Title of Invention

A PROCESS FOR THE PREPARATION OF SUBSTITUTED PHENYLACETONITRILES

Abstract

The present invention relates to a process for the preparation of a compound of formula wherein R1 is unsubstituted or substituted alkyl, comprising reacting a compound of formula with a compound of formula in the presence of an aqueous solution of an alkali hydroxide and a phase transfer catalyst selected from a quaternary ammonium salt, quaternary phosphonium salt or a crown ether at a temperature of 0 to 60˚ c

Full Text

Process for the preparation of substituted phenvlacetoniriles The present invention is directed to a process for the preparation of substituted . phenylacetonitriies which is carried out by the reaction of alkoxyphenylacetonitriles with cyclohexanone in the presence of an aqueous base and a phase transfer catalyst. Substituted phenylacetonitriies of formula (1) are known for being particularly useful as synthesis intermediates for preparing pharmaceutical active substances which are central nervous system antidepressants. An important substance is Veniafaxine (see Merck Index Twelfth Edition 1996, No. 10079). The preparation of this compound is described in US-A-4,535,186. According to US-A-4,535,186, Example 1, intermediates of formula (1) are prepared by the reaction of p-methoxyphenylacetonitrile and cyclohexanone in the presence of n-butyl lithium and an organic solvent, like tetrahydrofuran and cyclohexane. The overall yield according to this process is low and does not exceed 50%. Furthermore, the use of n-butyl lithium and organic solvents provides environmental as well as economical drawbacks and results in a process wherein the reaction conditions have to be carefully controlled. It is the object of the present invention to provide a process for the preparation of substituted phenylacetonitriies with improved yield, which also meets environmental as well as economical demands and wherein the reaction conditions can easily be controlled. The present invention relates to a process for the preparation of a compound of formula wherein R1 is unsubstituted or substituted alkyl, comprising reacting a compound of formula The amount of the compound of formula (3) used is preferably 0.9 to 1.8, preferably about 1 to 1.6 molar equivalents relative to the molar amount of the compound of formula (2). • The aqueous base is preferably an aqueous solution of an alkali hydroxide, especially an aqueous solution of sodium hydroxide or potassium hydroxide, most preferably sodium hydroxide. The amount of the base used is preferably 0.05 to 4, preferably 0.1 to 2 and most preferably 0.25 to 1.5 molar equivalents relative to the molar amount of the compound of formula (2). An aqueous solution of the base usually comprises 1 to 70%, preferably 1 to 60% by weight of the base, based on the total of the weight of water and the base. A minimum amount of the base of 3%, especially 5% by weight is preferred. The maximum amount of the base is preferably 50%, most preferably 25%. Examples of phase transfer catalysts are described in WO-A-97/20810, page 6, line 13 to page 7, line 5 which is hereby incorporated by reference. Preferred as phase transfer catalysts are quaternary ammonium salts, quaternary phosphonium salts or crown ethers. Examples for Hal" are fluoride, chloride, bromide and iodide. Preferably Hal' is fluoride, chloride or bromide, most preferably chloride or bromide. Highly preferred is bromide. • Phase transfer catalysts of formula (4a) are preferred. Highly preferred phase transfer catalysts are tetrabutylammonium chloride or bromide, especially tetrabutyiammonium bromide. !t is of course also possible to use mixtures of phase transfer catalysts. The amount of the phase transfer catalyst used is as a rule in the range of from 0.0001 to 0.1, especially 0.0005 to 0.05 molar equivalents relative to the molar amount of the compound of formula (2), A minimum amount of the phase transfer catalyst of 0,001 is preferred. The reaction of compound of formula (2) with compound of formula (3) is carried out at a temperature of 0 to 60°C, especially 0 to 40°C. It is preferred to carry out the reaction at a temperature of 15 to 35°C, especially at room temperature. . As to the reaction it is not necessary to add any organic solvents. This means, that the reaction usually is carried out by addition of the reactants, aqueous solution of the base and phase transfer catalyst. According to a preferred embodiment the reaction of compound of formula (2) with compound of formula (3) is carried out in the presence of an aqueous solution of sodium or potassium hydroxide, especially sodium hydroxide, and in the presence of a phase transfer catalyst of formula (4a), wherein R2 is C1-C4alkyl, especially butyl, and Hal' is chloride or bromide. After the reaction is completed the desired product can be separated, for example by filtration. If desired the product can be washed and subsequently be dried. Furthermore, the present invention is directed to a process for the preparation of a compound of formula in the presence of an aqueous base and a phase transfer catalyst to give the compound of formula wherein R1 is as defined above, and converting the compound of formula (1) to the compound of formula (5). As given above, the compounds of formula (1) are suitable intermediates for the preparation of Venlafaxine which is represented by the formula (5). As to R1 the above definitions and preferences apply. Most preferably, R1 is methyl. The conversion of the compound of formula (1) to the compound of formula (5) can be carried out according to known processes. Such a conversion and the reaction conditions to be used are described in US-A-4,535,186 (see especially Examples 2 and 3). In general, a method for such a conversion comprises the following steps: step A) can be carried put by catalytic hydrogenation (for example rhodium on alumina). Step B) can be carried out by reaction of the compound of formula (6) with formaldehyde, formic acid in a large excess of water. According to the present invention the intermediates of formula (1) can be obtained in high yields. The use of organic solvents and also of expensive bases can be dispensed with. Furthermore, the reaction can be easily controlled. The following examples illustrate the invention: Examples 1 to 8: (4-methoxyphenyl)acetonitrile and cyclohexanone are mixed and warmed/cooled to the desired temperature given in the following table. The phase transfer catalyst (PTC) and the aqueous base solution are added under vigorous stirring. The resulting reaction mixture is stirred for the time given in the following table, and subsequently filtered. The solid product is washed with water and dried in vacuum. • The reaction conditions are given in the following table. The equivalents given in the table are molar equivalents relative to the molar amount of (4-methoxyphenyl)acetonitrile TBAB = tetrabutylammonium bromide TBACI = tetrabutylammonium chloride Claims 1. A process for the preparation of a compound of formula wherein Ri is unsubstituted or substituted alkyl, comprising reacting a compound of formula in the presence of an aqueous base and a phase transfer catalyst. 2. A process according to claim 1, wherein R1 is C1-C4alkyl which is unsubstituted or substituted by phenyl. 3. A process according to claim 1 or 2, wherein R1 is methyl. 4. A process according to any of claims 1 to 3 wherein the aqueous base is an aqueous solution of an alkali hydroxide. 5. A process according to any of claims 1 to 4 wherein the aqueous base is an aqueous solution of sodium hydroxide or potassium hydroxide, preferably sodium hydroxide. 6. A process according to any of claims 1 to 5. wherein the phase transfer catalyst is a quaternary ammonium salt, a quaternary phosphonium salt or a crown ether. 7. A process according to any of claims 1 to 6. wherein the phase transfer catalyst is a compound of formula N(R2)/ Hal' (4a) or P(R3)/ Haf (4b), wherein each of R2 and R3 independently from the other substituents R2 and R3 is phenyl or alkyl which is unsubstituted or substituted by phenyl, and Hal" is a halide. 8. A process according to claim 7, wherein R2 and R3 are CrCiealkyI, benzyl or phenyl. 9. A process according to claim 7 or 8, wherein the phase transfer catalyst is a compound of formula (4a) and R2 is C1-C4alkyl, preferably butyl. 10. A process according to any of claims 7 to 9, wherein Hal' is fluoride, chloride or bromide, preferably chloride or bromide. 11. A process according to any of claims 1 to 10, wherein the reaction of compound of formula (2) with compound of formula (3) is carried out at a temperature of 0 to 60°C. 12. A process according to any of claims 1 to 11, wherein the reaction of compound of formula (2) with compound of formula (3) is carried out in the presence of an aqueous solution of sodium or potassium hydroxide and in the presence of a phase transfer catalyst of formula (4a), wherein R2 is C1-C4alkyl, preferably butyl, and Hal' is chloride or bromide. 13. A process for the preparation of a compound pf formula wherein R1 is unsubstituted or substituted alkyl, in tine presence of an aqueous base and a phase transfer catalyst to give the compound of formula wherein R1 is as defined above, and converting the compound of formula (1) to the compound of formula (5), 14. A process according to claim 13 wherein R1 is' methyl. 15. A process for the preparation of a compound substantially as herein described and exemplified. Dated this 7 day of March 2003

Documents:

347-chenp-2003-abstract.pdf

347-chenp-2003-assignement.pdf

347-chenp-2003-claims duplicate.pdf

347-chenp-2003-claims original.pdf

347-chenp-2003-correspondnece-others.pdf

347-chenp-2003-correspondnece-po.pdf

347-chenp-2003-description(complete) duplicate.pdf

347-chenp-2003-description(complete) original.pdf

347-chenp-2003-form 1.pdf

347-chenp-2003-form 26.pdf

347-chenp-2003-form 3.pdf

347-chenp-2003-form 5.pdf

347-chenp-2003-other documents.pdf

347-chenp-2003-pct.pdf

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