WO2006122977A2

WO2006122977A2 - PROCESS FOR PREPARING 3α(β)-7α(β)-DIHYDROXY-6α(β)-ALKYL-5β-CHOLANIC ACID

Info

Publication number: WO2006122977A2
Application number: PCT/EP2006/062446
Authority: WO
Inventors: Massimo Ferrari; Roberto Pellicciari
Original assignee: Erregierre S.P.A.
Priority date: 2005-05-19
Filing date: 2006-05-19
Publication date: 2006-11-23
Also published as: AU2006248906B2; ES2338698T3; WO2006122977A3; DK1888614T3; ATE453657T1; EP1888614B1; EP1888614A2; CA2608539C; US7994352B2; DE602006011457D1; US20080214515A1; AU2006248906A1; CN101203526A; CA2608539A1; JP2008540612A; ITMI20050912A1; CN101203526B; JP5127700B2

Abstract

Process for preparing 3α-7α(β)-dihydroxy-6α(β)-alkyl-5β-cholanic acid (I) in which R is a linear or branched C1-C5 alkyl and the relative intermediates 3α-hydroxy-6β-alkyl-7-keto-5β-cholanic (VIII) and 3α-hydroxy-6α-alkyl-7-keto-5β-cholanic (IX).

Description

PROCESS FOR PREPARING 3α(β)-7α(β)-DIHYDROXY-6α(β)-ALKYL-5β- CHOLANIC ACID.

Description FIELD OF THE INVENTION

The present invention concerns a process for the preparation of 3α-7α(β)- dihydroxy-6α(β)-alkyl-5β-cholanic acids.

STATE OF THE ART

Farnesoid X receptors (FXR) are initially orphan nuclear receptors, identified for the first time from a cDNA library of rat liver (B.M Forman et al., Ce//. 81:687-693

(1995)), they are members of the family of nuclear receptors of ligand-activated transcription factors, including the receptors of steroid, retinoid and thyroid hormones (DJ. Mangelsdorf , et al, Ce//.83:841 -850(1995)).

Several bile acids of a natural type bind together and activate FXR in physiological concentrations as described in WO00/37077 and in particular chenodeoxycholic, deoxycholic, litocholic acids and the relative conjugates with taurine and glycine.

It is also believed that FXR are involved in the regulation of the homeostasis of bile acids and of cholesterol.

WO02/072598 describes 3-α,7-α-dihydroxy-6α-alkyl-(allyl)-5β-cholanic acids with general formula (A)

(A) in which R' is ethyl, propyl or allyl which are also agonists of Farnesoid X receptors. In particular the compound with formula (I) in which R' = ethyl is two magnitude order more powerful than chenodeoxycholic acid, the most powerful natural FXR agonist

The compounds with general formula (A), used in particular to increase HDL cholesterol, to lower triglycerides for the prevention and treatment of hepatic diseases of cholestatic origin, are prepared with a process comprising the following stages: i) reacting 3-α-hydroxy-7-keto-5β-cholanic acid of formula (II)

(II) with dihydro pyrane to obtain the corresponding 3-α-tetrahydropyranyloxy-7-keto- 5β-cholanic acid of formula (B)

(B)

ii) reacting the compound (B) with an alkyl bromide with formula R¹Br in which R' has the meanings indicated above, to obtain the compound (C)

(C) iii) reducing the compound (C) with sodium borohydride to give (D),

(D) iv) hydrolysing (D) to give the compounds (A).

Even though this process comprises only few stages, it presents a series of drawbacks.

Firstly, in all stages the reaction products are purified on a chromatographic column, namely a very expensive separation method that cannot be realised on an industrial scale.

Moreover the reaction yield in stage (ii) is extremely low (12-13%), with a considerable decrease in the global yield, which is lower than 3.5%.

Moreover, still in this stage, hexamethylenphosphonamide is used as a reactant, which is a known cancerogenic agent

SUMMARY OF THE INVENTION

The Applicant has now found a process which makes it possible to obtain both compounds with general formula (I)

(I)

in which the dashed bond ( — ) in position 6 and 7 indicates that the substituent may be in position α or β chosen in the class consisting of: i) 3-α,7-α-dihydroxy-6-α-alkyl-5β-cholanic acid with general formula (IA)

(IA)

ii) 3-α,7-α-dihydroxy-6-β-alkyl-5β-cholanic acid with general formula (IB)

(IB) iii) 3-α,7-β-dihydroxy-6-α-alkyl-5β-choIanic acid with general formula (IC)

(IC) in which R is a linear or branched C-₁-C₅ alkyl, comprising the following stages a) esterifiying 3α-hydroxy-7-keto-5β-cholanic acid (II)

(II) in methanol in an acidic environment to obtain methyl 3α-hydroxy-7-keto- cholanate (III),

(III) b) Silylating methyl 3α-hydroxy-7-keto-5β-cholanate (III) with trimethylchlorosilane to obtain the corresponding 3-α-trimethylsiloxy-7-keto-5β-cholanate (IV),

(IV) c) Silylating methyl 3α-trimethyisiloxy-7-keto-5β-cholanate (IV) obtained in stage (b) with trimethylchlorosilane in the presence of a strong base to obtain methyl 3α-,7α-di-trimethylsiloxy-6-en-5β-cholanate (V),

d) Reacting methyl 3α-,7α-di-trimethylsiloxy-6-en-5β-cholanate (V) with the aldehyde R-CHO in which R has the meanings indicated above and a Lewis acid, to obtain methyl 3α-hydroxy-6-alkylidene-7-keto-5β-cholanate (Vl),

(Vl) e) hydrolysis of methyl 3α-hydroxy-6-alkylidene-7-keto-5β-cholanate to 3α- hydroxy-6-alkylidene-7-keto-5β-colanic acid (VII),

(VII)

f) hydrogenating 3α-hydroxy-6-alkylidene-7-keto-5β-cholanic in an aqueous alkaline environment with Pd/C to 3α-hydroxy-6β-alkyl-7-keto-5β-cholanic acid

(VIII) g) optionally heat treating the intermediate (VIII) in an aqueous alkaline environment to obtain the corresponding 3α-hydroxy-6α-alkyl-7-keto-5β- cholanic (IX)

(IX) h) reducing the ketonic group in position (7) to 7-hydroxy group of the intermediate (VIII) or (IX) according to one of the following alternative operating conditions: h') reducing 3α-hydroxy-6α-alkyl-7-keto-5β-cholanic compound (IX) with metallic hydride to 3α-,7α-di-hydroxy-6α-alkyl -5β-cholanic acid (IA), h") reducing 3α-hydroxy-6α-aikyl-7-keto-5β-cholanic compound (IX) in the presence of sodium and alcohol and obtaining 3α-,7β-di-hydroxy-6α-alkyl-5β- colanic (IC); h"^!) reducing 3α-hydroxy-6β-alkyl-7-keto-5β-cholanic (VIII) in the presence of a metallic hydride to 3α-,7α-di-hydroxy-6β-alkyl-5β-cholanic (IB).

The process according to the present invention in particular for obtaining 3α-,7α- di-hydroxy-6α-alkyl-5β-cholanic acids (IA) presents considerable advantages with respect to the known process described above. In fact, although it contemplates a larger number of stages, it allows the product with formula (I) to be obtained with decidedly satisfactory global yields (24.6%), in any case decidedly higher than those of the known process. Moreover, the intermediates do not need to be purified by chromatography and the use of reagents, such as the highly toxic hexamethylenphosphonamide is avoided. Lastly, with the process of the present invention and as shown above, it is possible to obtain the new compounds of formula (IB) and (IC) which may be used a hepatoprotectors in particular for the treatment and prevention of hepatic diseases of cholestatic origin. The present invention therefore concerns pharmaceutical compositions containing as active principle at least one of the acids (I-B) and (I-C) and the respective pharmaceutically acceptable salts in combination with suitable excipients and/or diluents. DETAILED DESCRIPTION OF THE INVENTION The esterifying reaction of the 3α-hydroxy-7-keto-5β-cholanic acid (II) in stage (a) of the process of the present invention is preferably carried out at a temperature between 30 and 60⁰C in an acid environment, in which the acid is preferably methanesulphonic acid. The silylating reaction of the hydroxy group in position 3α- of methyl 3α-hydroxy-7- keto-5β-cholanate contemplated in stage (b) of the process of the present invention is preferably carried out in an apolar solvent, more preferably an aromatic solvent, even more preferably toluene, in the presence of a hydrogen ion acceptor preferably consisting of a tertiary amine, of aliphatic, alicyclic or heteroaromatic type, even more preferably said tertiary amine is triethylamine. According to a particularly preferred embodiment, before being used in stage (c), methyl 3-α-trimethylsiloxy-7-keto-5β-cholanate is not isolated and purified, but on the contrary in this stage the oily residue is used which is obtained after evaporating the reaction solvent from which the salts have previously been removed by water extraction. The subsequent silylation of the ketonic group in position 7 contemplated in stage (c) of the process of the present invention is preferably carried out using as the strong base an alkaline amide obtained from ammonia or an alkaline amide of a secondary aliphatic amine. According to a particularly preferred solution, lithium diisopropylamide is used as the strong base. This reaction is preferably carried out in a polar aprotic solvent, and even more preferably said solvent is tetrahydrofuran. According to a preferred embodiment the product obtained in stage (c), before being used in the following stage (d), is not isolated and purified, but on the contrary in this case too the oily residue is used obtained by evaporating the reaction solvent from which the salts have been previously extracted with water. Stage (d) is preferably carried out in an apolar solvent, preferably chosen from alkyl halide, and even more preferably this solvent is methylene chloride. Stage (d) is preferably carried out using boron trifluoride etherate as the Lewis acid at a temperature between -90 and -60⁰C for a period of 2 to 4 hours in the presence of the aldehyde R-CHO in which R has the desired meanings. Subsequently, the reaction mixture is reacted at a temperature between 0 and 35°C for a period of 1 to 6 hours.

In this case too, before being used in the following stage (e), the product obtained in stage (d) is not isolated and purified, but the oily residue is used which was obtained after evaporating the reaction solvent, from which the salts and water- soluble components have been removed with water extraction.

Stage (e) is preferably carried out in an alcoholic solvent, preferably methanol, in the presence of an alkaline hydroxide, even more preferably said alkaline hydroxide is an aqueous solution of 30% sodium hydroxide. The temperature is preferably comprised between 20 and 60⁰C. Stage (e) reaction product is preferably isolated after acidification, by crystallisation with an organic solvent, preferably chosen from ethyl acetate and acetone, possibly in the presence of water.

The hydrogenation reaction contemplated in stage (f) is preferably carried out in an aqueous environment in the presence of an aqueous solution of sodium hydroxide with pressure between 1 and 3 atmospheres. When the process of the present invention contemplates stage (g), in particular when the compounds with general formula (IA) or (IC) have to be prepared, this stage is preferably carried out directly on the reaction mixture coming from hydrogenation reaction and is preferably carried by heating said reaction at a temperature between 95 and 105⁰C for a few hours to allow the epimerization of the 6-β-ethyl group into 6-α- ethyl. The reaction product coming from stage (f) or possible stage (g) is isolated from the reaction mixture preferably using the following operating conditions.

1) adding the aqueous solution, from which the catalyst has been removed by filtration is acidified preferably with 85% phosphoric acid, 2) ethyl acetate is added to the mixture obtained in stage (1) and the whole is heated at a temperature between 40 and 70⁰C. 3) this is then cooled to a temperature between 0 and 30°C and the precipitate obtained is filtered and subsequently dried. When the reduction of stage (h) is carried out according to the operative conditions contemplated in stage (h^J) to obtain the compound with formula (IA) or according to the operative conditions contemplated in stage (h"') to obtain the compound with formula (IB) of the process of the present invention, the metallic hydride is preferably sodium borohydride and the reduction reaction is carried out in an alkaline aqueous solution. The reaction is preferably carried out at a temperature between 70 and 105⁰C for 1 hour.

Instead, when the reduction of stage (h) is carried out according to the operating conditions contemplated in stage (h") it is preferably carried out in linear or branched Ci-C₅ alcohol, even more preferably in sec-butyl alcohol, at the solvent reflux temperature. The product obtained from stage (h^J) or (h'") is preferably isolated according to the following operative conditions:

1') adding a water immiscible solvent to the reaction mixture, preferably an apolar solvent such as methylene chloride, and acidifying the mixture preferably with phosphoric acid, 2') stirring and allowing to rest to the mixture obtained thereafter eliminating the aqueous phase,

3') extracting the product from the organic phase with water and ammonia,

4') adding phosphoric acid to the aqueous phase thus obtained and stirring the whole for a few hours at a temperature between 20 and 50⁰C,

5') recovering and drying the precipitated product by filtration. The process of the present invention is suitable in particular for the preparation of compounds with formula (I) in which R is preferably methyl. Some examples of preparation according to the process of the invention of the compounds with formula (I) and in particular (IA), (IB) and (IC) in cui R = methyl are given for illustrative purposes, but not limitative.

EXAMPLE 1- PROCESS FOR PREPARING 3α-,7α-DIHYDROXY-6α-ETHYL-5β- CHOLANIC ACID of formula (IA) in which R =methyl a) preparation of methyl 3-α-hvdroxy-7-keto-5β-cholanate (III). 17.0kg of 3-α-hydroxy-7-keto-5β-cholanic acid, 68kg of methanol and 0.17kg of methansulphonic acid are charged into a reactor. The reaction mixture is then heated to 30-60⁰C for 1 hour and 25.5kg of demineralised water are added. The mixture obtained is then stirred, cooled to 20-25⁰C until a good precipitation is obtained, then cooled further to 0-15⁰C. The precipitate is filtered and washed with a mixture of water and methanol and further dried in a oven at about 40⁰C. 15kg of methyl 3α-hydroxy-7-keto-5β-cholanate (III) is thus obtained. Stoichiometric yield 85.2%. b) preparation of methyl 3α-trimethylsiloxy-7-keto-53-cholanate (IV)₁

15.0kg of methyl 3α-hydroxy-7-keto-5β-cholanate, 45kg of toluene, 7.5kg of triethylamine, 7.5kg of trimethylchlorosilane are charged into a reactor. The mixture is heated to 70-80⁰C and is kept under stirring at that temperature for about 1 hour, then 37.5kg of water are added and the mixture is stirred at 15-20⁰C. The lower aqueous phase is then separated and eliminated. The organic phase is concentrated until an oily residue is obtained, which 15 kg of tetrahydrofuran are added to.

The solution thus obtained containing methyl 3α-trimethylsiloxy-7-keto-5β- cholanate (IV) is used in the following stage (c). c) preparation of methyl 3α-, 7α-di-trimethylsililoxy-5β-cholanate (V)

30kg of tetrahydrofuran are loaded in a reaction, then the mixture is brought to a temperature between -90° and -60⁰C, 9.8kg of 100% lithium diisopropylamide and 9.3kg of trimethylchlorosilane are added, and the whole solution of tetrahydrofuran prepared in (b) and containing methyl 3-α-trimethylsiloxy-7-keto- 5β-cholanate is poured. The mixture is then stirred for about 1 hour at a temperature between-60 and -90⁰C for 1 hour. A solution of 4.50kg of sodium bicarbonate and 60 kg of water is then poured and the mixture is stirred at 0-10⁰C₁ and the lower aqueous phase is separated and eliminated. The lower phase is then concentrated until an oily residue is obtained, which 45.0Kg of methylene chloride- are added to.

The solution of methyl 3α-,7α-di-trimethylsililoxy-5β-cholanate thus obtained is sent to the next stage (d). d) preparation of methyl 3α-hydroxy-6-ethyliden-7-keto -5β-cholanate (Vl) in which R = Methyl

The whole solution of methyl 3α,7-α-di-trimethylsililoxy-5β-cholanate in methylene chloride coming from the preceding example in charged into a reactor and cooled to -90/-60⁰C 1.97kg of acetaldehyde and 5.5kg of boron trifluoride etherate are then added. The reaction mixture is kept under stirring at the above temperature for 2/4 hours. After that it is heated to 30-35⁰C and kept at that temperature for about 2/4 hours. Then 60kg of water are added. The mixture obtained is stirred and the aqueous phase is separated. The solution thus obtained containing methyl 3α-hydroxy-6-ethyliden-7-keto-5β-cholanate is sent to the next stage. e) preparation of 3α-hydroxy-6-ethyliden-7-keto-5β-cholanic (VII) acid in which R =CH₃,

The solution of methyl 3-α-hydroxy-6-ethyliden-7-keto-5β-cholanate in methylene chloride obtained in the previous stage is charged into a reactor. The solvent is then removed by distillation until an oily residue is obtained, which 15 kg of methanol are added to.

The reaction mixture is then heated to 45-50° C and 7.5kg of 30% sodium hydroxide are poured , and the reaction mixture is kept at the above temperature for about 1 hour. Then 30kg of water are added. 45.0kg of methylene chloride and 7.5kg of 85% phosphoric acid are subsequently added. The lower organic phase is separated and the aqueous phase is eliminated subsequently. The solvent is removed from the organic phase by distillation until a pasty residue is obtained. About 37.5kg of ethyl acetate are added to the residue and the mixture is heated to 65-75°C, then cooled to 10-35°C. The precipitate obtained, filtered and washed with ethyl acetate, is dried. 8.0kg of 3-α-hydroxy-6-ethyliden-7-keto-5β-cholanic acid are obtained, with a stoichiometric yield of 51.8% calculated on methyl 3-α-hydroxy-7-keto-5β- cholanate. f) preparation of 3-α-hvdroxy-6-β-ethyl-7-keto-5β-cholanic acid (IX) in which R=CHg)

8.0 kg of 3-α-hydroxy-6-α-ethyliden-7-keto-5β-cholanic acid, 48.0kg of water, 5.1kg of 30% sodium hydroxide, 0.80kg of 5% Palladium/Carbon are charged into a reactor. The reaction mixture is hydrogenated at a pressure between 1 and 3 atmospheres, until the hydrogen absorption is no longer noted. (g) preparation of 3α-hydroxy -6-α-ethyl-7-keto-5β-cholanic acid (IX)

At the end of the reaction the mixture is heated to 95-105⁰C and is kept at that temperature for a few hours to allow the 3α-hydroxy-6-β-ethyl-7-keto-5β-choIanic acid (VIII) to convert into the corresponding epimer of the desired 3α-hydroxy -6- α-ethyi-7-keto-5β-cholanic acid (IX). The suspension is filtered, and the catalyst is recovered. 5.1 kg of 85% phosphoric acid 9.6 kg of ethyl acetate are added to the filtered solution, and the reaction mixture is heated to a temperature between 40 and 70⁰C. It is cooled to a temperature between 0 and 30⁰C and the precipitate is recovered by filtration. After washing with ethyl acetate, the precipitate is dried in a oven at 65°C. 5.0kg of 3α-hydroxy-6α-ethyl-7-keto-β-cholanic acid are obtained. Stoichiometric yield: 62.2%.

21

Analysis

3-α-hvdroxy-6-α-ethyl-7-keto-5β-cholanic (IX)

C₂₆H₄₂O₄ m.p. 185-188⁰C

The ¹H-NMR analysis carried out with the instrument Bruker DRX-ADVANCE- 400Mhz, dissolving the specimen in CD₃OD, gave the following results:

0.62 ppm (s, 3H of methyl C₁₈); 0.76ppm, J=7.4Hz (t, 3H of methyl C₂₆); 0.89ppm

J= 6.5Hz, (d, 3H₁ of methyl C₂i); 1.18ppm (s, 3H₁ of methyl C₁₉), 2.21 ppm (m, 2H,

-CH₂- of C₂₃); 2.50ppm, J=11.17Hz (ψt, CH on C₈); 2.85ppm J =13Hz and J=

5.4Hz (dd 1 H in C₆), 3.50ppm (m, CH on C₃). The ¹³C NMR analysis carried out with the instrument Bruker DRX-ADVANCE-

200Mhz, dissolving the specimen to be analysed in a mixture of CD₃OD and

CDCI₃, gave the following results:

212.82ppm (C₇); 179.44ppm (C₂₄), 71.26ppm (C₃), 54.77ppm (C₁₇), 51.98ppm

(C₁₄),18.84ppm (C₂₁), 18.34ppm (C₂₆), 12.09ppm (C₁₈). h¹) preparation of 3α,7α-dihvdroxy-6α-ethyl-5β-cholanic acid with formula (I) in which R= methyl.

5.0kg of 3α-hydroxy-6α-ethyl-7-keto-β-choianic acid, 5.0kg of water, 2.50 kg of sodium hydroxide are loaded in a reactor. The mixture is then heated to 70-105⁰C and a mixture of sodium borohydride dissolved in 2.50 kg of water is poured, the mixture is then kept warm for 1 hour, cooled to room temperature, and 10.0kg of demineralised water, 15.0kg of methylene chloride and 3.00kg of 85% phosphoric acid are added. The mixture is stirred, the lower organic phase is separated and the aqueous phase is removed.

Crystallization of the crude product is obtained by cooling the organic solution. This product is dissolved in 50kg of demineralised water and 1.10kg of 30% ammonia. The mixture is then stirred until a complete solution is obtained, and keeping the mixture at 20-50⁰C, 1.50kg of phosphoric acid is poured. The precipitated mixture is stirred, always at a temperature between 20 and 50⁰C, then the precipitate is recovered by filtration, washed with water and dried. 4.50 kg of 3α-,7α-di-hydroxy-6α-ethyl-5β-cholanic acid of formula (I) are obtained, in which R= methyl. Stoichiometric yield: 89.6%. EXAMPLE 2 preparation of 3-α,7α-di-hydroxy-6β-ethyi-5β-cholanic acid of formula (IB) in which R = methyl.

The 3-α-hydroxy-6β-ethyl-7keto-5β-cholanic acid of formula (VIII) prepared as described in example 1 stages (a)-(f) and isolated as described in stage (g), is reduced using the same operating conditions described in example 1 stage (h'). 3- α,7α-di-hydroxy-6β-ethyl-5β-cholanic acid of formula (IB) is then obtained in which R = methyl. Analysis

21

3-α,7-α-di-hvdroxy-6-β-ethyl-5β-cholanic (IB)

C₂₆H₄₄O₄ m.p. 115-118°C

The ¹H-NMR analysis carried out with the instrument Bruker DRX-ADVANCE-

400MHz, dissolving the specimen in CD₃OD, gave the following results:

0.70ppm (s, 3H of methyl Ci₈); 0.95ppm (s, 3JH, of methyl Ci₉), LOOppm, J=7,65Hz (t, 3H of methyl C₂₆); 1.45ppm J= 3.5Hz, (d, 3H, of methyl C₂₁);

2.25 ppm (m, 2H, -CH₂- of C₂₃); 3.40ppm (m, CH on C₃), 3.62ppm (m, CH on C₇).

The ¹³C NMR analysis carried out with the instrument Bruker DRX-ADVANCE-

200Mhz, dissolving the specimen to be analysed in a mixture of CD₃OD and

CDCI₃, gave the following results: 177.91 ppm (C₂₄), 72.18ppm (C₃), 71.68ppm (C₇); 55.79ppm (C₁₇), 50.83ppm

(Ci₄),18.17ppm (C₂₁), 14ppm (C₂₆), 11.60ppm (C₁₈).

EXAMPLE 3 preparation of 3-αJβ-di-hvdroxy-6α-ethyl-5β-cholanic acid with formula (IC) in which R= methyl

According to the operative conditions described in example 1 stages (a)-(g), the intermediate (IX) is prepared, to which is added until complete solution sec-butyl alcohol in which sodium has previously been dissolved in molar quantities with respect to the compound (IX) between 3:1 and 3:2. 3-α,7β-di-hydroxy-6α-ethyI-5β- cholanic acid with formula (IC) is obtained in which R= methyl

Analysis

3-α,7-β-di-hvdroxy-6-α-ethyl-5β-cholanic (IC)

C₂₆H₄₄O₄ m.p. 217-219°C

21

The ¹H-NMR analysis carried out with the instrument Bruker DRX-ADVANCE-

400MHz, dissolving the specimen in CD₃OD, gave the following results: 0.56ppm (s, 3H of methyl Ci₈) ; 0.73ppm, J=7.4Hz (t, 3H of methyl C₂₆); 0.81 ppm

(s, 3H₁ of methyl Ci₉), 0.82ppm J= 4.60Hz, (d, 3H, of methyl C₂₁); 2.21 ppm (m, 2H,

-CH₂- of C₂₃), 3.80ppm (br, O-H of hydroxyl on C3, on C₇ and of carboxyl C₂₄);

3.10ppm (m, CH on C₇); 3.44ppm (m, CH_ on C₃).

The ¹³C NMR analysis carried out with the instrument Bruker DRX-ADVANCE- 200MHz, dissolving the specimen to be analysed in a mixture of CD₃OD and

CDCI₃, gave the following results:

179ppm (C₂₄), 75.65ppm (C₇), 71.87ppm (C₃), 56ppm (Ci₇), 55ppm (C₁₄), 18.4ppm

(C₂₁), 12.24ppm (C₂₆), 11.20ppm (C₁₈).

Claims

1. Process for preparing 3α-7α(β)-dihydroxy-6α(β)-alkyl-5β-cho!anic acids with general formula (I)

(I) in which the dashed bond ( — ) in position 6 and 7 indicates that the substituent may be in position α or β, chosen in the class consisting of: i) 3-α,7-α-dihydroxy-6-α-alkyl-5β-cholanic acid with general formula (IA)

(IA) ii) 3-α,7-α-dihydroxy-6-β-alkyl-5β-cholanic acid with general formula (IB)

(IB) iii) 3-α,7-β-dihydroxy-6-α-alkyl-5β-cholanic acid with general formula (IC)

(IC) in which R is a linear or branched C₁-C₅ alkyl comprising: a) esterifying 3α-hydroxy-7-keto-5β-cholanic acid (II)

(II) in methanol in an acidic environment to obtain methyl 3α-hydroxy-7-keto-5β- cholanate (III),

(III) b) silylating methyl 3-α-hydroxy-7-keto-5β-cholanate (III) with trimethylchlorosilane to obtain the corresponding methyl 3α-trimethylsiloxy-7-keto-5β-cholanate (IV),

(IV) c) silylating methyl 3α-trimethylsiloxy-7-keto-5β-cholanate (IV) obtained in stage (b) in the presence of a strong base and trimethylchlorosilane to obtain methyl 3α-, 7α-di-trimethylsiloxy-6-en-5β-cholanate (V),

(V) d) reacting methyl 3-α-,7α-ditrimethylsiloxy-6-en-5β-cholanate (V) with the aldehyde R-CHO in which R has the meanings indicated above and a Lewis acid, to obtain methyl 3-α-hydroxy-6-alkylidene-7-keto-5β-cholanate (Vl),

(Vl) e) hydrolysing methyl 3-α-hydroxy-6-ethyliden-7-keto-5β-cholanate (Vl) to 3-α- hydroxy-6-alkylidene-7-keto-5β-colanic acid (VII),

(VII) f) hydrogenating S-α-hydroxy-δ-alkylidene-T-keto-δβ-cholanic in an aqueous alkaline environment with Pd/C to 3-α-hydroxy-6β-alkyl-7-keto-5β-cholanic acid (VIII)

(VIII) g) possibly heat treating the intermediate (VIII) in an aqueous alkaline environment to obtain the corresponding 3α-hydroxy-6α-alkyl-7-keto-5β-cholanic (IX)

(IX) h) reducing the ketonic group in position (7) to 7-hydroxy group of the intermediate (VIII) or (IX) according to one of the following alternative operating conditions. h') reducing 3α-hydroxy-6α-alkyl-7-keto-5β-cholanic acid (IX) with metallic hydride to 3α-,7α-di-hydroxy-6α-alkyl-5β-cholanic acid (IA), h") reducing 3α-hydroxy-6α-alkyl-7-keto-5β-cholanic acid (IX) in the presence of metallic sodium and alcohol and obtaining of 3α-,7β-di-hydroxy-6α-alkyl-5β- cholanic (IC); h'") reducing 3α-hydroxy-6β-alkyl-7-keto-5β-cholanic acid (VIII) in the presence of a metallic hydride to 3α-,7α-di-hydroxy-6β-alkyl-5β-cholanic (IB).

2. Process according to claim 1 , characterised in that the esterification of stage (a) is carried out at a temperature between 30 and 60⁰C in an acid environment.

3. Process according to claim 2, characterised in that said acid is methanesulphonic acid. 4. Process according to any one of the claims 1-3, characterised in that the silylation in stage (b) is carried out in an apolar solvent in the presence of a hydrogen ion acceptor.

5. Process according to claim 4, characterised in that said apolar solvent is an aromatic solvent. 6. Process according to claim 5 characterised in that said aromatic solvent is toluene.

7. Process according to claim 4-6, characterised in that said hydrogen ion acceptor is a tertiary amine of an aliphatic, alicyclic or heteroaromatic type

8. Process according to claim 7, characterised in that said tertiary amine is triethylamine.

9. Process according to any one of the claims 1-8, characterised in that the methyl 3-α-trimethylsiloxy-7-keto-5β-cholanate (IV) obtained from stage (b) is not isolated and purified before being used in stage (c).

10. Process according to claim 9, characterised in that in stage (c), as the reagent (IV), the oily residue is used which is obtained after evaporation of the reaction solvent from which the salts have previously been eliminated by extraction with water.

11. Process according to any one of the claims 1-10, characterised in that the subsequent silylation of the ketonic group in stage (c) is carried out using as strong base an alkaline amide obtained from ammonia or an alkaline amide obtained from a secondary amine.

12. Process according to claim 11, characterised in that said alkaline amide is lithium diisopropylamide.

13. Process according to any one of the claims 1-12, characterised in that said stage (c) is carried out in a polar aprotic solvent.

14. Process according to claim 13, characterised in that said polar aprotic solvent is tetrahydrofuran.

15. Process according to any one of the claims 1-14, characterised in that methyl 3-α,7-α-ditrimethyIsiloxy-6-en-5β-cholanate (V) obtained in stage (c) is not isolated and purified before being used in stage (d).

16. Process according to claim 15, characterised in that as reagent (V) the oily residue is used obtained after evaporating the reaction solvent from which the salts have previously been removed by extraction with water.

17. Process according to any one of the claims 1-16, characterised in that stage (d) is carried out in an apolar solvent.

18. Process according to claim 17, characterised in that said apolar solvent is an alkyl halide.

19. Process according to any one of the claims 17 and 18 in which said solvent is methylene chloride.

20. Process according to any one of the claims 1-19, characterised in that the Lewis acid is boron trifluoride etherate. 21. Process according to claim 20 characterised in that stage (d) is carried out according to the following operating conditions: the reaction mixture is cooled to a temperature between -90⁰C -60⁰C and for a period of 2 to 4 hours, then the reaction mixture is kept at a temperature between 0 and 35°C for a period of 1 to 6 hours. 22. Process according to any one of the claims 1-21 , characterised in that methyl 3-α-hydroxy-6-alkylidene-7-keto-5β-cholanate (Vl) obtained in stage (d), is not isolated and purified before being used in the following stage (e).

23. Process according to claim 22, characterised in that the hydrolysis in stage (e) is carried out using as reagent (Vl) the oily residue obtained after evaporation of the reaction solvent from which the salts and water-soluble components have been eliminated by extraction with water.

24. Process according to any one of the claims 1-23, characterised in that the hydrolysis reaction in stage (e) is carried out in an alcoholic solvent, in the presence of an aqueous solution of an alkaline hydroxide. 25. Process according to claim 24. characterised in that said reaction is carried out at a temperature between 20 and 60⁰C.

26. Process according to any one of the claims 1-25, characterised in that the hydrogenation in stage (f) is carried out in an aqueous environment in the presence of an aqueous solution of sodium hydroxide at a pressure between 1 and 3 atmospheres. 27. Process according to any one of the claims 1-26, characterised in that, when it comprises stage (g), that stage is carried out directly on the mixture of the reaction obtained from stage (f).

28. Process according to claim 27, characterised in that said stage (g) is carried out at a temperature between 95 and 105⁰C for a few hours. 29. Process according to any one of the claims 1-28, characterised in that the reaction product obtained from stage (f), when that process does not contemplate stage (g), or from stage (g), is isolated from the reaction mixture according to the following operating conditions:

1) acidifying the aqueous solution from which the catalyst has been removed by filtration,

2) adding ethyl acetate to the mixture obtained in stage (1) and heating the whole to a temperature between 40 and 70⁰C.

3) cooling to a temperature between 0 and 30⁰C, filtering and drying the precipitate obtained. 30. Process according to any one of the claims 1-29, characterised in that when the reduction of stage (h) is carried out according to the operating conditions contemplated in stage (h¹) or according to the operating conditions (h'") the metallic hydride is sodium borohydride in an aqueous solution in which an alkaline hydroxide has been dissolved. 31. Process according to claim 30, characterised in that said alkaline hydroxide consists of a solution of 30% sodium hydroxide.

32. Process according to claim 30-31 , characterised in that the reaction is carried out at a temperature between 70 and 105⁰C for 1 hour.

33. Process according to claim 30-32, characterised in that the product obtained is isolated according to the following operating conditions:

1') adding a water immiscible solvent to the reaction mixture and acidifying the mixture with phosphoric acid, 2') stirring and allowing to rest the mixture obtained and eliminating the aqueous phase,

3') extracting the product from the organic phase with water and ammonia,

4') adding phosphoric acid to the aqueous phase thus obtained and stirring the whole at a temperature between 20 and 5O⁰C,

5') recovering and drying the precipitated product by filtration.

34. Process according to any one of the claims 1-29, characterised in that when stage (h) is carried out according to the operative conditions (h") the reduction reaction is carried out in linear or branched alcohol Ci-C₅, at the solvent reflux temperature.

35. Process according to claim 34, characterised in that said alcohol is sec-butyl alcohol.

36. Process according to any one of the claims 1-35 in which R is preferably methyl.

37. Process according to any one of the claims 1-30 for preparing 3-α,7-α- dihydroxy-6α-ethyl-5β-cholanic acid.

38. 3-α-hydroxy-6-β-alky-7-keto-5β-cholanic acid (VIII)

(VIII) in which R is a linear or branched Ci-Cs alkyl. (IX)39. 3-α-hydroxy-6-α-alkyl-7-keto-5β-cholanic acid(IX)

(IX) in which R is a linear or branched C₁-C₅ alkyl. 40. 3-α,7-α-dihydroxy-6-β-alkyl-5β-cholanic of general formula (IB)

(IB) in which R is a linear or branched C₁-C₅ alkyl. 41. 3-α,7-β-dihydroxy-6-α-alkyl-5β-cholanic of general formula (IC)

(IC) in which R is a linear or branched C₁-C₅ alkyl.

42. Pharmaceutical composition containing as active ingredient at least one of the 3-α,7-α-dihydroxy-6-β-alkyl-5β-cholanic acids according to claim 40 or the respective pharmaceutically acceptable salts in combination with suitable excipients and/or diluents.

43. Pharmaceutical composition containing as active ingredient at least one of the 3-α,7-β-dihydroxy-6-α-alkyl-5β-cholanic acids according to claim 41 and the respective pharmaceutically acceptable salts in combination with suitable excipients and/or diluents.