FI92689B - Process for the preparation of cis-dihydronopol - Google Patents

Abstract

A process for the preparation of cis-dihydronopol and its esters is described. Corresponding esters of (-)-nopol are hydrogenated stereoselectively by heterogeneous hydrogenation in the presence of a platinum or platinum oxide catalyst or of a ruthenium/carbon catalyst and the cis-dihydronopyl esters obtained are, if desired, converted into the corresponding alcohol.

Description

92689

Process for the preparation of cis-dihydronopoly Förfarande för framställning av cis-dihydronopol

The present invention relates to a process for cis-dihydronopol {= 2 - [(1S, 2S, 5S) -6,6-dimethylbicyclo [3.1.1] hept-2-yl] -eth

noli} and its lower carboxylic acid or benzoic acid esters. The dihydronopol is a 2- (6,6-dimethylbicyclo [3.1.1] hept-2-yl) ethanol of formula A

Vch9-ch, -oh vy 2 2 (a) CH3A — v cA3

Formula A contains chiral centers at positions 1, 2, and 5 of the ring backbone, each of which may be in either the R or S configuration so that these compounds may exist in many stereoisomeric forms.

Dihydronopoly is obtained as a derivative of a natural terpene, i.e. (-) - B-pinene [= (1S, 5S) -6,6-dimethyl-2-methylenebicyclo- [3.1.1] heptane] of formula B

f-vV-S (B, CH, where the chiral centers at the 1- and 5-positions are in the S-configuration. Similarly, the centers at the 1- and 5-positions of the dihydronopol are in the S-configuration, while the center at the 2-position may be Thus, the 2-position substituent is located in the cis-dihydronopolis at the cis position relative to the dimethylmethylene bridge and in the trans-dihydronopolis at the trans position relative to that bridge.

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According to French patent publication 2097031, dihydronopoly is known as an intermediate in the processes used for the preparation of pharmacologically active substances. For example, dihydronopoly is an intermediate in a process for the preparation of commercially available anticonvulsant pinaverium bromide [trade name DicetelR = N- (2-bromo-4,5-dimethoxybenzyl) -N- {2- [2 - ((IS, 5S) -6,6-dimethylbicyclo [3.1.1] hept-2-yl) -ethoxy] -ethyl} -morpholinium bromide]. To prepare pinaverium bromide, the dihydronopol is first reacted with morpholinoethyl chloride according to the method described in French Patent 2097031 and the resulting reaction product is further reacted with the method described in French Patent 2097032 or German Patent 2137988-5-brom.

According to French patent publication 2079031, the dihydronopol is obtained by hydrogenation of a double bond obtained from (-) - O-pinene and, for example, from J. Am. Chem. Soc. , 68 (1946), page 638, in a known (-) - nopol {= 2 - [(1R, 5S) -6,6-dimethylbicyclo [3.1.1] hept-2-en-2-yl] -ethanol}, which is a terpene alcohol of formula III

\ ch2-ch2-oh dll) This hydrogenation is carried out at temperatures in the range from 80 to 100 ° C in the presence of a platinum oxide catalyst (Adams catalyst) or also Raney nickel or Urushibara nickel. If desired, a solvent such as alcohol may be used.

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Upon hydrogenation of the (-) -pole to the dihydronopoly by the method described in said French patent, a mixture of stereoisomers is formed which contains most of the cis compound but also a significant proportion of the trans compound. When the dihydronopol is further converted to pharmacologically active compounds, the configuration in the ring backbone is retained, whereby the pharmacologically active end products are also mixtures of stereoisomers. If stereoisomerically pure compounds are desired, they must first be enriched and then isolated from the mixture by complicated and high-loss separation methods known per se.

In the manufacture of medicines, the aim is usually to use the purest possible active ingredients as well as sterically uniform active ingredients.

Accordingly, it is an object of the present invention to provide an improved process for the diastereose-selective preparation of cis-dihydronopol and its esters.

Within the scope of the invention, a process was found which can prepare cis-dihydronopol in good yields with high diastereoselectivity.

Accordingly, the invention relates to a process for the preparation of 2 - [(1S, 2S, 5S) -6,6-dimethylbicyclo [3.1.1] hept-2-yl] -ethanol derivatives of the general formula I / (I) ^ Vch2-ch2-or CH5 \ ^ CH3 4 92689

wherein the 2-position substituent is in the cis position relative to the dimethylmethylene bridge and R represents hydrogen or an acyl group COR1, wherein R1 is lower alkyl or phenyl optionally substituted by lower alkyl, lower alkoxy or hydroxy, this method being characterized in that the general formula II

(-K \\ - CHoCH «-OCO 2 yy 2 2 CH, / \ ^ ch3 wherein R 1 is as defined above, the ester is hydrogenated with hydrogen in the presence of a solid platinum or platinum oxide catalyst or a ruthenium / carbon catalyst to give the general formula Compounds according to Ia

Vch2-ch2-ccor1 (Ia) 5 ch3 wherein R1 is as defined above, after which, if desired, the COR1 group is removed from the compounds of formula Ia.

If the substituent R of the compounds of the formula I contains lower alkyl groups, they can be straight-chain or branched and preferably contain 1 to 4, in particular 1 or 2, carbon atoms. In particular, esters of lower carboxylic acids of the formula II, for example acetate or propionate, preferably acetate, can be used in the process according to the invention.

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The process of the invention comprises heterogeneous hydrogenation in the presence of a solid platinum or platinum oxide catalyst or a ruthenium / carbon catalyst. As the catalyst, for example, a conventional, commercially available platinum oxide having a platinum content of 79 to 85% and known, for example, as a "Adams catalyst" can be used. As the platinum catalysts, supported catalysts containing platinum on an organic or inorganic support or platinum black can be used. As the support material for the supported catalysts, materials known per se for the production of catalyst supports can be used. Suitable are, for example, activated carbon or also ceramic materials, for example alumina, silica and aluminosilicate. The platinum content of such supported catalysts can be in the range from 1 to 10, in particular from 4 to 6% by weight, based on the total weight of the catalyst. For example, platinum / carbon catalysts with a platinum content of 3-7% by weight have proven to be preferred. Also suitable are supported catalysts comprising ruthenium on the surface of the carbon support. For example, ruthenium / carbon catalysts with a ruthenium content of 1-10, preferably 3-7% by weight have proven to be preferred. The amount of catalyst used may vary depending on the type of catalyst used, the hydrogen pressure used and the reaction time. When the hydrogen pressure used is about 80 bar, satisfactory yields are generally obtained in 3-4 hours with platinum oxide using a catalyst amount of 1-15 g of platinum oxide per mole of hydrogenated starting material of the formula II and with a platinum / carbon catalyst such that the amount of catalyst corresponds to 0.1 to 1 g of platinum metal per mole of the starting compound. When ruthenium / carbon catalysts are used and when operating, for example, at a hydrogen pressure of 95 bar, satisfactory yields are generally obtained in 4-5 hours, the amount of catalyst corresponding to 0.2-1 g of ruthenium per mole of starting compound.

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The hydrogenation can be carried out without a solvent or in the presence of an organic solvent. Suitable organic solvents include aliphatic, cycloaliphatic or aromatic hydrocarbons such as n-hexane, cyclohexane or toluene, open-chain or cyclic ethers such as tetrahydrofuran, lower alkyl esters or lower alkyl esters of lower carboxylic acids or lower acetones such as, for example, ethyl esters of acetic acid, , Alcohols having 1 to 4 carbon atoms, especially 1 to 3 carbon atoms, especially ethanol or isopropanol.

The hydrogenation can be carried out at a hydrogen pressure in the range from 1 to 100 bar. Suitably a higher pressure is used, for example so that the hydrogen pressure is in the range from 3 to 95, preferably from 60 to 95 bar. Platinum or platinum oxide catalysts can generally be operated at lower hydrogen pressures than ruthenium catalysts.

The hydrogenation can be carried out at room temperature or at slightly elevated temperatures, for example at temperatures in the range from 10 to 60 ° C, preferably from 15 to 50 ° C, in particular from 18 to 25 ° C. The reaction time varies depending on the hydrogen pressure used, the temperature, the type of catalyst and the amount of catalyst. It can be, for example, 1-10 hours. However, the starting compounds have generally reacted completely after as little as 3-7 hours.

The cleavage of the esters of the formula Ia to the alcohol can be carried out solvolytically in a manner known per se. The esters of formula Ia may be cleaved for ester decomposition under conventional conditions, for example by basic hydrolysis or alcoholysis. For example, the esters may be treated in the presence of an inorganic or organic base with water or a lower alcohol or a mixture thereof at temperatures between room temperature and the boiling point of the reaction mixture. Suitable inorganic bases are, for example, alkali metal hydroxides or carbonates or alkaline earth metal hydroxides or carbonates, in particular potassium or sodium hydroxide. The crude product obtained after hydrogenation and separation of the catalyst and solvent can be cleaved directly without first purification or isolation.

The hydrogenation product obtained after the separation of the catalyst and the solvent or the crude compound of the formula I obtained from the subsequent ester decomposition can, if necessary, be purified in a manner known per se, for example by distillation or chromatography.

Compared to the hitherto known process for the preparation of dihydronopol, the process according to the invention has the advantage that the starting compounds react rapidly and completely at temperatures already at room temperature, so that the cis compounds of the formula I are obtained in good yields with high stereoselectivity. The overall yields of the compounds of the formula I are generally more than 90%, for example 95-100%. The cis-dihydronopole prepared according to the invention generally contains less than 0.4%, often less than 0.2%, of trans-dihydronopoly as an impurity.

The starting esters of the formula II can be prepared in a manner known per se by acylation of an alcohol of the formula III.

\ cH2-CH2-0H (!!!)

For example, an alcohol of formula III may be reacted to form an ester under conventional conditions with a reactive acid derivative of formula IV R 1 -CO-X (IV), 92689 wherein R 1 is as defined above and X is halogen or an OCOR 1 residue where R 1 is as defined above. adequate. The acetate of the formula I can be obtained in a manner known per se directly from the (-) - 3-pinene of the formula B by reacting it with formaldehyde in glacial acetic acid.

The following examples further illustrate the invention without, however, limiting it.

Example 1

Preparation of cis-dihydronopol A) To a solution of 100 g (0.6 mol) of (-) - nopole and 130 ml (0.93 mol) of triethylamine in 600 ml of dichloromethane was slowly added dropwise at 5-10 ° C. 50 g (0.64 mol) of acetyl chloride under ice-cooling. The reaction mixture was then stirred for an additional 20 minutes at 5-10 ° C. It was then stirred without cooling until the reaction mixture had warmed to room temperature. To work up the reaction mixture, it was stirred in 800 ml of ice water. The organic phase was separated, the aqueous phase was washed with 100 ml of dichloromethane and the combined organic phases were washed neutral with saturated aqueous sodium hydrogen carbonate solution and dried over sodium sulfate. After distilling off the dichloromethane, 130 g of crude product remained, from which (-) - naphthyl acetate was isolated by fractional distillation. In this way, 98 g of (-) - nopyl acetate having a boiling point of 117-119 ° C (10 mm Hg) and a refractive index of n2 ° D = 1.4722 were obtained.

B) 20 g of (-) - nopyl acetate were dissolved at room temperature in 150 ml of ethyl acetate. The solution was transferred to a 1 liter autoclave containing 1 g of powdered platinum oxide catalyst (Adams catalyst, 82% platinum content).

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The reaction mixture was purged in an autoclave several times with nitrogen. The hydrogenation was then carried out at room temperature, 80 bar under nitrogen pressure. Hydrogen consumption ceased after about 3 hours.

Hydrogen was released from the autoclave and the autoclave was purged several times with nitrogen. The catalyst was then removed from the reaction solution by filtration and the solution was evaporated on a rotary evaporator. In this way, 20.3 g of crude cis-dihydronopyl acetate with a boiling point of 126-128 ° C (10 mm Hg) and a refractive index n2 = D = 1.4685 were obtained.

The crude cis-dihydronopyl acetate obtained was analyzed by gas chromatography (GC) to determine the relationship between purity and isomers.

The gas chromatographic assay used Sichromat-type gas chromatography comprising a Siemens flame ionization detector (FID) and a 30 m long quartz column column with an inner diameter of 0.32 mm (WCOT 123-1334 type "fused silica" column from J). & W Scientific), and whose stationary phase was of immobilized silicone material (= Durabond DB 624, from J & W Scientific). Helium with an outlet pressure of 0.6 bar and a flow rate of 30 cm / s was used as the carrier gas. The injection temperature used was 200 ° C, the column temperature program was 180 ° C to 230 ° C with a heating rate of 4 ° C / min and the detection temperature was 250 ° C. To perform the analysis, 0.5 μΐ of a 1% methanol solution of the test substance was injected into the gas chromatograph at a split ratio of 1:25. The analysis gave the following results: Total dihydronopyl acetate content: 98.1% cis / trans ratio: 99.8 / 0.2 Non-hydrogenated starting material content: 0.3%.

92689 C) 20 g of the crude cis-dihydronopyl acetate obtained in B) were added dropwise to a solution of 6.5 g of potassium hydroxide in 30 ml of methanol, and the reaction mixture was stirred for 2 hours under a nitrogen atmosphere at room temperature. 150 ml of ether were then added to the reaction mixture and the resulting mixture was washed three times with 75 ml of water each time. The combined washings were extracted with 75 mL of ether and the combined ether phases were dried over sodium sulfate. After removal of the ether by distillation, 15.1 g of cis-dihydronopol were obtained as a colorless oil with a boiling point of 123-125 ° C (10 mm Hg) and a refractive index of n2SD = 1.4882.

Example 2

Preparation of cis-dihydronopyl acetate 2.5 kg of (-) - nopyl acetate prepared analogously to Example IA) were dissolved in 15 l of ethyl acetate and the solution was placed in a 30 l autoclave. A slurry containing 90 g of a powdered platinum oxide catalyst (Adams catalyst) in 3 L of ethyl acetate was then added to the autoclave. The autoclave was rinsed several times with nitrogen. Hydrogen at a pressure of 95 bar was then introduced into the autoclave and the hydrogenation was carried out at this pressure for 135 minutes at a temperature of 13-23 ° C. The hydrogen was then released. from the autoclave and the autoclave was purged several times with nitrogen. The reaction mixture was removed from the autoclave and the catalyst was filtered off. The autoclave was rinsed with 3 L of ethyl acetate and the catalyst was also washed with this rinse. The combined filtrates were evaporated. In this way, 2,456 kg of crude cis-dihydronopyl acetate [boiling point 126-128 ° C (10 mm Hg), refractive index n2SD * 1, 4688] were obtained, the composition of which was as follows from the gas chromatographic determination described in Example IB: Π 92689 cis-dihydronopyl acetate 98, 7% trans-dihydronopyl acetate 0, 2% unreacted (-) - nopyl acetate 0, 1% cis-dihydronopoly 0, 2% other volatile components 0, 8%.

Based on this, the total yield of dihydronopyl acetate was 2.429 kg, or 96.2%, with a cis / trans ratio of 99, 8/0, 2.

The product was converted to the cis-dihydronopoly [b.p. 123-125 ° C (10 mm Hg)] as described in Example 1C).

Example 3

Preparation of cis-dihydronopyl acetate 150 g of (-) - nopyl acetate and 5 g of Adams catalyst were placed in an autoclave without solvent and the hydrogenation was carried out as described in Example 1. Hydrogen consumption ceased after about 6 hours. To work up the hydrogenation product, after purging with nitrogen, it was diluted with 0.5 L of ethyl acetate and the catalyst was removed by filtration. The catalyst was washed once more with 50 ml of ethyl acetate. The filtrate and washings were combined and the solvent was removed by distillation. In this way, 151 g of crude cis-dihydronophylacetate with a refractive index n2SD = 1.4689 were obtained.

GC analysis: total dihydronopyl acetate content: 98.6% cis / trans ratio: quantification of cis compound * non-hydrogenated starting compound content: 0.2%.

[* quantitative: the trans isomer was not detected by the GC analysis method described above. ]

Example 4

Preparation of cis-dihydronopyl acetate 12 92689 20 g of (-) - nopyl acetate were dissolved in 150 ml of ethanol at room temperature. This solution and 1 g of powdered ruthenium / carbon catalyst (ruthenium content 5%) were placed in a 1 L autoclave. The reaction mixture in the autoclave was purged several times with nitrogen. The hydrogenation was then carried out at room temperature, 95 bar hydrogen pressure for 7 hours. The hydrogen was then released from the autoclave and the autoclave was purged several times with nitrogen. The catalyst was separated from the reaction solution by filtration and the solution was evaporated on a rotary evaporator. In this way, 20.3 g of crude cis-dihydronopyl acetate with a boiling point of 126-128 ° C (10 mm Hg) and a refractive index n2SD = 1.4682 were obtained.

GC analysis: total dihydronopyl acetate content: 98.9% cis / trans ratio: 99.6 / 0.4 content of non-hydrogenated starting compound: 0.2%

Example 5

Preparation of cis-dihydronopyl acetate (-) - Nopyl acetate was hydrogenated analogously to the methods described in Examples 1-4, under the reaction conditions shown in the following table, at room temperature. The hydrogenation was stopped after 3 hours at the latest, the catalyst was removed by filtration, the solution was evaporated and the resulting hydrogenation product was analyzed by gas chromatography as described in Example IB. In addition to the reaction conditions, Table I shows the conversion of the starting product after a reaction time of 3 hours and the cis / trans ratio in the final product.

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Table I

e.g. catalyst H2 pressure, conversion, cis / trans. q / 20 g ly. 1 2 solvent_bar__ ratio3 5a4 lg PtCl 2 ethyl acetate 95-100 99.99, 83: 0.17 5b lg PtO 2 ethyl acetate 70 99.7 99.80: 0.20 5c lg PtO 2 ethyl acetate 50 99.9 99.82: 0, 18 5d lg PtQz ethyl acetate 30 85, 1 99.78: 0.22 5e lg PtO2 n-hexane 80 86.2 99.88: 0, 12 5f lg PtO2 toluene 80 90, 1 99, 77: 0, 23 5g lg PtO2 tetrahydrofuran 80 97, 1 quantum at5 ci s 5h 0, 67g PtCl2 - 80 89.7 - "- 5i lg PtO2 acetone 80 92.2 -" - 5j lg PtO2 C2H = OH 80 98.7 - "- 5k lg PtO2 CH3QH 80 97.4 - "- 51 lg PtO2 (CH3) 2CHOH 80 99.8 -" - 5m lg PtO2 C2H5OH 80 86.4 99, 66: 0, 34 5n6 lg PtO2 ethyl acetate 95 99, 7 99.85: 0 , 15 50 lg Ru / C (5%) C 2 H = OH 95 95, 3 99, 59: 0.41 g / 20 g of starting compound 2 conversion = reacted starting compound,% 3 cis / trans ratio in the final product 4 * reaction time only 2, 5 h 5 = quantitative cis = no trans product could be detected, i.e. trans << 0.1% 6 reaction time only 1 h 7 reaction time 4h, reaction temperature 50 'C.

Example 6

Preparation of cis-dihydronopyl propionate 14 9Z & 9A) In analogy to Example IA, 75 g of (-) - napole and 97 ml of triethylamine were dissolved in 500 ml of dichloromethane and this solution was reacted with propionic acid chloride (40.9 g). The reaction mixture was worked up as described in Example IA. After fractional distillation twice, 54.6 g of nopyl propionate with a boiling point of 136-138 ° C (10 mm Hg) were obtained.

B) 20 g of nopyl propionate were hydrogenated by the method described in Example IB at room temperature, 80 bar under hydrogen pressure, in ethanol, in the presence of an Adams catalyst. The hydrogenation was stopped after 3 hours and the reaction mixture was worked up as described in Example IB. In this way, 20.5 g of crude cis-dihydronopylpropionate with a refractive index n2 ° D = 1.4668 were obtained.

The obtained crude cis-dihydronopyl propionate was analyzed by gas chromatography analogously to the method described in Example IB, but using a 25 m long column with an internal diameter of 0.32 mm ("fused silica" WCOT 7745 type column from Chrompack) containing stationary phase type CP-Sil 43CB polysilicon material (0.2 microns, organic residues: 50% methyl, 25% cyanopropyl, 25% phenyl groups) from Chrompack. The injector temperature was 200 ° C, the column 1 temperature program was 160 -> 220 ° C at 3 ° C / min. The following results were obtained from the analysis: total dihydronopylpropionate content: 94.1% cis / trans ratio: 99, 9: 0, 1 non-hydrogenated starting compound content: 1.3%.

The obtained crude cis-dihydronopyl propionate can be converted to cis-dihydronopoly as described in Example 1C.

Example 7

Attenuation of cis-dihydronopyl benzoate (92) As described in Example IA, 49.9 g of (-) - nopole and 65 ml of triethylamine were dissolved in 350 ml of dichloromethane and the solution was reacted with benzoyl chloride (43.3 g). with. The reaction mixture was then worked up analogously as described in Example IA. After fractional distillation, 51.1 g of nopyl benzoate having a boiling point of 179-182 ° C (1 mm Hg) were obtained.

B) 26 g of nopyl benzoate were dissolved in 150 ml of ethanol as described in Example IB and the solution was hydrogenated at room temperature, 80 bar under hydrogen pressure in the presence of Adams catalyst (1 g). The hydrogenation was stopped after 8 hours and the reaction mixture was worked up analogously as described in Example IB. This gave 25.4 g of crude cis-dihydronophylbenzoate with a refractive index of naoo = 1.5295. It was analyzed by gas chromatography as described in Example 6B.

Gas chromatographic analysis: total dihydronopyl benzoate content: 92.4% cis / trans ratio: 99, 8: 0, 2 non-hydrogenated starting compound content: 3.3%.

The resulting crude cis-dihydronopyl benzoate can be converted to the cis-dihydronopoly as described in Example 1C.

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Claims (3)

A process for the preparation of 2 - [(IS, 2S, 5S) -6,6-dimethyl-bicyclo [3. 1. 1] hept-2-yl] ethanol derivative of the general formula I AAch 2 -ch 2 -or (i) CH 3 + CH 5 where R is hydrogen or an acyl group COR , lower alkoxy or tai hydroxy-substituted phenyl, characterized in that an ester of the general formula II a ruthenium / carbon catalyst, obtaining compounds of the general formula Ia K> CH 92689 Process according to claim 1, characterized in that the COR COR group is acetyl. 3. A process according to claim 1, characterized in that the hydrogenation is carried out at temperatures between 15 and 50 ° C, preferably between 18 and 25 ° C.