It has been surprisingly found that the preparation of (R)-5-(2-(2-(2-ethoxy phenoxy)ethylamino)-1-propyl)-2-methoxybenzenesulphonamide from (R)-5-(2-amino-1-propyl)-2-methoxybenzenesulphonamide (2) and 1-(2-bromoethoxy)-2-ethoxybenzene (3) may be successfully accomplished without the need for the addition of any base by carrying out the reaction in the presence of a molar excess of the non-chiral reagent, 1-(2-bromoethoxy)-2-ethoxybenzene (3).
It has been found that in the presence of a molar excess of the non-chiral intermediate compound, 1-(2-bromoethoxy)-2-ethoxybenzene (3), the reaction equilibrium is moved towards the formation of tamsulosin even without the presence of an additional base.
Preferred solvents are lower alkyl alcohols, more preferred is methanol.
The excess of the reagent (3) over the reagent (2) is effective above the ratios of about 1.2:1 and may be increased to about 5:1, preferably to about 3:1. More preferred ratio is from about 1.5:1 to about 2:1, most preferred from about 1.7:1 to about 1.9:1.
The process for the production of tamsulosin according to the present invention allows the provision of a good yield of the crude product at a good level of purity. The product isolated directly from the reaction conversion may comprise about 75% to about 90% of tamsulosin hydrochloride. It has been surprisingly found that the expected overalkylation occurs only to a limited extent, such that the production process of the present invention provides a crude product of tamsulosin hydrochloride in which the contents of any one of the overalkylated products, e.g. N-(2-(2-ethoxyphenoxy)ethyl)-5-(2-(2-(2-ethoxyphenoxy)ethylamino)-1 -propyl)-2-methoxybenzenesulphonamide (5) or 5-(2-(bis-(2-(2-ethoxyphenoxy)ethyl)amino)-1-propyl)-2-methoxybenzenesulphonamide (4) or the excessed 1-(2-bromoethoxy)-2-ethoxybenzene (3) does not exceed 6%.
Tamsulosin hydrochloride can be obtained by treating tamsulosin base with ethanolic HCl.
The crude tamsulosin hydrochloride according to the present invention may comprise no more than 5% w/w, preferably no more than 3% w/w, of N-(2-(2-ethoxyphenoxy)ethyl)-5-(2-(2-(2-ethoxyphenoxy)ethylamino)-1-propyl)-2-methoxy benzenesulphonamide (5), no more than 6% w/w, preferably no more than 5% w/w, of 5-(2-(bis-(2-(2-ethoxyphenoxy)ethyl)amino)-1-propyl)-2-methoxybenzene sulphonamide (4), no more than 2% w/w, preferably no more than 1% w/w, of (R)-5-(2-amino-1-propyl)-2-methoxybenzenesulphonamide (2) and no more than 2% w/w, preferably no more than 1% w/w, of 1,2-bis(2-ethoxyphenoxy)ethane (6).
The contents of the overalkylated products in the crude product may be minimised whilst at the same time maintaining a high yield for the desired tamsulosin hydrochloride by adjusting the extent of the excess of the reagent (3). Preferably a ratio of reagents (2) to (3) of between about 1:1.5 to about 1:2, more preferably about 1:1.75 can be used. At this ratio, the yield of tamsulosin is still not essentially decreased but the contents of overalkylated products (4) and (5) may be reduced below 2%.
The crude product, obtained directly from the reaction process, may be additionally purified to yield tamsulosin having a pharmaceutically acceptable purity by using conventional purification methods, such as thermal recrystallisation whereby a solution of the product is heated to a higher temperature and then the mixture is cooled in order to recrystallise the product. Tamsulosin hydrochloride can be recrystallised by thermal recrystallisation from alcohols whereby a part of impurities is eliminated from the product.
Surprisingly, it has been found that for the purification of crude tamsulosin hydrochloride a high level of elimination of impurities is achieved where a mixture of ethanol and methanol is used as the recrystallisation solvent.
It has been found that a mixture with a higher proportion of ethanol removes better non-polar impurities whereas mixtures with a lower proportion of ethanol are more effective for removal of less polar overalkylated products. Ratios of methanol to ethanol of around 1:1 are preferred for the recrystallisation of tamsulosin hydrochloride. Ratios of about 1:1 have been shown to approximately evenly remove all impurities to a sufficiently low level and therefore has been identified as preferable taking into consideration also a better yield because the recovery of the product is somewhat greater with mixtures richer in ethanol.
According to another embodiment of the present invention, there is provided a process for the purification of tamsulosin hydrochloride comprising recrystallising tamsulosin from a solution in methanol or ethanol or a mixture of ethanol and methanol, by thermal recrystallisation. Preferably a mixture of methanol and ethanol is used in a ratio of methanol to ethanol of from about 7:3 to about 3:7, more preferably about 1:1 is used.
The process of the present invention allows for the production of tamsulosin hydrochloride of a high purity and at a good yield, even from starting materials which are not purified to a low content of impurities. For instance it has been found that although the starting compound, 1-(2-bromoethoxy)-2-ethoxybenzene (3), can contain up to about 8% of 1,2-bis(2-ethoxyphenoxy)ethane (6), according to the method of this invention, there is not more than 0.2% of said impurity in the final product.
After purification of tamsulosin hydrochloride by recrystallisation from an ethanol/methanol mixture, tamsulosin hydrochloride having higher than 99.5% purity, even higher than 99.8% purity, may be obtained from, for example, tamsulosin hydrochloride having a purity of as low as 90%, even as low as 86%, after only two crystallisations.
Purification of tamsulosin hydrochloride by thermal recrystallisation according to the present invention allows the production of a purified product comprising as low as 0.08% w/w, even 0.06 % w/w of N,SO2N-dialkylated products, i.e. N-(2-(2-ethoxyphenoxy)ethyl)-5-(2-(2-(2-ethoxyphenoxy)ethylamino)-1-propyl)-2-methoxy benzenesulphonamide (4) and less than 0.1% w/w of all overalkylated products.
The efficacy of purification in view of the invention enables that the process with an excess of the less expensive reagent (3) becomes an economical procedure for industrial production because in only two steps, a high quality pharmaceutical active substance can be obtained.
For the purification of crude tamsulosin hydrochloride to a high quality, it is preferable to carry out more than one, preferably two crystallisations. Where more than one crystallisation is effected, each crystallisation can be carried out in a different medium. Thus, for example, for somewhat poorer quality crude samples, it may be particularly effective to carry out the first crystallisation in the mixture of methanol to ethanol at a ratio of about 1:1 whereas the second one in a mixture with a higher proportion of methanol or in methanol alone.
The presence and contents of impurities have been proven with the standards of these compounds whereas by-products of the reactions, which are not simply available, are isolated from mother liquors by using preparative chromatography.
Tamsulosin hydrochloride obtained by the process according to the present invention is suitable for a pharmaceutical use in any pharmaceutical formulation whereby the crystals may be additionally milled to obtain particles of the size d(0.9) below 120 μm and d(0.5) below 50 μm.
Tamsulosin hydrochloride of the present invention in any pharmaceutical formulation can be then used for the treatment of benign prostatic hyperplasia.
The present invention is illustrated but in no way limited by the following examples:
10 g (41 mmol) of 5-((R)-2-amino-1-propyl)-2-methoxybenzenesulphonamide, 19 g (77 mmol) of 2-(2-ethoxyphenoxy)ethylbromide and 170 ml of methanol are heated under reflux for 43 hours. Methanol is evaporated under vacuum on a rotavapor at 60° C. To the residue, 170 ml of water and 130 ml of ethyl acetate are added and while cooling and stirring also 16 g of 50% aqueous sodium hydroxide. After separation of both phases, the water phase is extracted twice with 100 ml of ethyl acetate. Combined extracts are washed twice with 130 ml of water and evaporated in vacuo on a rotavapor at 60° C. The residue is dissolved in 100 ml of ethanol and while cooling and stirring, 7 ml of ethanolic hydrogene chloride solution (300 mg HCl/ml) is added. While cooling (0° C.), the mixture is stirred for 4 hours and the formed crude (−)-(R)-5-(2-(2-(2-ethoxyphenoxy)ethylamino)-1-propyl)-2-methoxy benzenesulphonamide hydrochloride (TH) is filtered, washed with 20 ml of cooled ethanol (of about 0° C.) and dried under vacuum at 40° C. 7.0 g of a crude product is obtained.
HPLC analysis:
200 g (0.82 mol) of 5-((R)-2-amino-1-propyl)-2-methoxybenzenesulphonamide, 350 g (1.43 mol) of 2-(2-ethoxyphenoxy)ethylbromide and 3.4 l of methanol are heated under reflux for 45 hours. Methanol is evaporated in vacuo on a rotavapor at 60° C. To the residue 3.4 l of water and 2.6 l of ethyl acetate are added and while cooling and stirring also 650 g of 50% aqueous sodium hydroxide. After separation of both phases, the water phase is extracted twice with 2 l of ethyl acetate. The combined extracts are washed twice with 2.6 l of water and evaporated in vacuo on a rotavapor at 60° C. The residue is dissolved in 2 l of ethanol and 140 ml of ethanolic hydrogen chloride solution (300 mg HCl/ml) is added while cooling and stirring. While cooling (0° C.) the mixture is stirred for 4 hours and the formed crude (−)-(R)-5-(2-(2-(2-ethoxyphenoxy)ethylamino)-1-propyl)-2-methoxybenzenesulphonamide hydrochloride (TH) is filtered, washed with 400 ml of cool ethanol and dried in vacuo at 40° C. 158.0 g of a crude product is obtained.
HPLC analysis:
10 g of (−)-(R)-5-(2-(2-(2-ethoxyphenoxy)ethylamino)-1-propyl)-2-methoxybenzene sulphonamide hydrochloride (TH) from Example 2 is recrystallised from mixtures of methanol and ethanol.
Analysis:
7.0 g of recrystallised (−)-(R)-5-(2-(2-(2-ethoxyphenoxy)ethylamino)-1-propyl)-2-methoxybenzenesulphonamide hydrochloride (TH) from Example 3 is recrystallised from mixtures of methanol and ethanol.
Analysis:
7.0 g of (−)-(R)-5-(2-(2-(2-ethoxyphenoxy)ethylamino)-1-propyl)-2-methoxybenzene sulphonamide hydrochloride (TH) from Example 1 is recrystallised from the 1:1 methanol/ethanol mixture, the product is dried at 40° C. in vacuo and recrystallised again from methanol. 4.61 g of the product is obtained. The product is milled using a hammer-type mill at 4800 rpm.
Analysis:
The filtrate obtained after filtration of the product from Example 2 from the methanol to ethanol ratio 50:50 is evaporated and the residue in 2-g-aliquots is applied onto the column 200×50 mm with the stationary phase Luna 1 μM, prep C18(2), and eluted with the mobile phase (5 ml/l triethylamine, pH up to 2.8 with orthophosphoric acid, 20% methanol) at a flow rate 150 ml/min. Two fractions of each batch are collected, the corresponding fractions from different batches are combined, methanol evaporated, desalted, concentrated and lyophilized. The solid fractions A and B in the quantitative ratio 1:1.5 are obtained.
Fraction A:
5-(2-(bis-(2-(2-ethoxyphenoxy)ethyl)amino)-1-propyl)-2-methoxybenzenesulphonamide (5)
Appearance: Hygroscopic white crystals.
MS: 573 (M+H)+
NMR (300 MHz, TMS, CD3OD); δ (ppm): 6.8-7.8 (11H, m, aromatic protons); 3.80-4.10 (8H, m, OCH2); 3.87 (8H, S, OCH3); 2.40-3.20 (7H, m, CH2N, CH2CHN); 1.30 (6H, t, OCH2CH3); 1.05 (3H, d, CHCH3).
Fraction B:
N-(2-(2-ethoxyphenoxy)ethyl)-5-(2-(2-(2-ethoxyphenoxy)ethylamino)-1-propyl)-2-methoxybenzenesulphonamide (6)
Appearance: White crystals.
MS: 573 (M+H)+
NMR (300 MHz, TMS, CD3OD); δ (ppm): 6.7-7.8 (11H, m, aromatic protons); 3.80-4.30 (8H, m, OCH2); 3.86 (8H, S, OCH3); 2.60-3.30 (7H, m, CH2N, CH2CHN); 1.35 and 1.38 (6H, t, t, OCH2CH3); 1.15 (3H, d, CHCH3).
Bis-(2-ethoxyphenoxy)ethane is isolated from a commercial raw material, 2-(2-ethoxyphenoxy)ethylbromide, by column chromatography on silica gel (ether: petroleum ether=1:2 v/v).
Number | Date | Country | Kind |
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P-200300319 | Dec 2003 | SI | national |
Filing Document | Filing Date | Country | Kind | 371c Date |
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PCT/SI04/00047 | 12/27/2004 | WO | 00 | 4/17/2007 |