WO2007138440A1 - Process for the production of benzopyran-2-ol derivatives - Google Patents

Process for the production of benzopyran-2-ol derivatives Download PDF

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Publication number
WO2007138440A1
WO2007138440A1 PCT/IB2007/001379 IB2007001379W WO2007138440A1 WO 2007138440 A1 WO2007138440 A1 WO 2007138440A1 IB 2007001379 W IB2007001379 W IB 2007001379W WO 2007138440 A1 WO2007138440 A1 WO 2007138440A1
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Prior art keywords
compound
formula
secondary amine
acid
amine compound
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PCT/IB2007/001379
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French (fr)
Inventor
Jens Bertil Ahman
Barry Richard Dillon
Alan John Pettman
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Pfizer Limited
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Priority to DE602007009096T priority Critical patent/DE602007009096D1/en
Priority to CA2651978A priority patent/CA2651978C/en
Application filed by Pfizer Limited filed Critical Pfizer Limited
Priority to EP07734680A priority patent/EP2029567B1/en
Priority to AT07734680T priority patent/ATE480531T1/en
Priority to MX2008012976A priority patent/MX2008012976A/en
Priority to PL07734680T priority patent/PL2029567T3/en
Priority to US12/302,228 priority patent/US8067594B2/en
Priority to BRPI0712037-0A priority patent/BRPI0712037A2/en
Priority to NZ571988A priority patent/NZ571988A/en
Priority to KR1020087028577A priority patent/KR101087326B1/en
Priority to SI200730392T priority patent/SI2029567T1/en
Priority to DK07734680.7T priority patent/DK2029567T3/en
Priority to CN2007800191401A priority patent/CN101454304B/en
Priority to AU2007266761A priority patent/AU2007266761B2/en
Publication of WO2007138440A1 publication Critical patent/WO2007138440A1/en
Priority to IL194959A priority patent/IL194959A0/en
Priority to HK09111229.1A priority patent/HK1133425A1/en
Priority to IL220430A priority patent/IL220430A0/en

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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D311/00Heterocyclic compounds containing six-membered rings having one oxygen atom as the only hetero atom, condensed with other rings
    • C07D311/02Heterocyclic compounds containing six-membered rings having one oxygen atom as the only hetero atom, condensed with other rings ortho- or peri-condensed with carbocyclic rings or ring systems
    • C07D311/04Benzo[b]pyrans, not hydrogenated in the carbocyclic ring
    • C07D311/06Benzo[b]pyrans, not hydrogenated in the carbocyclic ring with oxygen or sulfur atoms directly attached in position 2
    • C07D311/20Benzo[b]pyrans, not hydrogenated in the carbocyclic ring with oxygen or sulfur atoms directly attached in position 2 hydrogenated in the hetero ring
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C213/00Preparation of compounds containing amino and hydroxy, amino and etherified hydroxy or amino and esterified hydroxy groups bound to the same carbon skeleton
    • C07C213/02Preparation of compounds containing amino and hydroxy, amino and etherified hydroxy or amino and esterified hydroxy groups bound to the same carbon skeleton by reactions involving the formation of amino groups from compounds containing hydroxy groups or etherified or esterified hydroxy groups
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C219/00Compounds containing amino and esterified hydroxy groups bound to the same carbon skeleton
    • C07C219/26Compounds containing amino and esterified hydroxy groups bound to the same carbon skeleton having esterified hydroxy groups bound to carbon atoms of at least one six-membered aromatic ring and amino groups bound to acyclic carbon atoms or to carbon atoms of rings other than six-membered aromatic rings of the same carbon skeleton
    • C07C219/28Compounds containing amino and esterified hydroxy groups bound to the same carbon skeleton having esterified hydroxy groups bound to carbon atoms of at least one six-membered aromatic ring and amino groups bound to acyclic carbon atoms or to carbon atoms of rings other than six-membered aromatic rings of the same carbon skeleton having amino groups bound to acyclic carbon atoms of the carbon skeleton
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C45/00Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds
    • C07C45/61Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by reactions not involving the formation of >C = O groups
    • C07C45/67Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by reactions not involving the formation of >C = O groups by isomerisation; by change of size of the carbon skeleton
    • C07C45/68Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by reactions not involving the formation of >C = O groups by isomerisation; by change of size of the carbon skeleton by increase in the number of carbon atoms
    • C07C45/69Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by reactions not involving the formation of >C = O groups by isomerisation; by change of size of the carbon skeleton by increase in the number of carbon atoms by addition to carbon-to-carbon double or triple bonds
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D311/00Heterocyclic compounds containing six-membered rings having one oxygen atom as the only hetero atom, condensed with other rings
    • C07D311/02Heterocyclic compounds containing six-membered rings having one oxygen atom as the only hetero atom, condensed with other rings ortho- or peri-condensed with carbocyclic rings or ring systems
    • C07D311/04Benzo[b]pyrans, not hydrogenated in the carbocyclic ring
    • C07D311/58Benzo[b]pyrans, not hydrogenated in the carbocyclic ring other than with oxygen or sulphur atoms in position 2 or 4

Definitions

  • the present invention relates to an improved process for the production of intermediates useful in the preparation of tolterodine, fesoterodine and other pharmaceutically useful compounds.
  • the invention also provides improved processes for the production of such pharmaceutically useful compounds using the intermediates.
  • WO 98/29402 discloses a process for the production of tolterodine which comprises condensing p-cresol (a) with cinnamic acid (b), followed by reduction of the resulting lactone (c) with a reducing agent, such as diisobutylaluminium hydride (DIBAL), sodium bis(2-methoxyethoxy)aluminium hydride or lithium txi-tert-butoxyaluminohydride, to give the corresponding benzopyran-2-ol compound (d).
  • DIBAL diisobutylaluminium hydride
  • DIBAL sodium bis(2-methoxyethoxy)aluminium hydride
  • lithium txi-tert-butoxyaluminohydride lithium txi-tert-butoxyaluminohydride
  • the benzopyran-2-ol compound (d) can then be converted to racemic tolterodine hydrochloride (e) by reductive amination with diisopropylamine, followed by addition of aqueous hydrochloric acid. Finally, tolterodine L-tartrate is formed by neutralisation of the hydrochloride salt (e) with NaOH/NaHCO 3 and subsequent resolution using L-tartaric acid. The process is shown in Scheme 1 below. DIBAL
  • WO 01/49649 describes the reductive amination of the enantiomers of compound (d) above to give tolterodine and its enantiomer.
  • the enantiomers of compound (d) are produced by enantioselective reactions. It also relates to the same processes applied to analogous compounds, in particular the analogue of tolterodine in which the methyl group in the phenolic ring is replaced with a 5 -hydroxy methyl group.
  • Jurd Journal of Heterocylic Chemistry, vol 28 (4), 1991, pp 983-986 describes the reaction of 3,4-methylenedioxyphenol, morpholine and cinnamaldehyde in methanol to produce 2-morpholinyl-4-phenylbenzopyrans.
  • Y is selected from CH 3 , CH 2 OH, CH 2 CH 2 OH, CH 2 Br and Br; comprising the steps of:
  • OX is hydroxy or 0 " M + , in which M + is a cation selected from Li + , Na + and K + , and Y is as defined above; with traMs-cinnamaldehyde (III), in the presence of a secondary amine compound; then
  • secondary amine compound we mean an organic compound which contains at least one secondary amine group, i.e. a compound of the formula:
  • R a and R b are not hydrogen.
  • R a and R b are each linked to the nitrogen atom by a CH 2 group, for example they are independently Ci -6 alkyl or together form a 4- or 5-membered alkyl chain in which one carbon atom is optionally replaced by O or N.
  • Preferred embodiments of the first aspect of the invention are those in which: (a) OX is hydroxy;
  • Y is CH 3 or CH 2 OH
  • the secondary amine compound contains two secondary amine groups, for example piperazine (this catalyst produces particularly high yields); (e) when the secondary amine compound contains two secondary amine groups, 0.5- 1.25 mole equivalents of the secondary amine compound are used in step (i); (f) alternatively, the secondary amine compound contains one secondary amine group, and more preferably the secondary amine compound is morpholine, dibutylamine, dibenzylamine, 1,1,3,3-tetramethylguanidine, diethylamine, diisopropylamine, piperidine or an N-(Ci -6 alkyl)piperazine.
  • 7V-methylpiperazine is particularly preferred because it produces good yields, the initial product [see formula (VI) below] is readily hydrolysed to the corresponding lactol compound of formula (I), and the crude compound of formula (I) has an improved purity which facilitates crystallization; (g) when the secondary amine compound contains one secondary amine group, 1-5, more preferably 1-2.5 mole equivalents of the secondary amine compound are used in step (i);
  • the acid used in step (ii) is aqueous hydrochloric acid (preferably no more than 2M concentration), although the following aqueous acids at similar concentrations also provide good results: citric acid, acetic acid, oxalic acid, trifluoroacetic acid, maleic acid, fumaric acid, salicyclic acid, traws-cinnamic acid, benzoic acid, camphor sulfonic acid and tosic acid;
  • step (i) the reaction of step (i) is carried out in an organic solvent selected from toluene, xylene, N-butyl acetate, t-amyl alcohol, dioxane and dibutyl ether, most preferably toluene (which produces particularly high yields);
  • step (j) the reaction of step (i) is carried out at a temperature in the range 80 0 C to the reflux temperature of the solvent;
  • step (k) the reaction of step (i) is carried out under conditions that remove water from the reaction system (e.g. Dean-Stark conditions, in which * water produced by the reaction is condensed in a side condenser so that it does not return to the reaction mixture, and can be drained off if desired); and
  • step (i) the reaction of step (i) is carried out at or around ambient pressure (e.g. a nitrogen atmosphere of slightly elevated pressure may be used, particularly on an industrial scale).
  • ambient pressure e.g. a nitrogen atmosphere of slightly elevated pressure may be used, particularly on an industrial scale.
  • the secondary amine compound is N- methylpiperazine.
  • the secondary amine compound contains two basic nitrogen atoms.
  • Such compounds produce initial products [see formula (VI) below] which hydrolyse readily to compounds of formula (I).
  • Y is CH 3 or CH 2 OH.
  • the compound of formula (IV) may be treated with L-tartaric acid in step (c), to produce tolterodine L-tartrate [i.e. i?-(+)-tolterodine L-tartrate].
  • the salt form produced in this second aspect of the invention is preferably pharmaceutically acceptable. However, when the compound will be processed further, this is not essential.
  • the reductive amination of a compound of formula (I) may comprise treatment with diisopropylamine in a suitable solvent, such as methanol (which is preferred) or tert-amyl alcohol or mixtures thereof, followed by hydrogenation in the presence of a catalyst, such as Pd/C or Pd(OH) 2 /C.
  • a suitable solvent such as methanol (which is preferred) or tert-amyl alcohol or mixtures thereof
  • a catalyst such as Pd/C or Pd(OH) 2 /C.
  • the compound of formula (IV) may be treated with an aqueous acid, such as hydrochloric acid, to afford the corresponding hydrochloride salt.
  • the racemic compound may be converted to the corresponding (R)-enantiomer L-tartrate salt by neutralization of the hydrochloride salt in the presence of base, such as a mixture of sodium hydroxide and sodium carbonate, followed by resolution with L-tartaric acid.
  • base such as a mixture of sodium hydroxide and sodium carbonate
  • tolterodine L-tartrate i.e. i?-(+)-tolterodine L-tartrate] is prepared.
  • the (R)-enantiomer L-tartrate salt of the compound of formula (IV) may be prepared directly following reductive amination of the compound of formula (I) without formation of the hydrochloride salt.
  • the product of the reductive amination step may be treated with a solvent such as acetone and L-tartaric acid to afford the L-tartrate salt.
  • Y is CH 3
  • the invention provides a process for the production of fesoterodine
  • step (b) resolving the product of step (a) to obtain the (R)-enantiomer; (c) acylating the phenolic hydroxy group of the product of step (b) to produce the corresponding isobutyric acid ester;
  • Fesoterodine having chemical name 2-[(li?)-3-[bis(l-methylethyl)amino]-l- phenylpropyl]-4-hydroxymethylphenyl isobutyrate or alternatively R-(+)-isobutyric acid 2-(3-diisopropylamino-l-phenylpropyl)-4-hydroxymethylphenyl ester, is disclosed in European Patent 1077912 (see page 32 line 5 and claim 4, 3 rd compound). It is indicated in the treatment of overactive bladder.
  • the resolution is preferably carried out by fractional crystallization with a chiral acid, preferably (i?)-(-)-acetoxy(phenyl)acetic acid.
  • the acylating agent is preferably isobutyryl chloride.
  • the compound of formula (I) may exist in an open-ring form, although it is believed to exist predominantly in the closed-ring (lactol) form. Furthermore, it is believed that the process according to the first aspect of the invention produces a mixture of diastereoisomers of the lactol:
  • step (i) of the first aspect of the invention the reaction proceeds via an isolable intermediate compound of formula (V),
  • Y is selected from CH 3 , CH 2 OH, CH 2 CH 2 OH, CH 2 Br and Br. These compounds are provided according to a fourth aspect of the present invention. Preferably, Y is CH 3 .
  • step (i) of the first aspect of the invention the reaction proceeds via an intermediate compound of formula (VI)
  • Y is selected from CH 3 , CH 2 OH, CH 2 CH 2 OH, CH 2 Br and Br. These compounds are provided according to a fifth aspect of the present invention.
  • Y is CH 2 OH.
  • the invention further provides a compound of formula (I),
  • Y is selected from CH 2 CH 2 OH, CH 2 Br and Br.
  • the process according to the invention differs from US Patent Application 2003/0236438 (see above) in that none of the reactants are an aniline compound, and the compound of formula (II) according to the invention does not have an additional strongly activating or strongly electron-donating group present (such as methoxy in Example 2 of US Patent Application 2003/0236438). Furthermore, the amine catalysts used in the present invention are much simpler (e.g. they do not need to be chiral) and hence cheaper.
  • the process according to the invention differs from the Jurd paper mentioned above (Journal of Heterocylic Chemistry, vol 28 (4), 1991, pp 983-986) in that none of the reactants are an aniline compound, and the compound of formula (II) according to the invention does not have an additional strongly activating or strongly electron-donating group present, such as alkoxy or hydroxy.
  • the invention has the further advantage that, as part of a process for the production of tolterodine, in comparison with the process disclosed by WO 98/29402, a number of reaction and processing steps are eliminated, leading to a reduction in costs. Furthermore, the process avoids the use of expensive reducing agents such as diisobutylaluminium hydride (DIBAL), sodium bis(2-methoxyethoxy)aluminium hydride or lithium tri-tert-butoxyaluminohydride, which are also difficult to dispose of.
  • DIBAL diisobutylaluminium hydride
  • the invention has the further advantage that, as part of a process for the production of fesoterodine, in comparison with the processes disclosed in the prior art, a number of reaction and processing steps are eliminated, leading to a reduction in costs. Furthermore, the process avoids the use of hazardous and environmentally undesirable reagents, which are difficult to dispose of.
  • BuOH butanol .
  • DEA diethylamine
  • DMPU l,3-dimethyl-3,4,5,6-tetrahydro-2(lH)-pyrimidone
  • DMSO dimethylsulphoxide
  • EDTA ethylenediaminetetraacetic acid
  • ee enantiomeric excess
  • n-BuOH n-butanol
  • p.s.i. pounds per square inch
  • reaction mixture was filtered through ArbocelTM (filter aid) to remove catalyst residues and then heated to reflux and all diisopropylamine and methanol removed by distillation and replaced with toluene resulting in a final volume of 10ml/g.
  • the black solution was then cooled to 25°C, acetone (750L, 5ml/g) was added, and then the solution heated to 55-6O 0 C.
  • a solution of L-Tartaric acid (312g, 2.081mol, 1.5eq) in methanol (1.05L, 7ml/g) was added over 30 minutes maintaining the temperature at 55-6O 0 C.
  • the resulting suspension was then allowed to cool to room temperature and stirred for 12 hours.
  • the filtrate was then azeotroped with toluene to remove all methanol and diisopropylamine to end at a final volume corresponding to 10ml/g cresol.
  • the solution was then stirred at 50-60 0 C and 37% HCl (19.3 ml, 0.231 mol, 1.0 equiv c.f cresol) was added resulting in the precipitation of racemic tolterodine hydrochloride.
  • the suspension was cooled to 25 0 C and stirred for 2h, then filtered and washed with toluene (2 X 50ml). Racemic tolterodine hydrochloride was then dried under vacuum at 5O 0 C. Yield was 52.7 g, 63% from p- cresol with achiral purity of 97%.
  • Example 1 The reaction of Example 1 was repeated, but varying the amine catalyst and the solvent. The temperature used was approximately 100 0 C or the reflux temperature of any solvent if lower (unless indicated otherwise). Dean-Stark conditions were not used unless indicated (by *). The yields are shown in the following table.
  • the biphasic mixture was allowed to cool to ambient temperature, diluted with ethyl acetate (250 mL) and the organic phase separated. The organic phase was washed with aqueous HCl (25OmL), potassium bicarbonate (IM, 25OmL), dried over magnesium sulphate and evaporated under reduced pressure to give a black oil (50.0g, assumed to be quantitative).
  • Aqueous sodium bicarbonate (165 mL) was added to a mixture of the HCl salt (Example 8, 16.5g, 42.1 mmol, 1 equiv) in ethyl acetate (165 mL) and the mixture stirred for 1 hour. The phases were separated and the organic phase washed with water (195 mL), dried over magnesium sulphate and evaporated under reduced pressure to give the title compound as an oil containing ⁇ 25% wt/wt ethyl acetate (14.6g total, 11.03g of title compound, 31 mmol, 74%).
  • Enantiomeric excess was determined by converting the salt to the free base with sodium hydroxide and running normal phase chiral HPLC chromatography (Chiral Pak AS-H column, eluting with hexane (89.8%), IPA (10%), DEA (0.1%), TFA (0.1%) at 1 mL/minute).
  • Example 5 The title compound could be useful as a starting material to produce Example 5 in our co- pending International Patent Application No PCT/IB07/000619.
  • the corresponding hydrochloride salt to the title compound is disclosed as Example 12 in WO 98/43942.
  • Example l(e) The benzyloxy analogue of the title compound is disclosed as Example l(e) in WO 94/11337.
  • the title compound, once resolved, could also be useful as a starting material in the production of Example 3 in our co-pending International Patent Application No PCT/IB07/000619.
  • the catalyst Pd-ESCAT 142 [(5%Pd/C paste, ca. 50% water wet) 83g, 10% w/w] was added as a slurry in methanol (2075 mL, 2.5 mL/g). The system was purged with hydrogen, then the mixture was hydrogenated at 115 psi (793 x 10 3 Nm "2 , 7.92 bar) at a temperature of 4O 0 C for 20 hours.
  • the organic phase was washed with purified water (1.75 kg, 1 mL/g) at 50 0 C.
  • the phases were separated at 50 0 C and the toluene volume reduced to 3 mL/g (5.5 L) by distillation.
  • Crystallization was performed by reducing the temperature to 62 °C and then cooling to 40 °C over 40 mins.
  • the batch was held at 40 °C for 30 mins and then seeded using (i?)-2-[3-(diisopropylamino)-l-phenylpropyl]-4-(hydroxymethyl)phenol (0.01 kg, prepared previously using a similar method on a smaller scale).
  • the batch was agitated for a further 1 hour at 40 °C and then cooled to 20 °C over 3.5 hours.
  • the batch was granulated at 20 °C for 10 hours.
  • the slurry was then cooled to 2 °C over 1 hour and granulated at 2 °C for 1 hour (see temperature profile below).
  • the suspension was filtered and the cake washed with cold toluene (1.5 kg, 1 mL/g).
  • the damp product (0.933 kg, dry estimated by % LOD analysis) was a white crystalline solid. A toluene re-slurry was then performed.
  • the title compound is prepared from the compound of Example 16 using the method of US Patent 6,858,650 (see section 5, column 16). Alternatively, this reaction can be performed without the addition of an external acid-intercepting base - see US Patent 6,858,650 column 10 lines 32-40.
  • the title compound is prepared from the compound of Example 17 using the method of US Patent 6,858,650 (see section 6, column 16).

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
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Abstract

The invention provides a process for the production of a compound of formula (I), wherein Y is selected from CH3, CH2OH, CH2CH2OH, CH2Br and Br; comprising the steps of: (i) reacting a compound of formula (II), wherein OX is hydroxy or O- M+, in which M+ is a cation selected from Li+, Na+ and K+, and Y is as defined above; with trans-cinnamaldehyde (III), in the presence of a secondary amine compound; then (ii) treating the product of the preceding step with acid to afford the compound of formula (I). The above process may be used in the production of tolterodine and fesoterodine, which are useful in the treatment of overactive bladder.

Description

Process for the production of benzopyran-2-ol derivatives
The present invention relates to an improved process for the production of intermediates useful in the preparation of tolterodine, fesoterodine and other pharmaceutically useful compounds. The invention also provides improved processes for the production of such pharmaceutically useful compounds using the intermediates.
Tolterodine { 2- [( 1 i?)-3 - [bis( 1 -methylethyl)amino] - 1 -phenylpropyl] -4-methylphenol or alternatively (+)-Λf,N-diisopropyl-3-(2-hydroxy-5-methylphenyl)-3-phenylpropylamine},
Figure imgf000002_0001
is a muscarinic receptor antagonist for the treatment of overactive bladder including urinary incontinence. It gained its first marketing approval (as the tartrate salt) in 1997 and was launched in many markets in the following years under the trade marks DETROL and DETRUSITOL. Tolterodine tartrate was disclosed in International Patent Application WO 89/06644 (see in particular Example 22 and claim 7).
WO 98/29402 discloses a process for the production of tolterodine which comprises condensing p-cresol (a) with cinnamic acid (b), followed by reduction of the resulting lactone (c) with a reducing agent, such as diisobutylaluminium hydride (DIBAL), sodium bis(2-methoxyethoxy)aluminium hydride or lithium txi-tert-butoxyaluminohydride, to give the corresponding benzopyran-2-ol compound (d). The benzopyran-2-ol compound (d) can then be converted to racemic tolterodine hydrochloride (e) by reductive amination with diisopropylamine, followed by addition of aqueous hydrochloric acid. Finally, tolterodine L-tartrate is formed by neutralisation of the hydrochloride salt (e) with NaOH/NaHCO3 and subsequent resolution using L-tartaric acid. The process is shown in Scheme 1 below. DIBAL
Figure imgf000003_0001
Figure imgf000003_0002
(i) HN1Pr2, H2, Pd/C MeOH
(ii) HCI
Figure imgf000003_0003
It can be seen that in the process disclosed by WO 98/29402, the benzopyran-2-ol compound (d) is prepared in two steps and involves the use of a relatively expensive reducing agent (DIBAL).
WO 01/49649 describes the reductive amination of the enantiomers of compound (d) above to give tolterodine and its enantiomer. The enantiomers of compound (d) are produced by enantioselective reactions. It also relates to the same processes applied to analogous compounds, in particular the analogue of tolterodine in which the methyl group in the phenolic ring is replaced with a 5 -hydroxy methyl group.
US Patent Application 2003/0236438 (MacMillan et al) discloses the use of comparatively complex chiral imidazolidinone catalysts [e.g. (2S,5S)-5-benzyl-2-tert- butyl-3-methylimidazolidin-4-one] for carrying out enantioselective 1,4-addition reactions between aniline nucleophiles and α,β-unsaturated aldehydes (this work is also described in MacMillan et al, J. Am. Chem. Soc, 2002, 124, 7894-7895). Example 2 from US Patent Application 2003/0236438 is typical of the reactions disclosed:
Figure imgf000004_0001
It can be seen that the carbon atom of the aromatic ring para to the amine group bonds to the alpha-beta unsaturated aldehyde.
Jurd (Journal of Heterocylic Chemistry, vol 28 (4), 1991, pp 983-986) describes the reaction of 3,4-methylenedioxyphenol, morpholine and cinnamaldehyde in methanol to produce 2-morpholinyl-4-phenylbenzopyrans.
Surprisingly, it has now been found that the benzopyran-2-ol compound (d) of Scheme 1 can be produced in a one-pot reaction starting from p-cresol (a). Analogous compounds can also be produced. Thus, according to a first aspect of the present invention, there is provided a process for the production of a compound of formula (I),
Figure imgf000004_0002
wherein Y is selected from CH3, CH2OH, CH2CH2OH, CH2Br and Br; comprising the steps of:
(i) reacting a compound of formula (II),
Figure imgf000004_0003
wherein
OX is hydroxy or 0"M+, in which M+ is a cation selected from Li+, Na+ and K+, and Y is as defined above; with traMs-cinnamaldehyde (III),
Figure imgf000005_0001
in the presence of a secondary amine compound; then
(ii) treating the product of the preceding step with acid to afford the compound of formula (I).
By "secondary amine compound" we mean an organic compound which contains at least one secondary amine group, i.e. a compound of the formula:
Figure imgf000005_0002
in which Ra and Rb are not hydrogen. Preferably, Ra and Rb are each linked to the nitrogen atom by a CH2 group, for example they are independently Ci-6 alkyl or together form a 4- or 5-membered alkyl chain in which one carbon atom is optionally replaced by O or N.
Preferred embodiments of the first aspect of the invention are those in which: (a) OX is hydroxy;
(b) Y is CH3 or CH2OH;
(c) the secondary amine compound is achiral;
(d) the secondary amine compound contains two secondary amine groups, for example piperazine (this catalyst produces particularly high yields); (e) when the secondary amine compound contains two secondary amine groups, 0.5- 1.25 mole equivalents of the secondary amine compound are used in step (i); (f) alternatively, the secondary amine compound contains one secondary amine group, and more preferably the secondary amine compound is morpholine, dibutylamine, dibenzylamine, 1,1,3,3-tetramethylguanidine, diethylamine, diisopropylamine, piperidine or an N-(Ci-6 alkyl)piperazine. 7V-methylpiperazine is particularly preferred because it produces good yields, the initial product [see formula (VI) below] is readily hydrolysed to the corresponding lactol compound of formula (I), and the crude compound of formula (I) has an improved purity which facilitates crystallization; (g) when the secondary amine compound contains one secondary amine group, 1-5, more preferably 1-2.5 mole equivalents of the secondary amine compound are used in step (i);
(h) the acid used in step (ii) is aqueous hydrochloric acid (preferably no more than 2M concentration), although the following aqueous acids at similar concentrations also provide good results: citric acid, acetic acid, oxalic acid, trifluoroacetic acid, maleic acid, fumaric acid, salicyclic acid, traws-cinnamic acid, benzoic acid, camphor sulfonic acid and tosic acid;
(i) the reaction of step (i) is carried out in an organic solvent selected from toluene, xylene, N-butyl acetate, t-amyl alcohol, dioxane and dibutyl ether, most preferably toluene (which produces particularly high yields);
(j) the reaction of step (i) is carried out at a temperature in the range 800C to the reflux temperature of the solvent;
(k) the reaction of step (i) is carried out under conditions that remove water from the reaction system (e.g. Dean-Stark conditions, in which* water produced by the reaction is condensed in a side condenser so that it does not return to the reaction mixture, and can be drained off if desired); and
(1) the reaction of step (i) is carried out at or around ambient pressure (e.g. a nitrogen atmosphere of slightly elevated pressure may be used, particularly on an industrial scale).
It is particularly preferred that when Y is CH2OH, the secondary amine compound is N- methylpiperazine.
Preferably, the secondary amine compound contains two basic nitrogen atoms. Such compounds produce initial products [see formula (VI) below] which hydrolyse readily to compounds of formula (I).
According to a second aspect of the invention, there is provided a process for the production of a compound of formula (IV),
Figure imgf000007_0001
wherein Y is selected from CH3, CH2OH, CH2CH2OH, CH2Br and Br, or a salt thereof, comprising:
(a) producing a compound of formula (I) as defined above, using the process according to the first aspect of the invention; then
(b) reductively aminating the compound of formula (I) with diisopropylamine;
(c) and where desired converting the resulting compound into a salt.
Preferably, in the second aspect of the invention, Y is CH3 or CH2OH. When Y is CH3, the compound of formula (IV) may be treated with L-tartaric acid in step (c), to produce tolterodine L-tartrate [i.e. i?-(+)-tolterodine L-tartrate]. When the compound of formula (IV) is to be used as a pharmaceutical, the salt form produced in this second aspect of the invention is preferably pharmaceutically acceptable. However, when the compound will be processed further, this is not essential.
The reductive amination of a compound of formula (I) may comprise treatment with diisopropylamine in a suitable solvent, such as methanol (which is preferred) or tert-amyl alcohol or mixtures thereof, followed by hydrogenation in the presence of a catalyst, such as Pd/C or Pd(OH)2/C.
In one. embodiment, the compound of formula (IV) may be treated with an aqueous acid, such as hydrochloric acid, to afford the corresponding hydrochloride salt. The racemic compound may be converted to the corresponding (R)-enantiomer L-tartrate salt by neutralization of the hydrochloride salt in the presence of base, such as a mixture of sodium hydroxide and sodium carbonate, followed by resolution with L-tartaric acid. In one embodiment, tolterodine L-tartrate [i.e. i?-(+)-tolterodine L-tartrate] is prepared. In an alternative embodiment, the (R)-enantiomer L-tartrate salt of the compound of formula (IV) may be prepared directly following reductive amination of the compound of formula (I) without formation of the hydrochloride salt. For example, in one embodiment the product of the reductive amination step may be treated with a solvent such as acetone and L-tartaric acid to afford the L-tartrate salt. When Y is CH3, this produces tolterodine L-tartrate [i.e. i?-(+)-tolterodine L-tartrate].
According to a third aspect, the invention provides a process for the production of fesoterodine,
Figure imgf000008_0001
or a pharmaceutically acceptable salt thereof, which comprises:
(a) producing a compound of formula (IV), as defined above in which Y is CH2OH, using the process described above;
(b) resolving the product of step (a) to obtain the (R)-enantiomer; (c) acylating the phenolic hydroxy group of the product of step (b) to produce the corresponding isobutyric acid ester;
(d) and where desired or necessary, converting the resulting compound into a pharmaceutically acceptable salt.
Fesoterodine, having chemical name 2-[(li?)-3-[bis(l-methylethyl)amino]-l- phenylpropyl]-4-hydroxymethylphenyl isobutyrate or alternatively R-(+)-isobutyric acid 2-(3-diisopropylamino-l-phenylpropyl)-4-hydroxymethylphenyl ester, is disclosed in European Patent 1077912 (see page 32 line 5 and claim 4, 3rd compound). It is indicated in the treatment of overactive bladder. In this third aspect, the resolution is preferably carried out by fractional crystallization with a chiral acid, preferably (i?)-(-)-acetoxy(phenyl)acetic acid.
The acylating agent is preferably isobutyryl chloride.
The compound of formula (I) may exist in an open-ring form, although it is believed to exist predominantly in the closed-ring (lactol) form. Furthermore, it is believed that the process according to the first aspect of the invention produces a mixture of diastereoisomers of the lactol:
Figure imgf000009_0001
ω
The R- and S-enantiomers of the chiral centre marked with an asterisk above are believed to be present in equal amounts. The production of all these tautomeric and stereoisomeric forms is embraced by the present invention.
When piperazine is used in step (i) of the first aspect of the invention, the reaction proceeds via an isolable intermediate compound of formula (V),
Figure imgf000009_0002
wherein Y is selected from CH3, CH2OH, CH2CH2OH, CH2Br and Br. These compounds are provided according to a fourth aspect of the present invention. Preferably, Y is CH3.
When iV-methylpiperazine is used in step (i) of the first aspect of the invention, the reaction proceeds via an intermediate compound of formula (VI)
(VI)
Figure imgf000009_0003
wherein Y is selected from CH3, CH2OH, CH2CH2OH, CH2Br and Br. These compounds are provided according to a fifth aspect of the present invention. Preferably, Y is CH2OH.
The invention further provides a compound of formula (I),
Figure imgf000010_0001
wherein Y is selected from CH2CH2OH, CH2Br and Br.
The process according to the invention differs from US Patent Application 2003/0236438 (see above) in that none of the reactants are an aniline compound, and the compound of formula (II) according to the invention does not have an additional strongly activating or strongly electron-donating group present (such as methoxy in Example 2 of US Patent Application 2003/0236438). Furthermore, the amine catalysts used in the present invention are much simpler (e.g. they do not need to be chiral) and hence cheaper.
The process according to the invention differs from the Jurd paper mentioned above (Journal of Heterocylic Chemistry, vol 28 (4), 1991, pp 983-986) in that none of the reactants are an aniline compound, and the compound of formula (II) according to the invention does not have an additional strongly activating or strongly electron-donating group present, such as alkoxy or hydroxy.
The invention has the further advantage that, as part of a process for the production of tolterodine, in comparison with the process disclosed by WO 98/29402, a number of reaction and processing steps are eliminated, leading to a reduction in costs. Furthermore, the process avoids the use of expensive reducing agents such as diisobutylaluminium hydride (DIBAL), sodium bis(2-methoxyethoxy)aluminium hydride or lithium tri-tert-butoxyaluminohydride, which are also difficult to dispose of. The invention has the further advantage that, as part of a process for the production of fesoterodine, in comparison with the processes disclosed in the prior art, a number of reaction and processing steps are eliminated, leading to a reduction in costs. Furthermore, the process avoids the use of hazardous and environmentally undesirable reagents, which are difficult to dispose of.
The invention is illustrated by the following examples in which the following abbreviations may be used:
BuOH = butanol . DEA = diethylamine
DMA = dimethylacetamide
DMF = dimethylformamide
DMPU = l,3-dimethyl-3,4,5,6-tetrahydro-2(lH)-pyrimidone
DMSO = dimethylsulphoxide EDTA = ethylenediaminetetraacetic acid ee = enantiomeric excess
EtOAc = ethyl acetate
EtOH = ethanol h = hour IPA = isopropyl alcohol
LC-MS = liquid chromatography - mass spectrometry
LOD = loss on drying
MeOH = methanol min = minute n-BuOH = n-butanol p.s.i. = pounds per square inch
TFA = trifluoroacetic acid
THF = tetrahydrofuran tic = thin layer chromatography
Example 1
Synthesis of 3,4-Dihvdro-6-methyl-4-phenyl-2H-benzopyran-2-ol
Figure imgf000012_0001
p-Cresol (15Og, 1.387mol) was stirred with piperazine (72g, 0.832mol, 0.6eq) in toluene (1.5L, 10ml/g) and then heated at reflux under Dean & Stark conditions for at least 30 minutes to remove water giving a clear pale yellow solution. Trans-Cinnamaldehyde (262ml, 275g, 2.081 mol, 1.5eq) was then added over 2 hours whilst maintaining the reaction mixture at reflux under Dean & Stark conditions. Once the addition was complete, heating of the reaction mixture was continued at reflux under Dean & Stark conditions for a further 4 hours. The black solution was allowed to cool to 800C and then slowly quenched over 45 minutes with a solution of 0.67M HCl(aq) (750ml, 0.601 mol, 1.3eq). The two-phase solution was then stirred vigorously for at least 12 hours at a temperature of 75-8O0C. The stirring was then stopped and the mixture allowed to cool to room temperature and the phases separated. The toluene solution was then washed with IM HCl(aq) (750ml, 5ml/g), then water (3 X 750ml, 5ml/g). The 3,4-dihydro-6-methyl-4- phenyl-2H-benzopyran-2-ol was not isolated but instead the toluene solution was used directly in the reductive amination step (Example 2).
Example 2
Synthesis of Tolterodine L-Tartrate
Figure imgf000012_0002
Tolterodine L-Tartrate The toluene solution comprising crude 3,4-dihydro-6-methyl-4-phenyl-2H-benzopyran-2- ol from Example 1 (theoretical = 333.3g in l.5L of toluene) was diluted with methanol (750ml, 5ml/g), then diisopropylamine (583ml, 421g, 4.161 mol, 3eq) was added. The black solution was then hydrogenated over 20wt% Pd(OH)2/C moist (10wt%, 33g) at 62IxIO3 Nm'2 (90 psi) and 1100C for 48 hours. A sample was removed for analysis.
The reaction mixture was filtered through Arbocel™ (filter aid) to remove catalyst residues and then heated to reflux and all diisopropylamine and methanol removed by distillation and replaced with toluene resulting in a final volume of 10ml/g. The black solution was then cooled to 25°C, acetone (750L, 5ml/g) was added, and then the solution heated to 55-6O0C. A solution of L-Tartaric acid (312g, 2.081mol, 1.5eq) in methanol (1.05L, 7ml/g) was added over 30 minutes maintaining the temperature at 55-6O0C. The resulting suspension was then allowed to cool to room temperature and stirred for 12 hours. The suspension was filtered, washed with acetone (2 X 600ml, 4ml/g), then dried in a vacuum oven at 5O0C for 12 hours to give the title compound as an off white solid [159.2g, 48% (24% from p-Cresol)]. Achiral purity was 100% (no impurities detected) and chiral purity was 91.4% e.e.
Example 3
Synthesis of racemic tolterodine hydrochloride
Figure imgf000013_0001
Toluene
Figure imgf000013_0002
Figure imgf000013_0003
(i) Toluene/MeOH 20% Pd(OH)2/C (wet) H2, diisopropylamine, 11O 0C, 90psi
(ii) 37%HCI Racemic tolterodine HCI
Step A. Preparation of 3,4-Dihvdro-6-methyl-4-phenyl-2H-benzopyran-2-ol
To a solution of p-cresol (25 g, 0.231 mol, 1 equiv), piperazine (11.94 g, 0.139 mol, 0.6 equiv) and toluene (250ml, 10 ml/g) at reflux under Dean & Stark conditions was added cinnamaldehyde (45.83 g, 44 ml, 0.347 mol, 1.5 equiv) over a 2 hour period and reaction mixture monitored by HPLC for the presence of p-cresol. Upon completion (2 to 3 hours), the mixture was cooled to 800C and a solution of c.HCl (25 ml, 0.301 mol, 1.3 equiv) in water (100ml, 5 ml/g) was slowly added and heated at 80-900C for at least 5 hours. The resulting solution was allowed to cool to room temperature and the phases separated. The toluene solution was washed with IM HCl (125 ml, 5 ml/g), then water (3 X 125 ml). The resulting organic layer was taken into the reductive amination step (Step B) as a crude mixture.
Step B. Preparation of racemic tolterodine hydrochloride
To the crude solution from Step A was added methanol (125 ml, 5 ml/g cresol) and diisopropylamine (92 ml, 0.693mol, 3 equiv). The mixture was then hydrogenated over 20wt% Pd(OH)2/C wet (5.6 g, 10wt% theory of the benzopyran-2-ol) at 110 0C under 586xlO3 Nm"2 (85 psi) hydrogen pressure. Reaction progress was monitored by HPLC (completion usually occurs between 16 and 24h). Upon completion, the mixture was cooled, purged with nitrogen, filtered and washed with toluene (2 X 25 ml). The filtrate was then azeotroped with toluene to remove all methanol and diisopropylamine to end at a final volume corresponding to 10ml/g cresol. The solution was then stirred at 50-600C and 37% HCl (19.3 ml, 0.231 mol, 1.0 equiv c.f cresol) was added resulting in the precipitation of racemic tolterodine hydrochloride. The suspension was cooled to 25 0C and stirred for 2h, then filtered and washed with toluene (2 X 50ml). Racemic tolterodine hydrochloride was then dried under vacuum at 5O0C. Yield was 52.7 g, 63% from p- cresol with achiral purity of 97%.
The synthesis of tolterodine L-tartrate according to the methods of Examples 1-3 is shown in Scheme 2 below.
Figure imgf000015_0001
p-Cresol frans-Cinnamaldehyde
Figure imgf000015_0002
Figure imgf000015_0003
Example 4
Influence of amine catalyst and solvent on yield of 3,4-Dihydro-6-methyl-4-phenyl-2H- benzopyran-2-ol
The reaction of Example 1 was repeated, but varying the amine catalyst and the solvent. The temperature used was approximately 1000C or the reflux temperature of any solvent if lower (unless indicated otherwise). Dean-Stark conditions were not used unless indicated (by *). The yields are shown in the following table.
Figure imgf000016_0001
Figure imgf000017_0002
f denotes secondary amine compound
Example 5 l,4-Bis-(6-methyl-4-phenyl-chroman-2-yl)-piperazine
Figure imgf000017_0001
The preparation of the title compound was carried out using the procedure of Example 1, except for the omission of a quench with aqueous acid. Instead, upon completion of the reaction the mixture was allowed to cool to ambient temperature resulting in a brown suspension. Filtration of this suspension gave a brown solid with 1H and 13C NMR providing confirmation of the structure. Melting point: 241°C.
Example 6 Preparation of 6-(2-Hvdroxy-ethyl)-4-phenyl-chroman-2-ol
Figure imgf000018_0001
To a solution of 4-hydroxyphenethyl alcohol (Tyrosol) (5.0 g, 36 mmol, 1 equiv), piperazine (1.87 g, 22 mmol, 0.6 equiv) and toluene (50 ml) at reflux under N2 and Dean & Stark conditions was added cinnamaldehyde (6.4 ml, 51 mmol, 1.4 equiv) and the reaction mixture maintained at heat for 17 h. The reaction was cooled to 8O0C and quenched with aqueous HCl (0.7 molar, 1.3 equiv) then stirred at heat for 18 h. The biphasic mixture was allowed to cool to ambient temperature, separated, the organic phase washed with aqueous HCl and water and the organic phase concentrated to a black residue under reduced pressure. Flash chromatography eluting with 20% EtOAc/Heptane afforded the title compound as the main constituent of an approximately 80% pure yellow oil, R/ = 0.37 (50% EtOAc/Heptane) and structure confirmed by 1H NMR and LC-MS (M+l = 271).
Example 7
Alternative preparation of 6-(2-hvdroxy-ethyl)-4-phenyl-chroman-2-ol using N- methylpiperazine
Figure imgf000019_0001
To a solution of 4-hydroxyphenethyl alcohol (Tyrosol) (25.0 g, 181 mmol, 1 equiv), N-methylpiperazine (54.4g g, 543 mmol, 3 equiv) and toluene (200 ml) at reflux under N2 and Dean & Stark conditions was added cinnamaldehyde (35.9g ml, 272 mmol, 1.5 equiv) over a period of 2 hours and the reaction mixture maintained at reflux for 17 h. The reaction was cooled to 500C and quenched with aqueous HCl (2M, 375mL, ~4 equiv). The biphasic mixture was allowed to cool to ambient temperature, diluted with ethyl acetate (250 mL) and the organic phase separated. The organic phase was washed with aqueous HCl (25OmL), potassium bicarbonate (IM, 25OmL), dried over magnesium sulphate and evaporated under reduced pressure to give a black oil (50.0g, assumed to be quantitative).
Example 8 Preparation of 2-F3-(Diisopropylaminoπ-phenylpropyH-4-(2-hvdroxyethyl)phenol hydrochloride
Figure imgf000019_0002
A mixture of 6-(2-hydroxy-ethyl)-4-phenyl-chroman-2-ol (Example 7, 3Og, 111 mmol, 1 equiv), diisopropylamine (33.7g, 333 mmol, 3 eq) and palladium hydroxide on carbon [50% wet catalyst (50% by weight is water), 6g, 0.2 equiv] in toluene (120 mL) was hydrogenated at 621 x 103 Nm"2 (90 psi) hydrogen pressure at 110 0C. The reaction mixture was cooled to room temperature and filtered through arbocel and evaporated under reduced pressure. The resulting oil was dissolved in acetonitrile (200 mL) and concentrated hydrochloric acid (11.6 mL, 1.05 equiv) was added. The mixture was distilled at ambient pressure, removing approximately 100 mL of acetonitrile, and the distilled solvent replaced with fresh acetonitrile. The mixture was allowed to cool and crystallise overnight. The product was filtered and washed with a small portion of acetonitrile and dried overnight in vacuo at 50 0C to give the title compounds as a white solid (26.7g, 68.1 mmol, 61%).
Example 9 Preparation of 2-r3-(Diisopropylamino)- 1 -phenylpropyl~|-4-(2-hvdroxyethyl')phenol
Figure imgf000020_0001
Aqueous sodium bicarbonate (165 mL) was added to a mixture of the HCl salt (Example 8, 16.5g, 42.1 mmol, 1 equiv) in ethyl acetate (165 mL) and the mixture stirred for 1 hour. The phases were separated and the organic phase washed with water (195 mL), dried over magnesium sulphate and evaporated under reduced pressure to give the title compound as an oil containing ~25% wt/wt ethyl acetate (14.6g total, 11.03g of title compound, 31 mmol, 74%).
Example 10 Preparation of (/?)-2-[3-(Diisopropylamino)- 1 -phenylpropyl~|-4-(2-hvdroxyethyl)phenol (S*)-2-phenoxypropionic acid salt
Figure imgf000021_0001
(S)-2-Phenoxypropionic acid (3.4Og, 20.5 mmol, 1 equiv) was added to a solution of 2-[3- (diisopropylamino)-l-phenylpropyl]-4-(2-hydroxyethyl)phenol (Example 9, 7.28g, 20.5 mmol, 1 equiv) in ethyl acetate. The mixture was heated at 80 0C for 2 days, upon which the mixture was cooled to room temperature, filtered and washed with ethyl acetate and dried in vacuo at 50 0C overnight to give the title compound as a white solid (3.9g, 7.48 mmol, 37% yield, 94% ee).
Enantiomeric excess was determined by converting the salt to the free base with sodium hydroxide and running normal phase chiral HPLC chromatography (Chiral Pak AS-H column, eluting with hexane (89.8%), IPA (10%), DEA (0.1%), TFA (0.1%) at 1 mL/minute).
The title compound could be useful as a starting material to produce Example 5 in our co- pending International Patent Application No PCT/IB07/000619. The corresponding hydrochloride salt to the title compound is disclosed as Example 12 in WO 98/43942.
Example 11
Synthesis of 3,4-dihvdro-6-bromo-4-phenyl-2H-benzopyran-2-ol
Figure imgf000022_0001
4-Bromophenol (2.Og, l l.όmmmol) was stirred with N-methylpiperazine (3.48g, 34.8mmol, 3eq) in toluene (30ml, 15ml/g) and heated at reflux under Dean & Stark conditions. Once reflux was achieved, trans-cinammaldehyde (2.2g, 17.4mmol, 1.5eq) was added over 2 hours. Once addition was complete, heating of the reaction mixture at reflux under Dean & Stark conditions was continued for 3 hours. The dark solution was cooled to 250C and diluted with ethyl acetate (20ml, 10ml/g) and quenched with 2M HCl (30ml, 15ml/g). The phases were separated and the upper organic layer was washed with further 2M HCl (20ml, 10ml/g) and IM sodium hydrogen carbonate solution (20ml, 10ml/g). The organic phase was dried (MgSO4), filtered and concentrated to give a dark coloured oil (4.2g, 1 l.όmmol, assumed to be quantitative)
Example 12 Synthesis of 2-r3-(Diisopropylamino)-l-phenylpropyll-4-bromophenol hydrochloride salt
Figure imgf000022_0002
Crude 3,4-dihydro-6-bromo-4-phenyl-2H-benzopyran-2-ol (Example 11, 2.Og, 6.55mmol) was dissolved in toluene (20ml, 10ml/g) and to this solution was added titanium tetraisopropoxide (5.84ml, 3eq) and diisopropylamine (1.0ml, l.leq). The reaction mixture was cooled to 0-50C and sodium borohydride (0.75g, 3eq) was added portionwise over 15 minutes. Ethanol was charged dropwise over 15 minutes and stirred at 0-5°C for a further 2 hours. The reaction was quenched with water (20ml), ethyl acetate (50ml) and concentrated ammonia solution (20ml). The suspension was filtered through celite and the phases were separated. The organic layer was washed with water (50ml), dried (MgSO4), filtered and concentrated to give the free base as a brown oil. This was dissolved in ethyl acetate (50ml) and 5M HCl (2ml) was added. Excess acid and water were azeotroped with fresh ethyl acetate (2x5 OmI) and the resulting solid was granulated in fresh ethyl acetate (20ml) for 48 hours. The solid was collected by filtration, washed with ethyl acetate (10ml) and dried at 5O0C under vacuum for 4 hours. The title compound was obtained as a white solid ( 1.12g, 40% from 4-bromophenol).
The benzyloxy analogue of the title compound is disclosed as Example l(e) in WO 94/11337. The title compound, once resolved, could also be useful as a starting material in the production of Example 3 in our co-pending International Patent Application No PCT/IB07/000619.
Example 13
Synthesis of (2-Hydroxy-4-phenyl-3 ,4-dihydro-2H-chromen-6-yl)methanol
N-methylpiperazine
Figure imgf000023_0001
1) Toluene, reflux, 10h
2) Toluene, EtOAc, HCi 2M wash
Figure imgf000023_0003
3) Toluene, EtOAc, Crystallisation
4-(Hydroxymethyl)phenol trans-Cinnamaldehyde
Figure imgf000023_0002
(2-Hydroxy-4-phenyl-3,4- dihydro-2H-chromen-6- yl)methanol 4-(Hydroxymethyl)phenol (2.515kg, 20.26mol, leq) was stirred with TV-methylpiperazine (5.06kg, 50.52mol, 2.5eq) in toluene (17.74kg, 20.5L, 8.15mL/g) and then heated to reflux. trans-Cinnamaldehyde (3.35kg, 25.35mol, 1.25eq) was then added over 2 hours maintaining the reaction mixture at reflux. The transfer line was washed with toluene (0.9Kg, 0.35ml/g). Once the addition was complete the reaction mixture continued to be heated at reflux for 19h. Then some toluene was distilled off, reducing the volume to approximately 18.5L. The mixture was then allowed to cool to room temperature and EtOAc was added (13.5Kg 15L, 6mL/g). The organic phase was washed with HCl 2M (46.4kg, 46.4L 18.5mL/g). The phases were separated, and ethyl acetate (27.1kg, 3OL, 12ml/g) was added to dilute the organic layer. The organic phase was washed with IM HCl (17.75kg, 17.75L 7.1mL/g), 5% w/w NaHCO3 (17.5L, 7mL/g) and water (25L, lOmL/g). The phases were separated, and toluene (6.5Kg, 7.5L, 3ml/g) was added to the organic layer, and the mixture was distilled to approximately 8L. Additional toluene (7kg) was charged followed by ethyl acetate (3.9L). The mixture was heated to reflux then cooled to 220C at l°C/minute, then stirred for 20hrs. The suspension was cooled to 20C and granulated for 2hrs. The slurry was filtered and the cake was washed with cold toluene (2x4.3Kg, 5L). The resulting pale tan solid was dried in vacuum for 68h at 40°C, to provide 2.76Kg of product (2-hydroxy-4-phenyl-3,4-dihydro-2H-chromen-6- yl)methanol (53.4% yield) which was used in the following example without purification: 1H NMR 300MHz d6 DMSO δ ppm (mixture of isomers, 10:1): 1.95-2.10 (m, 2H), 2.15- 2.35 (m, minor isomer), 3.25-3.35 (m, IH), 4.15-4.35 ( m, 3H), 4.80-4.95 (m, IH), 5.35- 5.45 (m, minor isomer), 5.46-5.55 (m, IH), 6.51-6.54 (m, minor isomer), 6.58-6.63 (m, IH), 6.75 (d J=8.2Hz, IH), 6.98-7.40 (m, 6H).
Example 14
Synthesis of 2-r3-(Diisopropylamino> 1 -phenylpropylM-ftiydroxymethvDphenol
Ih w/w
Figure imgf000024_0001
Figure imgf000024_0002
2-[3-(Diisopropylamino)-1 -
(2-Hydroxy-4-phenyl-3,4- phenylpropyl]-4- dihydro-2H-chromen-6- (hydroxymethyl)phenol yl)methanol
(2-Hydroxy-4-phenyl-3,4-dihydro-2H-chromen-6-yl)methanol (Example 13, 830 g, 3.24 mol, 1.0 eq) was stirred in methanol (4150 mL, 5.0mL/g). Diisopropylamine (1362 mL, 9.72 mol, 3.0 eq) was then added over 15 minutes via dropping funnel. The resulting solution was then stirred for one hour under nitrogen.
The catalyst Pd-ESCAT 142 [(5%Pd/C paste, ca. 50% water wet) 83g, 10% w/w] was added as a slurry in methanol (2075 mL, 2.5 mL/g). The system was purged with hydrogen, then the mixture was hydrogenated at 115 psi (793 x 103 Nm"2, 7.92 bar) at a temperature of 4O0C for 20 hours.
The mixture was purged with nitrogen and filtered over Arbocel™ (filter aid). The residue pad was washed with methanol (2x1660 mL, 2x2.0 mL/g).
Due to equipment limitations, the above procedure was performed two further times on 830 and 840 g scale.
The three filtrates and their respective pad- washes were then combined to produce a single solution equivalent to a single 2.50 Kg scale reaction. The total volume was noted to act as the initial target volume in the following distillation procedure:
• Diisopropylamine (2500 mL, 1.0 mL/g) and t-amyl alcohol (10000 mL, 4.0 mL/g) were added to the reaction mixture. A vacuum distillation (100 mbar vacuum set) was then performed to distil down to the target volume previously noted.
• Diisopropylamine (2500 mL, 1.0 mL/g) and t-amyl alcohol (10000 mL, 4.0 mL/g) were added to the reaction mixture. A vacuum distillation (100 mbar vacuum set) was then performed to distil down to the target volume previously noted.
• Diisopropylamine (2500 mL, 1.0 mL/g) and t-amyl alcohol (10000 mL, 4.0 mL/g) were added to the reaction mixture. A vacuum distillation (100 mbar vacuum set) was then performed to distil down to the target volume previously noted.
• t-Amyl alcohol (12500 mL, 5.0 mL/g) was added to the reaction mixture. A vacuum distillation (100 mbar vacuum set) was then performed to distil down to a volume of 1250O mL. • t-Amyl alcohol (12500 mL, 5.0 mL/g) added to the reaction mixture. A vacuum distillation (100 mbar vacuum set) was then performed to distil down to a volume of 12500 mL. t-Amyl alcohol (12500 mL, 5.0 mL/g) added to the reaction mixture to give a final volume of 25L.
The t-amyl alcohol solution of crude product 2-[3-(diisopropylamino)-l-phenylpropyl]-4- (hydroxymethyl)phenol was used in the next step with no further purification. HPLC analysis (area/area) showed 93.3% product, plus: 4.2% starting material, and other impurities at 1.4% and 0.4%. Quantitative HPLC analysis indicated the crude solution contained 295Og product (89% yield).
Example 15 Synthesis of (7?)-2-|"3-(Diisopropylamino)-l-phenylpropyl1-4-(hvdroxymethyl)phenol (R)- acetoxy(phenyl)acetate
acid 0.5eq O r t.
Figure imgf000026_0002
Figure imgf000026_0001
2-[3-<Diisopropylamino)-1 - (R)-2-[3-(diisopropylamino)-1 -phenylpropyl]-4- phenylpropyQ-4- (hydroxymethyl)phenol (R)-acetoxy(phenyl)acetate
(hydroxymethyl)phenol t-Amyl alcohol (19.2L) was added to the previous solution of 2-[3-(diisopropylamino)-l- phenylpropyl]-4-(hydroxymethyl)phenol (from Example 14) in t-amyl alcohol (25L, containing 2.95kg, 8.64mol, leq) to give a total volume of 44.2L. This solution was heated to 7O0C. In a separate pot, a solution of (i?)-(-)-acetoxy(phenyl)acetic acid (0.839kg, 4.32mol, 0.5eq) in t-amyl alcohol (14.8L) was prepared at 5O0C then cooled to room temperature once all the acid had dissolved. This solution was then added to the solution of 2-[3-(diisopropylamino)-l-phenylpropyl]-4-(hydroxymethyl)phenol in t-amyl alcohol over one hour. The resulting solution was then seeded with product (0.03kg, lwt%, prepared previously by a similar method but on a smaller scale). The slurry was cooled to 6O0C over 2 hours and then to 250C over another 3 hours. The mixture was stirred at 250C for an additional 12 hours. The slurry was filtered and the cake was twice re-slurried with t-amyl alcohol (2x29.5L, 2xl0mL/g) and de-liquored well. The white solid was dried under reduced pressure at 4O0C for 12hours to provide 2.04kg (i?)-2-[3- (diisopropylamino)- 1 -phenylpropyl]-4-(hydroxymethyl)phenol
(i?)-acetoxy(phenyl)acetate (37.8% yield, corrected for 14.3%w/w t-amyl alcohol (determined by LOD analysis) with 99% ee by chiral HPLC.
HPLC method for ee monitoring:
Column: Chiralpak AS-H Flow rate: lml/min
Mobile Phase: Heptane 92.5/ Ethanol 7.5/ Diethylamine 0.12/ Trifluoroacetic acid 0.18 Temperature: 350C Detection: 220nm Retention times:
(i?)-2-[3-(diisopropylamino)- 1 -phenylpropyl]-4-(hydroxymethyl)phenol 15min (1S)-2-[3-(diisopropylamino)-l-phenylpropyl]-4-(hydroxymethyl)phenol 18.4min
Example 16 Synthesis of (i?)-2-r3-(Oiisopropylamino)- 1 -phenylpropyll-4-(hvdroxymethyl)phenol
potassium carbonate aq. toluene 5Q0C, toluene crystalization
Figure imgf000027_0002
Figure imgf000027_0001
(R)-2-[3-(Diisopropylamino)-1- (R)-2-[3-(Diisopropylamino)- phenylpropyl]-4- 1 -phenylpropyl]-4-
(hydroxymethyl)phenol (hydroxymethyl)phenol (R)-acetoxy(phenyl)acetate
(i?)-2-[3-(diisopropylamino)-l-phenylpropyl]-4-(hydroxymethyl)phenol (i?)-acetoxy(phenyl)acetate (Example 15, 1.75 kg, 3.27 mol, leq) was slurried in toluene (15.2 kg, 10 mL/g) and warmed to 50 0C. A 10% aq. solution Of K2CO3 (1.75 kg K2CO3 dissolved in 17.5 L purified water, 10 mL/g) was charged. The mixture was stirred vigorously at 50 °C for 30 minutes. The two solution phases were separated at 50 0C. The organic phase was washed with purified water (1.75 kg, 1 mL/g) at 50 0C. The phases were separated at 50 0C and the toluene volume reduced to 3 mL/g (5.5 L) by distillation. Crystallization was performed by reducing the temperature to 62 °C and then cooling to 40 °C over 40 mins. The batch was held at 40 °C for 30 mins and then seeded using (i?)-2-[3-(diisopropylamino)-l-phenylpropyl]-4-(hydroxymethyl)phenol (0.01 kg, prepared previously using a similar method on a smaller scale). The batch was agitated for a further 1 hour at 40 °C and then cooled to 20 °C over 3.5 hours. The batch was granulated at 20 °C for 10 hours. The slurry was then cooled to 2 °C over 1 hour and granulated at 2 °C for 1 hour (see temperature profile below). The suspension was filtered and the cake washed with cold toluene (1.5 kg, 1 mL/g). The damp product (0.933 kg, dry estimated by % LOD analysis) was a white crystalline solid. A toluene re-slurry was then performed. Toluene (2.42 kg, 2.6 mL/g (based on dry estimate)) cooled to 3 0C and damp product was charged and agitated at 3 °C for 15 mins. The suspension was filtered and the cake washed with cold toluene (1.6 kg, 1.5 mL/g (based on dry estimate)). The damp product was dried in vacuo at 45 °C to yield (R)-2- [3-(diisopropylamino)-l-phenylpropyl]-4-(hydroxymethyl)phenol (0.74 kg, 2.17 mol) in 66.7% yield as a white crystalline solid. HPLC indicates > 99.6% purity, and chiral HPLC indicates > 99% ee.
Example 17 Preparation of (i?)-(+)-Isobutyric acid 2-[3-(diisopropylamino)-l-phenylpropyH-4- (hvdroxymethyl)phenvl ester
Figure imgf000028_0001
The title compound is prepared from the compound of Example 16 using the method of US Patent 6,858,650 (see section 5, column 16). Alternatively, this reaction can be performed without the addition of an external acid-intercepting base - see US Patent 6,858,650 column 10 lines 32-40.
Example 18
Preparation of (7?)-(+VIsobutyric acid 2-r3-(diisopropylamino')-l-phenylpropyπ-4- (hvdroxymethyl)phenyl ester hydrogen fumarate
Figure imgf000028_0002
The title compound is prepared from the compound of Example 17 using the method of US Patent 6,858,650 (see section 6, column 16).
Example 19 Synthesis of r2-(4-Methylpiperazin- 1 -yl)-4-phenyl-2H-chroman-6-vn-methanol
Figure imgf000029_0002
4-(Hydroxymethyl)phenol traπs-Cinnamaldehyde
Figure imgf000029_0001
[2 (4-Methylpiperazin-1 -yl)-4-phenyl- 3,4-dihydro-2H-chromen-6-yl]methanol tra«5-Cinnamaldehyde (66.5g, 0.66mol, 1.25eq) was diluted with toluene (10OmL, 2mL/g based on 4-(hydroxymethyl)phenol), and was washed twice with a saturated solution of sodium hydrogen carbonate (2x10OmL) and once with water (10OmL). This toluene solution of cinnamaldehyde was then added over 2 hours to a mixture of 4- (hydroxymethyl)phenol (5Og, 0.40mol, leq) and N-methylpiperazine (113mL, l.Omol, 2.5eq) in toluene (35OmL, 7mL/g) heated to reflux under Dean-Stark conditions. Once the addition was complete the reaction mixture continued to be heated at reflux under Dean- Stark conditions for 1Oh. The mixture was then cooled to room temperature and a sample was evaporated to dryness under reduced pressure for analytical purposes. The dark oil contains crude [2-(4-methylpiperazin- 1 -yl)-4-phenyl-2H-chroman-6-yl]methanol (mixture of diastereoisomers) and impurities.
EI-GC-MS (Agilent), column: ZB-5ΗT, Temperature program: 5O0C (0.5min), 20°C/min to 32O0C (2min) obtained: RT=24.4min, MW: 338.
1H NMR (DMSO) (crude mixture) 30OmHz δ (ppm): 7.40-7.00 (28H, m); 6.89 (IH, d, J=2.0 Hz); 6.81 (IH, d, J=8.3 Hz); 6.75 (IH, d, J=8.2 Hz); 6.54 (IH, d, J=LO Hz); 4.87 (IH, d, J=10.2 Hz); 4.45 (IH, d, J=10.0 Hz); 4.40-4.20 (3H, m); 4.36 (2H, s); 4.23 (1.8H, s); 2.86 (4H, m); 2.80-2.50 (14H, m); 2.50-2.00 (50H, m) including 2.31 (s); 2.17 (s); 2.14 (s); 2.11 (s). The synthesis of fesoterodine hydrogen fumarate according to the methods of Examples 13-18 is shown in Scheme 3 below.
Figure imgf000030_0001
uri
Figure imgf000030_0002

Claims

Claims:
1. A process for the production of a compound of formula (I),
Figure imgf000031_0001
wherein Y is selected from CH3, CH2OH, CH2CH2OH, CH2Br and Br; comprising the steps of:-
(i) reacting a compound of formula (II),
Figure imgf000031_0002
wherein OX is hydroxy or O M+, in which M+ is a cation selected from Li+, Na+ and K+, and Y is as defined above; with trαns-cinnamaldehyde (III),
Figure imgf000031_0003
in the presence of a secondary amine compound; then (ii) treating the product of the preceding step with acid to afford the compound of formula (I).
2. The process as claimed in claim 1 , wherein OX is hydroxy.
3. The process as claimed in claim 1 or claim 2, wherein Y is CH3 or CH2OH.
4. The process as claimed in any one of claims 1 to 3, wherein the secondary amine compound is achiral.
5. The process as claimed in any one of claims 1 to 4, wherein the secondary amine compound contains two secondary amine groups.
6. The process as claimed in any one of claims 1 to 5, wherein the secondary amine compound is piperazine.
7. The process as claimed in claim 5 or claim 6, wherein 0.5-1.25 mole equivalents of the secondary amine compound are used in step (i).
8. The process as claimed in any one of claims 1 to 4, wherein the secondary amine compound contains one secondary amine group.
9. The process as claimed in any one of claims 1, 2, 3, 4 and 8, wherein the secondary amine compound is morpholine, dibutylamine, dibenzylamine, 1,1,3,3- tetramethylguanidine, diethylamine, diisopropylamine, piperidine or an N-(Ci-6 alkyl)piperazine.
10. The process as claimed in claim 9, wherein the secondary amine compound is N- methylpiperazine.
11. The process as claimed in any one of claims 8 to 10, wherein 1-5 mole equivalents of the secondary amine compound are used in step (i).
12. The process as claimed in any one of the preceding claims, wherein the acid used in step (ii) is aqueous hydrochloric acid.
13. The process as claimed in any one of the preceding claims, wherein the reaction of step (i) is carried out in an organic solvent selected from toluene, xylene, N-butyl acetate, t-amyl alcohol, dioxane and dibutyl ether.
14. The process as claimed in claim 13, wherein the solvent is toluene.
15. The process as claimed in any one of the preceding claims, wherein the reaction of step (i) is carried out at a temperature in the range 800C to the reflux temperature of the solvent.
16. The process as claimed in any one of the preceding claims, wherein the reaction of step (i) is carried out under conditions that remove water from the reaction system.
17. The process as claimed in any one of the preceding claims, wherein the reaction of step (i) is carried out at or around ambient pressure.
18. A process for the production of a compound of formula (IV),
(IV)
Figure imgf000032_0001
wherein Y is as defined in claim 1, or a salt thereof, comprising:
(a) producing a compound of formula (I) as defined in claim 1, using the process claimed in any one of the preceding claims; then
(b) reductively aminating the compound of formula (I) with diisopropylamine;
(c) and where desired converting the resulting compound into a salt.
19. The process as claimed in claim 18, wherein Y is CH3 or CH2OH.
20. The process as claimed in claim 19, wherein Y is CH3, the compound of formula (IV) is treated with L-tartaric acid in step (c), and tolterodine L-tartrate is produced.
21. A process for the production of fesoterodine,
Figure imgf000033_0001
or a pharmaceutically acceptable salt thereof, which comprises:
(a) producing a compound of formula (IV), as defined in claim 18, in which Y is CH2OH, using the process of claim 18;
(b) resolving the product of step (a) to obtain the (R)-enantiomer; (c) acylating the phenolic hydroxy group of the product of step (b) to produce the corresponding isobutyric acid ester;
(d) and where desired or necessary, converting the resulting compound into a pharmaceutically acceptable salt.
22. The process as claimed in claim 21, wherein the secondary amine compound used to produce the compound of formula I is N-methylpiperazine.
23. A compound of formula (V) ,
Figure imgf000033_0002
or a salt thereof, wherein Y is as defined in claim 1.
24. A compound of formula (VI),
Figure imgf000034_0001
or a salt thereof, wherein Y is as defined in claim 1.
25. A compound of formula (VII),
Figure imgf000034_0002
wherein Y is selected from CH2CH2OH, CH2Br and Br.
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US8722920B2 (en) 2009-07-27 2014-05-13 Crystal Pharma S.A.U. Process for obtaining 3, 3-diphenylpropylamines
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WO2011154854A1 (en) 2010-06-10 2011-12-15 Chemi Spa Process for the preparation of 2 -hydroxy- 4 -phenyl -3, 4 -dihydro-2h-chromen- 6 -yl -methanol and (r) - feso - deacyl
ITMI20101047A1 (en) * 2010-06-10 2011-12-11 Chemi Spa NEW PROCESS OF PREPARATION OF 2-HYDROXY-4-PHENYL-3,4-DIHYDRO-2H-CHROMEN-6-IL-METHANOL E (R) -2- [3- (DIISOPROPYLAMINOUS) -1-PHENYLPROPYL] -4- ( hydroxymethyl) Phenol.
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