PROCESS FOR THE PREPARATION OF AN ANTIBIOTIC

Abstract: The invention relates to a process for the preparation of an antibiotic, in particular cefalexin, ampicillin, amoxicillin, cefaclor, cefradin, cefadroxil, cefotaxim and the like, wherein a beta -lactam core is acylated, the antibiotic is recovered from the reaction mixture, the remaining mother liquor is subjected to a hydrolysis reaction in which the antibiotic present in the mother liquor is decomposed into its initial compounds, in particular the beta -lactam core, and the acylation agent is hydrolized. The beta -lactam core can then be recovered virtually quantitatively or recycled to the acylation reaction. This is because it has been found that the solubility of the beta -lactam core is unexpectedly high at relatively high concentrations of acylation agent and antibiotic.

Description: PROCESS FOR THE PREPARATION OF AN ANTIBIOTIC The invention relates to a process for the preparation of an antibiotic whorein a β-lactam core is acylated and the antibiotic is recovered from the reaction mixture and subsequently the remaining mother liquor is worked up. In the preparation of antibiotics involving the acylation of a β-lactam core with an acylation agent, for instance a derivative of a D-phenyl glycine, the recovery of the antibiotic and the working up of the reaction mixture are difficult in general. Thus WO- A-93/12250 for instance describes that the acylation reaction never runs to completion and the ultimate purification of the final product is hindered because the acid/base properties and solubilities of some other components that are present (in particular 7-ADCA and phenyl glycine in the case of cephalexin preparation as described in US-A-4003896) differ little from those of the final product. As a result, coprecipitation occurs, so that impure antibiotic, i.e. cephalexin, is obtained. In WO-A-93/12250 and US-A-4003896 the use of a complexing agent such as naphthol is proposed. However, this entails the drawback that an additional substance alien to the process has to be added. The objective of the invention is to provide a 9imρle, general and widely applicable process, enabling the antibiotic to be recovered pure, without using such organic compounds that are foreign to the process and without large losses of costly (starting) material/ i.e. β-lactam core. This is achieved according to the invention in that in the wor ing-up step the mother liquor - which still contains a relatively high concentration of antibiotic - is subjected to a hydrolysis reaction and subsequently the β-lactam core is at least partially re-used for instance in an acylation reaction. The acylation reaction can be effected either chemically or enzymatically. In the case of a chemical acylation and subsequent working up, racemisation will generally also result in the formation of a very small amount of acylation product with the wrong side chain enantiomer. If the acylation product in the mother liquor is recycled, strong accumulation of this side product may occur. The process according to the invention, with the acylation product and the acylation agent (side chain) being hydrolyzed again, offers the additional advantage of circumventing this problem. The process according to the invention is preferably carried out in combination with an enzymatic acylation reaction. In the state-of-the-art processes a large excess of acylation agont has to be used in an enzymatic acylation reaction in order to ensure a high yield of antibiotic relative to β-lactam core. This entails the drawback that either large losses of acylation agent occur as a result of hydrolysis or that a large quantity of the reaction mixture (that which remains after recovery of the antibiotic in the solid state) has to be worked up. The applicant now has found a process wherein the use of a large excess of acylation agent during the acylation reaction is obviated and wherein nevertheless the β-lactam core losses are limited, by subjecting the mother liquor to a hydrolysis reaction in which antibiotic still present in the mother liquor is decomposed into its initial compounds and the acylation agent is hydrolized as well, with the ability to subsequently recover or recycle the β-lactam core. The fact is that it has appeared that the process according to the invention enables a simple process to be realized, with no need for full conversion of the β- lactam core, while nevertheless only minor losses of β- lactam core occur. Surprisingly, it has been found that the solubility of the β-lactam core is influenced by the presence of remaining acylation agent and antibiotic in the reaction mixture, in the sense that the solubility of the β-lactam core is unexpectedly high at relatively high concentrations of acylation agent and antibiotic. As a result, it was found to be possible to recover virtually quan itatively the β-lactam core in the solid state by hydrolizing the mother liquor obtained after isolation of the antibiotic, which results in hydrolysis of the antibiotic and the acylation agent. Moreover, it waε found that the β-lactam core, in the solid state, was recovered in a purer form than in a process in which hydrolysis of the mother liquor had not been effected. Especially the content of α- substituted acetic acid in the β-lactam core appeared to have been strongly decreased, which in turn had a surprisingly large effect on the acylation reaction speed. In particular, the content of phenylacetic acid in 7-ADCA and the content of phenyl or phenyloxy acetic acid in 6-APA appeared to be strongly decreased. In addition it appeared that the β-lactam core crystals contained little adhering moisture, which means a little amount of impurities. An additional advantage appears in that, because of their low solubility, the β-lactam core crystals could also be washed without large losses. This in turn, means a lower build-up of impurities, possibly accumulating in the antibiotic, in recycling. The β-lactam core obtained after the hydrolysis reaction constitutes a novel composition that has particular advantages in the enzymatic preparation of β-lactam antibiotics. Applicant has found that the free phenyl or phenoxy acetic acid content in the β-lactam core recovered after hydrolysis, is significantly lower than that of the β- lactam core starting material, in particular it has appeared in relation to the 7-ADCA β-lactam core that where the free phenylacetic acid content of the 7-ADCA starting material was 120 ppm, the free phenylacetic acid content of the 7-ADCA obtained after hydrolysis was 69 ppm; for 6-APA these figures were 30 ppm and < 15 ppm, respectively (ppm calculated with respect to the amount of β-lactam core). The invention, therefore, also relates to 7-ADCA with less than 100, in particular lees than 80, preferably less than 70 ppm phenylacetic acid, and to 6-APA with less 20, preferably less than 15 ppm α-aryl- or aryloxy acetic acid, particularly α-phenyl- or α-phenyoxyacetic acid. Another advantage of the process according to the invention is that as a rule the - generally valuable - hydrolized acylation agent can effectively be recovered. Optionally, the β-lactam core can be recycled in solution to the acylation reaction after the hydrolysis reaction. Preferably, the β-lactam core is recovered, however, for instance by lowering the pH and isolating the β-lactam core precipitated in the solid state. The hydrolized acylation agent can be recovered at various places in the process as a whole, for instance after the hydrolysis reaction, after the recovery of the β-lactam core or after the condensation reaction. The hydrolysis is preferably carried out in the presence of a suitable enzyme. Suitable enzymes for the enzymatic hydrolysis reaction are for instance the enzymes that are used in the preparation of β-lactam cores and in the enzymatic acylation reactions, for instance amidases or acylases, in particular penicillin amidases or acylases. Such enzymes are described for instance by J.G. Shewale et al. in Process Biochemistry, August 1989, pp. 146-154, and in Process Biochemistry International, June 1990, pp. 97-103. Examples of suitable enzymes are enzymes derived from Acetobacter, in particular Acetobacter oasteurianum. Aeromones. Alcaliσenes. in particular Alcaliσenes faecalis, Aphanocladlum, Bacillus sp. , in particular Bacillus meqateriυiri, Cephalosporiμm, Escherichia. in particular Escherichia coli , Flavobacterium, Kluyvera. Mvcoplana. Protaminobacter . Pseudomonas en Xanthomonas, in particular Xanthomonas citrll. Preferably an immobilized enzyme is used, since the enzyme can be easily isolated and re-used then. A suitable immobiliza ion technology is described for instance in EP-A-222462. Another suitable technology consists in immobilizing the Penicillin G acylase on a carrier which contains a gelating agent, for instance gelatin, and a polymer with free amino groups, for instance alginate amine, chitosan or polyethylene i ine. If besides the immobilized enzyme other solid substances are present as well, isolation can be effected with good results for instance by the method described in WO-A-9212782. Immobilized enzymes are known as such and are commercially available. A suitable enzyme for the enzymatic hydrolysis reaction has appeared to be Penicillin-G acylase from Bacillus meσaterium or Alcallαenes faecalis, described for instance in EP-A-453047. Also suitable are the Esςherj.chia coli enzyme from Boehringer Mannheim GmbH, which ia commercially available under the name 'Enzygel*', a Penicillin-G acylase from Escherichia coll. immobilized by means of the above-mentioned techniques, and the immobilized Penicillin-G acylase from Recordati. A suitable method of recovering the antibiotic is for instance to lower the pH of the reaction mixture obtained after the acylation reaction, having a pH between 5 and 10, particularly between 6 and 10, preferably between 6 and 9, particularly between 7 and 8.5, thereby causing selective precipitation of the antibiotic; optionally, first the pH of the reaction mixture is brought to a value between 5 and 10, particularly between 6 and 10, preferably between 6 and 9 particularly between 7 and 8.5, and/or the solids are removed. The optimum pH at which antibiotic is recovered depends on the composition of the mixture and is chosen such that optimum separation of β-lactam core and antibiotic is achieved. In practice the optimum pH is a compromise between on the one hand high purity of the antibiotic recovered, which is achieved if the antibiotic is recovered at a relatively high pH, so that the antibiotic is still partly in solution and the β-lactam core still completely in solution, and on the other hand a high yield, which is achieved if the pH at which the antibiotic is recovered is relatively low, so that the antibiotic has been precipitated virtually completely, while at the same time part of the β-lactam core has also been precipitated. For the person skilled in the art it is easy to determine the optimum pH in a given situation. The pH may be lowered in several ways in the framework of the invention, for instance this may be done chemically by adding an acid, for instance a mineral acid or a carboxylic acid, in particular sulphuric acid, hydrochloric acid, nitric acid, acetic acid or formic acid. Another possibility can be applied where for instance, if D-phenyl glycine amide (PGA) has been used as acylation agent in the acylation reaction or if an ester of D-phenyl glycine (PGM) has been used and the pH has been kept constant by means of titration with ammonia during the acylation reaction. In such case the pH can be lowered through physical removal of ammonia. Suitable physical removal methods include for instance stripping with steam or an inert gas; (steam) distillation at reduced pressure, in particular thin- film evaporation; evaporation in a spray tower; gas membrane separation or electrodialysis. The temperature at which the hydrolysis reaction is carried out is not particularly critical and is preferably between 0 and 50°C, in particular between 5 and 40 β C, preferably between 15 and 30°C. The pH at which the hydrolysis reaction is carried out iε not particularly critical and is preferably between 6 and 9, in particular between 7 and 8. The process according to the invention can be suitably applied for the preparation of β-lactam antibiotics, for instance cefalexin, amoxicillin, ampicillin, cefaclor, cefradin, cefadroxil and cefotaxim, cefazolin and the like. Suitable examples of β-lactam cores which can be used according to the invention are various penicillanic acid derivatives, for instance 6- aminopenicillanic acid (6-APA), and cephalosporanic acid derivatives, for instance 7-aminocephalosρoranic acid, with or without a substituent at the 3-site (7- ACA) , for instance 7-aminodesacetoxycephalosporanic acid (7-ADCA) and 7-amino-3-chlorocephalosporanic acid (7-ACCA). In the (enzymatic) acylation reaction, the acylation agent can be for instance a phenyl glycine in activated form, preferably an amide or an ester, for instance a methyl ester; suitable phenyl glycines are for instance substituted or non-substituted phenyl glycines, in particular phenyl glycine, p-hydroxyphenyl glycine, dihydrophenyl glycine. The enzymatic acylation reaction is mostly carried out at a temperature lower than 40°C, preferably between 0 and 35°C. The pH at which the enzymatic acylation reaction is carried out is mostly between 5 and 10, particularly between 6 and 10, preferably between 6 and 9, particularly between 6.5 and 9. In practice the (enzymatic) acylation reaction and the further working up of the reaction mixture are mostly carried out in water. Optionally, the reaction mixture may also contain an organic solvent or a mixture of organic solvents, preferably less than 30 vol.%. Examples of organic solvents that can be used are alcohols with 1-7 carbon atoms, for instance a monoalcohol, in particular methanol or ethanol; a diol, in particular ethylene glycol or a triol, in particular glycerol. An embodiment of the process according to the invention is worked out in detail in the following, relating to the preparation of cephalexin from 7-ADCA and D-phenyl glycine amide (PGA). In this embodiment a reaction mixture obtained after an enzymatic acylation reaction at a pH between 8 and 10 and containing cephalexin. 7-ADCA, PGA and D-phenyl glycine (PG) , is treated to isolate the solid it contains, which solid mainly consists of the immobilized enzyme and possibly PG. The pH of the remaining liquid mixture is then lowered to 6-8, particularly to 6.5-7.5, resulting in the formation of a precipitate which mainly contains cephalexin, after which the solid cephalexin is recovered. In this preferred embodiment the then remaining liquid mixture is subjected to an enzymatic hydrolysis, resulting in hydrolysis in particular of the remaining, dissolved cephalexin and the remaining PGA to 7-ADCA and PG and to PG, respectively; the PG precipitates virtually completely and can be isolated, for instance by filtration. If so desired the PG can be removed (in whole or partly) already during the hydrolysis reaction by circulation of the supsension over a filter outside the reactor. Next, the 7-ADCA can be separated from the then remaining mixture for instance after a further lowering of the pH, thereby causing the 7-ADCA to precipitate; it can then be isolated, for instance by filtration or centrifugation, and used again in an acylation reaction. In the framework of the present invention the various components may bo present in the reaction mixture in the free form or as salts. The pH values mentioned are in all cases the pH values measured with a pH electrode calibrated at room temperature. The invention will be further elucidated by means of the following examples, without however being restricted thereto. Abbreviations; AMOX - amoxicillin trlhydrate AMPI - ampicillin trihydrate CEX « cephalexin CEX.H 2 0 = cefalexin onohydrate 6-APA = 6-aminoρenicillanic acid 7-ADCA - 7-aminodesacetoxycephalosporanic acid PGA = D-phenyl glycine amid© PG = D-phenyl glycine HPGA = D-p-hydroxyphenyl glycine amide HPG = D-p-hydroxyphenyl glycine HPG-Me - D-p-hydroxyphenyl glycine methyl ester Example I Effect of PGA and PEX on the solubility of 7-ADCA The following synthetic mixtures were prepared, with a final pH of 4.5: Mixture 1: 3% (m/m) 7-ADCA in water Mixture 2: 3% (m/m) 7-ADCA and 0.4% (m/m) PG in water Mixture 3: 3% (m/m) 7-ADCA, 0.4% (m/m) PG and 1.5% (m/m) PGA in water Mixture 4: 3% (m/m) 7-ADCA, 0.4% (m/m) PG, 1.5% (m/m) PGA and 3.0% (m/m) CEX.H 2 0 in water Mixture 5: 3% (m/m) 7-ADCA and 3.0% (m/m) CEX.H 2 0 in water. After 2 hours' incubation in a shaker incubator (20°C) samples were taken and the dissolved concentration of each of these components was determined. This table shows that only the combination of PG, PGA and CEX has any significant effect on the solubility of 7-ADCA. Example II Effect of PGA and AMPI on the solubility of 6-APA The following synthetic mixtures were prepared, with a final pH of 4.5: Mixture l: 3% (m/m) 6-APA in water Mixture 2: 3% (m/m) 6-APA and 0.4% (m/m) PG in water Mixture 3: 3% (m/m) 6-APA, 0.4% (m/m) PG and 1.5% (m/m) PGA in watei Mixture 4: 3% (m/m) 6-APA, 0.4% (m/m) PG, 1.5% (m/m) PGA and 3.0% (m/m) AMPI in water After 2 hours' incubation in a shaker incubator (20 β C) samples were taken and the dissolved concentration of each of these components was determined. Results: Here only mixture 4 shows any significant effect on the solubility of 6-APA. Example III Effect of HPGA HPG-Me and AMOX on the solubility of 6- APA The following synthetic mixtures were prepared, with a final pH of 4.5: Mixture 1 : 3% (m/m) 6-APA in water Mixture 2: 3% (m/m) 6-APA and 0.5% (m/m) HPG in water Mixture 3: 3% (m/m) 6-APA, 0.5% (m/m) HPG and 1.5% (m/m) HPGA in water Mixture 4: 3% (m/m) 6-APA, 0.5% (m/m) HPG and 2.0% HPG- Me in water Mixture 5: 3% (m/m) 6-APA, 0.5% (m/m) HPG, 1.5% (m/m) HPGA and 3.0% AMOX in water Mixture 6: 3.0% (m/m) 6-APA, 0.5% (m/m) HPG, 2.0% (m/m) HPG-Me and 3.0% (m/m) AMOX in water After 2 hours' incubation in a shaker incubator (20°C) samples were taken and the dissolved concentration of each of these components was determined. Here only mixtures 5 and 6 had any significant effect on the solubility of 6-APA. Comparative Experiment A Recovery of 7-ADCA from CEX mother liquor through acidi ication 1850 g of slurry containing 12.0% (m/m) of 7- ADCA and 7.2% (m/m) of PGA was supplied to a sieve bottom reactor (pore size 40 μm) which contained 150 g of Enzygel*. The content of phenyl acetic acid in the 7-ADCA amounted to 120 ppm. The initial pH was 7.8 and the temperature was kept at 5°C (reactor flushed continuously with N 2 , stirring rate 500 r.p.m. ). After 3 hours' incubation the reaction mixture (final pH 8.4) was separated across the sieve bottom and the enzyme remaining behind was washed with 185 g of water. Combining of the two flows resulted in a clear solution which contained 11.5% CEX.H 2 0, 4.5% 7- ADCA, 1.5% PGA and 0.6% PG. Next, CEX.H 2 0 was recovered through selective crystallization. To that effect H 2 S0 4 (25% (m/m)) and said solution were supplied simultaneously to a crystallization vessel (pH 7.0, 30 β C). After recrystallization for 30 minutes the CEX.HjO crystals were separated by means of a centrifuge and washed with water and then an acetone/water (80:20) mixture. After drying 168 g of CEX.HjO was thus obtained. The mother liquor solution together with the CEX.H 2 0 washing water had the following composition: CEX.H j O 2.6% (m/m), 7-ADCA 4.2% (m/m), PGA 1.4% (m/m), PG 0.5% (m/m). When this solution was acidified further to pH 4.5, again using 25% H 2 S0 4 , a large portion of the valuable β-lactam components could be crystallized, isolated and recycled. The resulting mother liquor had the following composition: 1.8% (m/m) CEX.H j O, 0.28% (m/m) 7-ADCA, 1.4% (m/m) PGA and 0.5% (m/m) PG. Example IV Recovery of 7-ADCA from CF.X mother llouor bv enzvmatlc hydrolysis of the gEX mother liquor, followed bv acidification The CEX.HjO mother liquor together with the CEX.HjO washing water (obtained as described in comparative experiment A) was brought to a pH of 7.6 with NH OH and a temperature of 30°C. This solution was then supplied to a sieve bottom reactor (pore size 40 μ ) containing 200 g oi immobilized Penicillin-G acylaβe from Recordati. After reacting for 3 hours (500 r.p.m.) the reaction mixture, containing PG in solid form, was drained off and the enzyme and PG in solid form were washed with water in order to reduce β-lactam losses. When the two solutions had been combined the PC crystals were isolated by filtration. The resulting filtrate had the following composition: 4.2% (m/m) 7- ADCA, 0.04% (m/m) CEX.H 2 0, 0.01% (m/m) PGA and 0.54% (m/m) PG. This mother liquor was acidified with H 2 S0 4 (25%) to pH 4.5, causing 7-ADCA to crystallize. After isolation of the 7-ADCA crystals by means of a centrifuge, a mother liquor with a very low β-lactam content was obtained: 0.04% (m/m) CEX.H 2 0 and 0.08% (m/m) 7-ADCA. The content of phenylacetic acid in the 7- ADCA obtained was 69 ppm. Example V Use of the 7-ADCA obtained after a hydrolysis reaction, in an enzymatic acylation reaction. The acylation reaction was carried out in the same way as in Example IV (or Comparative experiment A), apart from the fact that one half of the 7-ADCA used is the same as in Example IV and the other half consists of 7-ADCA which Is regained after the hydrolysis of Example IV, and the fact that the incubation time was 2 hours. Essentially the same composition of the resulting process flows and the same yield of cephalexin were obtained.

Claims: C L I S 1. Process for the preparation of an antibiotic wherein a β-lactam core is acylated and the antibiotic is recovered from the reaction mixture and subsequently the remaining mother liquor is worked up, characte ized in that in the working-up step the mother liquor is subjected to an enzymatic hydrolysis reaction and subsequently the β-lactam core is at least partially re-used. 2. Process according to claim 1, wherein an enzymatic acylation reaction is carried out. 3. Process according to claim l or 2, wherein the hydrolysis is carried out in the presence of an enzyme selected from the group comprising Alcallαanes faecalis. Escherichia coli. Bacillus megate ium and Xanthomonas citrii. 4. Process according to anyone of claims 1-3, wherein an enzyme in immobilized form is used. 5. Process according to any one of claims 1-4, wherein the hydrolysis reaction is carried out at a pH between 6 and 8.5. 6. Process according to any one of claims 1-5, wherein the antibiotic is recovered by lowering the pH. 7. Process according to any one of claims 1-6, wherein the β-lactam core is recovered by modifying the pH of the mixture obtained after the hydrolysis reaction and isolating the precipitate formed. 8. Process according to any one of claims 1-7, wherein cephalexin is prepared by acylation of 7- aminodesacetoxycephalosporanic acid with D-phenyl glycine amide or an ester of D-phenyl glycine. 9. Process according to any one of claims 1-7, wherein amoxiclllin is prepared by acylation of 6- aminopenicillanic acid with D-p-hydroxyphenyl glycine amide or an ester of D-p-hydroxyphenyl glycine. 10. Process according to any one of claims 1-7, wherein ampicillin is prepared by acylation of 6- aminopenicillanic acid with D-phenyl glycine amide or an ester of D-phenyl glycine. 11. Process according to any one of claims 1-7, wherein cefachlor is prepared by acylation of 7- amino-3-chlorocephalosporanic acid with D-phenyl glycine amide or an ester of D-phenyl glycine. 12. Process according to any one of claims 1-7, wherein cefradin is prepared by acylation of 7- aminodesacetoxycophalosporanic acid with D- dihydrophenyl glycine amide or an ester of D- dihydrophenyl glycine. 13. Process according to any one of claims 1-7, wherein cefadroxil is prepared by acylation of 7- aminodesacetoxycephalosporanic acid with D-p- hydroxyphenyl glycine amide or an ester of D-p- hydroxyphenyl glycine. 14. 7-Aminodesacetoxy cephalosporanic acid with less than 100, particularly less than 80, more particularly less than 70 ppm, free phenylacetic acid. 15. 6-Aminopenicillanic acid with less than 20, particularly less than 15 ppm free phenylacetic or phenoxyacetic acid.

Inventors: BOESTEN WILHELMUS HUBERTUS JOS, DEKKERS ROCUS MARINUS, VAN DEN TWEEL WILHELMUS JOHANN, BOESTEN, WILHELMUS, HUBERTUS, JOSEPH, DEKKERS, ROCUS, MARINUS, VAN DEN TWEEL, WILHELMUS, JOHANNES, JOSEPH
Applicants: BOESTEN WILHELMUS H J, CHEMFERM VOF, DEKKERS ROCUS MARINUS, DEN TWEEL WILHELMUS JOHANNES J, BOESTEN, WILHELMUS, HUBERTUS, JOSEPH, CHEMFERM V.O.F., DEKKERS, ROCUS, MARINUS, VAN DEN TWEEL, WILHELMUS, JOHANNES, JOSEPH
Application year: 1996
Main classification: C07D501
IPC codes: C07D501, C12P35, C12P37