invention is now further explained with reference to the following examples, without being limited thereto. Each experiment is carried out in a nitrogen atmosphere. The method used to analyse the products obtained is thin-layer chromatography, for which the following applies: Merck 60 F 254 silica gel is used as a carrier in thin-layer chromatography (tlc). The tlc detection methods are: U.V. (short wave) and ninhydrin. The three tlc eluents and the volume ratios in which they are used are: The selectivity (enantiomeric purity) is defined as follows: selectivity = 50% + 50 x [α] 20 D max. [α] 20 D % enantiomer The maximum specific rotation of D-methionine amide.HCl is described in US-A-4,847,412: [α]²⁰ D = -18.2° (c = 1.0; water). The maximum specific rotation of L-methionine is given in W.J. Pope and J. Ree, J. Chem. Soc. 97 p. 2199 (1910): [α]²⁰ D = +23.4° (c = 3.0; 1.0 N hydrochloric acid). Comparative Experiment Equimolar resolution 0.1 mole (23.6 g) of D,L-N-benzylidene-methionine amide (Schiff base of benzaldehyde and D,L-methionine amide), 0.1 mole (15.2 g) of D-mandelic acid, 250 ml of n-di-butylether, 10 ml of methanol and 2 ml of water (0.11 mole) were stirred for 3 hours at a temperature of 71°C in a reaction flask fitted with a stirrer, a thermometer and a reflux condenser. After cooling to 20°C the salt obtained was filtered and rinsed through a glass filter using 3 x 30 ml of n-di-butyl ether. The salt yield was 26.9 g 3.0 g (0.01 mole) of the salt obtained was dissolved in a mixture of 2 ml of water, 3 ml of 36 wt.% hydrochloric acid and 5 ml of acetone at a temperature of 50°C. With stirring, 100 ml of acetone was then added to this clear solution. The specific rotation of the dried methionine amide.HCl obtained after filtration and rinsing through a glass filter (3 x 10 ml of acetone) (yield = 1.5 g; tlc pure) was: [α]²⁰ D = + 1.0° (c = 1.0; water); selectivity = 52.7% L-enantiomer. Example I Resolution with the aid of 0.5 equivalent D-mandelic acid 0.1 mole (23.6 g) of D,L-N-benzylidene-methionine amide, 0.05 mole (7.5 g) of D-mandelic acid, 90 ml of methyl isobutyl ketone, 10 ml of methanol and 0.9 ml of water (0.05 mol) were stirred for a period (t) of 15 minutes at a temperature of 50°C in a reaction flask fitted with a stirrer, a thermometer and a reflux condenser. The diastereoisomeric salt obtained after cooling to 30°C was filtered and rinsed through a glass filter using 3 x 20 ml of methyl isobutyl ketone. The amount of salt obtained after drying was 8.2 g, which corresponds to an efficiency (E) of 54.7%, relative to the amount of L-methionine amide used. The specific rotation of the tlc-pure methionine amide.HCl prepared from this diastereoisomeric salt was: [α]²⁰ D = + 17.9° (c = 1.0; water); selectivity = 99.2% L-enantiomer (L). Examples II-V Example I was repeated. The data are given in the table. BIMA = D,L-N-benzylidenemethionine amide MA = mandelic acid BA = benzaldehyde MTBE = methyl tert.-butyl ether. Ex. BIMA mole MA mole solvent comb. t min. T °C [α]²⁰ D sel. % E % II 0.2 0.1 (L) 210 ml MTBE 45 50 -17.8° 99.2 (D) 45.7 40 ml CH₃OH 2 ml H₂O III 0.1 0.05 (D) 90 ml MTBE 20 45 +16.7° 95.9 (L) 64.0 9 ml CH₃OH 1 ml H₂O IV 0.2 0.1 (D) 90 ml MTBE 10 45 +17.8° 99.2 (L) 68.7 10 ml CH₃OH 2 ml H₂O V 0.1 0.05 (L) 45 ml MTBE 10 50 -11.7° 82,1 (D) 72.0 5 ml BA 1 ml H₂O Example VI Resolution with the aid of less than 0.5 equivalent D-mandelic acid followed by acid hydrolysis of L-methionine amide to L-methionine 2.7 mole (637 g) of D,L-N-benzylidene-methionine amide, 1.25 mole (190 g) of D-mandelic acid, 1150 ml of methyl tert.-butyl ether, 200 ml of methanol and 23 ml of water (1.25 mol) were stirred for 1 hour at 50°C in a reaction vessel fitted with a stirrer, a thermometer and a reflux condenser. The diastereoisomeric salt obtained after cooling to 30°C was filtered and rinsed through the glass filter using 5 x 200 ml of 85 vol.% methyl tert.-butyl ether/methanol. The yield obtained after drying was 212 g, which corresponds to an efficiency of 52.4%, relative to the amount of L-methionine amide used. 208 g (0.69 mole) of diastereoisomeric salt was dissolved in a mixture of 210 ml of water and 25 ml of 96 wt.% sulphuric acid (0.45 mol) and then the D-mandelic acid was removed by means of extraction using 4 x 300 ml of methyl tert.-butyl ether at a temperature of 30°C. 90 ml of 96 wt.% sulphuric acid was added to the aqueous L-methionine amide.H₂SO₄ solution and this was followed by hydrolysis to L-methionine in 3 hours, with stirring, at 90°C. The acid hydrolysate was neutralized using 250 ml of 25 wt.% ammonia to a pH of 6, with stirring, at a temperature of 60-80°C. The L-methionine obtained after cooling to 25°C was filtered and then rinsed through a glass filter using 2 x 100 ml of water (saturated with L-methionine) and 4 x 75 ml of 70 vol.% methanol/water. The yield of tlc-pure L-methionine obtained after drying was 90.3 g, which corresponds to an efficiency of 88.2%. The specific rotation of the L-methionine is: [α]²⁰ D = + 22.9° (c = 3.0; 1.0 N hydrochloric acid), selectivity = 99.0%. Literature: J. Chem. Soc. 97 p. 2199 (1910); W.J. Pope, J. Reed [α]²⁰ D = + 23.4° (c = 3.0; 1.0 N hydrochloric acid).

Claims: Process for the preparation of optically active methionine amide according to which, in the presence of water and an organic solvent, using an optically active carboxylic acid, a mixture of the Schiff bases of D- and L-methionine amide is at least partly converted into a salt of the methionine amide and the carboxylic acid, a portion consisting substantially of one of the diastereoisomers of said salt is separated from the reaction mixture obtained and the salt is converted into the optically active methionine amide in a manner known per se, characterised in that L- or D-mandelic acid, respectively, is used as the optically active carboxylic acid, that the amount of L- or D-mandelic acid, respectively, is smaller than 1.2 equivalents, relative to the amount of Schiff base of D- or L-methionine amide, respectively, present in the mixture of Schiff bases of D- and L-methionine amide, and that use is made of an amount of water that is at least equimolar relative to the amount of mandelic acid. Process for the preparation of optically active methionine amide according to which a mixture of L- and D-methionine amide is at least partly converted, in the presence of 0.5-4 equivalents of an aldehyde, relative to the amount of methionine amide, and an organic solvent, using an optically active carboxylic acid, into a salt of the methionine amide and the carboxylic acid, a portion consisting substantially of one of the diastereoisomers of said salt is separated from the reaction mixture obtained and the salt is converted into the optically active methionine amide in a manner known per se, characterised in that L- or D-mandelic acid is used as the optically active carboxylic acid and that the amount of L- or D-mandelic acid, respectively, is smaller than 1.2 equivalents, relative to the amount of D- or L-methionine amide, respectively, present in the mixture of D- and L-methionine amide. Process according to claim 2, characterised in that use is made of 1-2 equivalents of an aldehyde, relative to the amount of methionine amide. Process according to any one of claims 1-3, characterised in that use is made of a racemic or virtually racemic mixture of L- and D-methionine amide or their Schiff bases. Process according to any one of claims 1-4, characterised in that use is made of 0.8-1.1 equivalent of L- or D-mandelic acid, respectively, relative to the amount of D- or L-methionine amide, respectively, or of the Schiff bases thereof, present in the mixture of D- and L-methionine amide or the Schiff bases thereof. Process according to any one of claims 1-5, characterised in that mandelic acid with an ee of more than 98% is used as the optically active mandelic acid. Process according to any one of claims 1-6, characterised in that a mixture of an apolar solvent that is not miscible with water and a polar solvent is used as the organic solvent. Process according to any one of claims 1-7, characterised in that the mixture of the Schiff bases of L- and D-methionine amide is at least partly prepared by reacting a mixture of L- and D-methionine nitrile in the presence of at least 1 equivalent of an aldehyde or a ketone, relative to the amount of methionine nitrile, in the presence of a base in an organic solvent in which the reaction mixture obtained after the separation of the diastereoisomeric salt and removal of the optically active mandelic acid is returned to the Schiff base of the D,L-methionine amide preparation. DL-salt of D-methionine amide and L-mandelic acid. LD-salt of L-methionine amide and D-mandelic acid. Process for the preparation of optically active methionine, according to which the optically active methionine amide obtained according to any one of claims 1-8 is hydrolysed to the corresponding methionine.

Inventors: BOESTEN WILHELMUS HUBERTUS JOS, BROXTERMAN QUIRINUS BERNARDUS, BOESTEN, WILHELMUS HUBERTUS JOSEPH, BROXTERMAN, QUIRINUS BERNARDUS
Applicants: DSM NV, DSM N.V.
Application year: 1993
Main classification: C07C319
IPC codes: C07C319, C07C323, C07B53