(12) Patent Application Publication (10) Pub. No.: US 2004/0048346A1 Tikare (43) Pub

(12) Patent Application Publication (10) Pub. No.: US 2004/0048346A1 Tikare (43) Pub

US 2004004.8346A1 (19) United States (12) Patent Application Publication (10) Pub. No.: US 2004/0048346A1 Tikare (43) Pub. Date: Mar. 11, 2004 (54) SYNTHESIS OF CHIRAL INTERMEDIATES (52) U.S. Cl. .............................................................. 435/128 USEFUL IN PREPARING PHARMACOLOGICALLY ACTIVE COMPOUNDS (57) ABSTRACT (76) Inventor: Raveendra Khandurao Tikare, Majiwada (IN) A process is disclosed for preparing (R)-2-hydroxy-4-phe nylbutyronitrile of formula (I) wherein * signifies the (R) Correspondence Address: stereoisomer; and Ph is the phenyl group C6H5, which Kit M Stetina process comprises reacting, in a biphasic System, 3-phenyl Stetina Brunda Garred & Brucker propionaldehyde of formula (X): with a cyanide compound Suite 250 in the presence of (R)-hydroxynitrilase, wherein the reaction 75 Enterprise is carried out a temperature below (10) C. Preferably, the Aliso Viejo, CA 92656 (US) reaction is carried out at a temperature in the range of from -(5) to (0) C. The compounds of formula (I) thereby (21) Appl. No.: 10/416,171 prepared are useful in the preparation of the family of ACE inhibitors known as "prils, of the general formula (A): (22) PCT Filed: Nov. 21, 2001 wherein R' is hydrogen or C1-C2 alkyl and R" is selected from a large number of possible moieties. Example of (86) PCT No.: PCT/IB01/02794 “prils include lisinopril, cilaZapril, enalapril, benazepril, (30) Foreign Application Priority Data ramipril, delapril, enalaprilat, imidapril, Spirapril, trandola pril and others. These 'prils compounds are chiral com Nov. 23, 2000 (GB)......................................... OO28523.9 pounds, only one of their diastereomers being pharmaco logically active. Use of a chiral intermediate (I) thereby Publication Classification avoids the necessity to isolate and purify the active pril diastereomer, rather than using a racemic mixture, for phar (51) Int. Cl. .................................................. C12P 13700 maceutical/medical applications. US 2004/004.8346 A1 Mar. 11, 2004 SYNTHESIS OF CHRAL INTERMEDIATES 0012. A method that has been proposed for the prepara USEFUL IN PREPARING PHARMACOLOGICALLY tion of optically active cyanohydrins, which are useful in the ACTIVE COMPOUNDS preparation of, inter alia, the optically active prils of 0001. The present invention relates to a process for the formula (A) above, involves synthesis of (R)-2-hydroxy-4- Synthesis of chiral compounds and, in particular, chiral phenylbutyronitrile (I): nitrites for use as intermediates in the Synthesis of the family * Ph-Chi-Chi-CH(OH)–CN (I) of ACE inhibitors known as 'prils. 0013 wherein * signifies the (R) stereoisomer; and Ph is 0002 The prils have the general formula (A): the phenyl group CHs. Ph-CH-CH-CH(COOR)-NH(R") (A) 0014) This method has been reported in U.S. Pat. No. 0003 wherein R' is hydrogen or C-C alkyl and R" is 5,008,192 (and European patent specification no. 326 063), Selected from a large number of possible moieties. Examples in which the reaction between an aldehyde and hydrogen of “prils include lisinopril, cilaZapril, enalapril, benazepril, cyanide is carried out in a homogeneous aqueous medium ramipril, delapril, enalaprilat, imidapril, Spirapril, trandola comprising oxynitrilase at a temperature varying from -5 to pril and others. +50 C. and a pH value ranging from 4 to 6.5. Using this method, the nitrile (I) is said to be produced in a chemical 0004. These “pril compounds are chiral compounds, only purity of up to 93.8% and an optical purity of 95.1%. one of their diastereomers being pharmacologically active. It According to this US patent Specification, however, “ . is therefore necessary to isolate and purify the active dias Since the enzyme activity is considerably reduced by the tereomer, rather than using a racemic mixture, for pharma presence of even Small amounts of organic co-solvents (for ceutical/medical applications. example ethanol), the process should be carried out in the 0005 Typically, separation of diastereomers is carried Substantial absence of an organic co-Solvent'. Thus, it out by preferential crystallisation, for example as described Strongly recommends the avoidance of any organic co in U.S. Pat. No. 5,616,727. However, the yields from such Solvents in the reaction. There is no mention, however, of the crystallisations are often low and, indeed, the yield from the possibility of the use of water-immiscible solvents, thereby process used in U.S. Pat. No. 5,616,727 was only 68%. Signifying that biphasic reactions are also to be avoided. 0006 Alternatively, a stereochemical synthesis may be 0015. Another method involves the use of the stereospe used, wherein various intermediates used in the preparation cific enzyme (R)-hydroxynitrilase (also known as (R)oxyni of the 'prils are, in turn, prepared in chiral form, which trilase) in a two-phase reaction. For example, European results in a predominance of the desired diastereomer in the patent specification no. 547 655 describes the reaction of final 'pril product. However, Such chiral Syntheses are phenylpropionaldehyde with hydrogen cyanide (HCN) at complex and the yields are unsatisfactory. 10° C. and pH 4.5 in the presence of pure (R)-hydroxynit 0007. The present invention relates to an improved, ste rilase at a concentration of 1.5 mg enzyme per mmol of reospecific process for the Synthesis of an intermediate for aldehyde and in the presence of a buffer. This Specification making 'pril compounds. This intermediate can then be reports that this proceSS resulted in an enantiomeric exceSS converted to the required 'pril isomer, or any other desired of the corresponding (R)-cyanohydrin of formula (I) here end-product, without loSS of Stereospecificity. inabove of “ca. 90' (optical purity ca 90%). 0008. One of the building blocks in the synthesis of the 0016. In the same example, this European patent speci 'prils is a cyanohydrin containing the common pril moiety fication discloses up to 99% enantiomeric excess when Ph-CH-CH-CH-, which cyanohydrin can then be con applying Similar reaction conditions to other Substrates, but verted, via the corresponding carboxylic acid ester, to the clearly the reaction is much leSS Successful in the case of the desired “pril. As discussed by C G Kruse in “Chirality in production of (R)-2-hydroxy-4-phenylbutyronitrile (I). If, Industry” (Ed. Collins etal, chapter 14 (1992)), it is probable therefore, one were to use the process of European patent that the use of enantiomerically pure cyanohydrins as build specification no. 547 655 to prepare the “pril intermediate of ing blocks for the production of chiral industrial chemicals formula (I), further purification would be required in order will continue to grow. This avoids the problems associated to provide the level of enantiomeric excess (ee) of the (R) with the optical resolution or asymmetric Synthesis of cer isomer that is desired (ie, an ee of at least 97-98%). As tain products. New routes to homochiral cyanohydrins rep mentioned above, Such purification is a costly process, resent, therefore, an opportunity to enlarge the pool of chiral especially on a production Scale, using chromatographic Separation. Furthermore, this additional Step reduces the Starting materials, which are available to the fine chemicals yield of (R) isomer. High initial purity is therefore required industry. Several criteria must be realized fully before the in the preparation of (R)-2-hydroxy-4-phenylbutyronitrile optically pure cyanohydrins can be adopted as raw materials (I) for it to be commercially advantageous in the Synthesis for industrial processes. These are: of 'prils. 0009 (i) the availability of a range of methods for the manufacture of cyanohydrins with a high enan 0017 We have therefore looked at the possibility of using tiomeric excess (ee) in an economically feasible alternative methods of Synthesizing this nitrile, but none of way; these appeared to provide the desired combination of highee 0010 (ii) the preservation of optical purity during (eg 97-98%); economic reaction time; acceptable yields (eg 95-97%); and overall ease of handling and commercial Subsequent chemical transformations, and viability of the process. 0011 (iii) the possibility of chirality transfer by diastereoselective reactions at either the cyano group 0018. Instead, we have surprisingly found that, by careful or the main organic residue. Selection of novel reaction conditions, we can obtain the US 2004/004.8346 A1 Mar. 11, 2004 desired ee in high yields and under commercially-acceptable isomer of formula (I) of >98% can be achieved, with a yield conditions, using the two-phase oxynitrilase process. also of >98% of theoretical yield, by weight. 0.019 Accordingly, the present invention provides a pro 0029. In the process of the present invention, the ratio of cess for preparing (R)-2-hydroxy-4-phenylbutyronitrile of the Volumes of the aqueous phase to the organic phase is formula (I), which comprises reacting, in a biphasic System, suitably in the range of from 1:5 to 5:1, and it is important 3-phenylpropionaldehyde of formula (X): to control the concentration of the cyanide compound in the organic phase. This is because HCN (the cyanide com Ph-CH-CH-CHO (X) pound) is miscible in both phases. Even though it is Soluble 0020 with cyanide compound in the presence of (R)- in the organic phase, its Solubility in the aqueous phase is hydroxynitrilase, wherein the reaction is carried out a tem greater. For instance, if the Volume of the organic phase is perature below 10° C. increased, nevertheless keeping the Strength of the cyanide 0021. The biphasic system comprises (i) an aqueous compound (eg hydrocyanic acid) constant, the reaction will phase comprising an aqueous Solution of the enzyme and (ii) remain substantially unaffected. However, if the volume of an organic phase comprising a Solution of the cyanide the organic phase is increased by diluting the concentration compound and the aldehyde (X) in a water-immiscible of the cyanide compound in Said phase, the rate of reaction organic Solvent.

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