The present invention relates to a process for preparing 17α-acetoxy-6-methylenepregn-4-ene-3,20-dione (4) as an intermediate, and to processes for preparing medroxyprogesterone acetate (1) (17α-acetoxy-6α-methylpregn-4-ene-3,20-dione) and megestrol acetate (2) (17α-acetoxy-6-methylpregna-4,6-diene-3,20-dione) via this intermediate (4).
DE 3004508 describes the direct 6-methylenation of 3-oxo-Δ4 steroids by means of a formaldehyde acetal in the presence of phosphorus oxychloride. EP 0326340, the closest prior art, describes the disadvantages of the direct of 6-methylenation and the advantages of the Mannich reaction to the 6-methylenation of androsta-4-ene-3,17-diones.
The subject-matter of the present invention differs from that of EP 0326340 in that the steroid to be 6-methylenated is 17α-acetoxypregn-4-ene-3,20-dione (by the 17-substituent).
It is therefore an object of the present invention to provide an alternative process for preparing 17α-acetoxy-6-methylenepregn-4-ene-3,20-dione (4) as an intermediate, and processes for preparing medroxyprogesterone acetate (1) (17α-acetoxy-6α-methylpregn-4-ene-3,20-dione) and megestrol acetate (2) (17α-acetoxy-6-methylpregna-4,6-diene-3,20-dione) via this intermediate (4).
The object is achieved by a process for preparing the 17α-acetoxy-6-methylenepregn-4-ene-3,20-dione intermediate (4)
The present invention further relates to a process for preparing 17α-acetoxy-6α-methylpregn-4-ene-3,20-dione (1),
from 17α-acetoxypregn-4-ene-3,20-dione of the formula (3), comprising steps a) and b), wherein, after step b), the compound of the formula (4) is hydrogenated in step c).
The present invention also relates to a process for preparing 17α-acetoxy-6-methyl-pregna-4,6-diene-3,20-dione (2)
comprising steps a) and b), wherein, after step b), the compound of the formula (4) is isomerized in step d).
Preference is given according to the present invention to dissolving or suspending the reagents in the Mannich reaction in ethylene glycol dimethyl ether or pure tetrahydrofuran. The solvents described in EP 0326340, for example dioxane, methanol, ethanol, are incapable of suppressing side reactions such as the bis-Mannich reaction ((3) is 2,6-dimethylenated) and the retro-Mannich reaction (the starting compound (3) is reformed). The by-products formed can be separated from the compounds (1) or (2) only with exceptional difficulty or only by complicated column chromatography.
The preferred procedure variant also has the advantage that it enables isolation and hence specific prepurification of the 6-methylamino compound formed in step a) as a precursor of the Hofmann elimination (in step b), which would otherwise not be possible with the solvents described in EP 0326340.
In the process according to the invention, the intermediate (4) without chromatographic purification already has a purity of at least 97.5%, in contrast to the qualities achievable in the known processes (DE 3004508, EP 0 326 340 A2) (purity below 95.5%). The higher purity of the intermediate (4) additionally has the effect that it can be fully hydrogenated to the compound (1) or isomerized to the compound (2) with significantly smaller amounts of catalyst, and that 17α-acetoxy-6α-methylpregn-4-ene-3,20-dione (1) and 17α-acetoxy-6-methylpregna-4,6-diene-3,20-dione (2) can be obtained in very high purity.
To perform the Mannich reaction (step a), it is typically possible to employ primary or secondary amines (Synthesis 1973, 703-775). Suitable amines are, for example, those of the formula (5),
in which R2 and R3 together are the —(CH2)2-Q-(CH2)2— moiety where Q is defined as a carbon-carbon bond, a methylene group or an oxygen atom, or in which R2 is an alkyl group having up to eight carbon atoms, a benzyl group or a phenyl radical optionally substituted by alkyl groups or alkoxy groups containing up to 4 carbon atoms and/or fluorine atoms or chlorine atoms, and R3 is as defined for R2 or represents a hydrogen atom.
In the Mannich reactions performed to date, the N-methylaniline was used as the amine component. However, other amines are also suitable, for example pyrrolidine, piperidine, morpholine, diethylamine, diisopropylamine or N-methylbenzylamine.
The Hofmann elimination (step b) is preferably performed in the presence of acids as catalysts (for example mineral acids, such as hydrogen chloride, sulphuric acid or phosphoric acid, or preferably strong organic acids such as trifluoroacetic acid, methanesulphonic acid or trifluoromethanesulphonic acid). In step b), preference is given to subjecting the isolated and optionally purified intermediate from step a) to the Hofmann elimination dissolved or suspended in ethylene glycol dimethyl ether or pure tetrahydrofuran.
The purity of the 6-methylene compound of the formula (4) is sufficiently high that, for the subsequent hydrogenation to the compound of the formula (1) or for the isomerization to the compound of the formula (2), compared to the Vilsmeier process, only very small amounts of catalyst (Pd/C) are required.
The intermediate of the formula (4) is hydrogenated to the compound of the formula (1) by hydrogen transfer from cyclohexene in the presence of a palladium/carbon catalyst (Chem. Soc., London; 1954, 3578f.). To perform the hydrogenation, the components are dissolved or suspended in a polar solvent, preferably ethanol. After the workup, 17α-acetoxy-6α-methylpregn-4-ene-3,20-dione of the formula (1) is obtained in good yield and in outstanding purity (reference is made to the content determination in Example 1 adduced below).
The intermediate of the formula (4) is isomerized in a similar manner to the hydrogenation, but in the presence of a catalytic amount of 4-methyl-1-cyclohexene instead of cyclohexene. After the workup, 17α-acetoxy-6-methylpregna-4,6-diene-3,20-dione of the formula (2) is obtained in good yield, and likewise satisfies very high purity requirements (reference is made to the content determination in Example 2 adduced below).
The process according to the invention allows medroxyprogesterone acetate (1) and megestrol acetate (2) to be prepared in a purity of ≧99.0%.
The working examples which follow serve to illustrate the process according to the invention.
Without further elaboration, it is believed that one skilled in the art can, using the preceding description, utilize the present invention to its fullest extent. The preceding preferred specific embodiments are, therefore, to be construed as merely illustrative, and not limitative of the remainder of the disclosure in any way whatsoever.
In the foregoing and in the examples, all temperatures are set forth uncorrected in degrees Celsius and, all parts and percentages are by weight, unless otherwise indicated.
The entire disclosures of all applications, patents and publications, cited herein and of corresponding U.S. Provisional Application Ser. No. 60/942,285, filed Jun. 6, 2007, are incorporated by reference herein.
The preceding examples can be repeated with similar success by substituting the generically or specifically described reactants and/or operating conditions of this invention for those used in the preceding examples.
From the foregoing description, one skilled in the art can easily ascertain the essential characteristics of this invention and, without departing from the spirit and scope thereof, can make various changes and modifications of the invention to adapt it to various usages and conditions.
This application claims the benefit of the filing date of U.S. Provisional Application Ser. No. 60/942,285, filed Jun. 6, 2007.
Number | Date | Country | |
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60942285 | Jun 2007 | US |