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Title:
NOVEL MANDELATE SALT OF FESOTERODINE
Document Type and Number:
WIPO Patent Application WO/2009/122303
Kind Code:
A2
Abstract:
Provided herein is a novel raantlelate sail of fesoterodine, process for the preparation, pharmaceutics!! compositions, and method of treating thereof. Provided also herein are solid state forms of fesoterodine mandelate, process for the preparation, pharmaceutical compositions, and method of treating thereof. The raandelate salt of fesoterodine is useful for preparing fesoterodine free base or a pharmaceutically acceptable salt thereof; particularly fesoterodine fumaraie, in high purity.

Inventors:
CHARUGUNDLA KISHORE (IN)
KUMAR UDHAYA (IN)
NEELA PRAVEEN KUMAR (IN)
PRADHAN NITIN SHARADCHANDRA (IN)
VALGEIRSSON JON (IS)
Application Number:
PCT/IB2009/005679
Publication Date:
October 08, 2009
Filing Date:
April 06, 2009
Export Citation:
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Assignee:
ACTAVIS GROUP PTC EHF (IS)
CHARUGUNDLA KISHORE (IN)
KUMAR UDHAYA (IN)
NEELA PRAVEEN KUMAR (IN)
PRADHAN NITIN SHARADCHANDRA (IN)
VALGEIRSSON JON (IS)
International Classes:
C07C51/41; C07C213/06; C07C213/10; C07C219/28; C07C59/50; C07C57/15; A61K31/21; A61P13/00
Domestic Patent References:
WO2005092341A12005-10-06
WO2003099268A12003-12-04
WO2007141298A12007-12-13
WO2009037569A22009-03-26
Foreign References:
US6858650B12005-02-22
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Claims:

We claim: 1. A mandelate salt of 2-[(lR)-3-|>i3(l-mcthylcthyl)amiix>]-l-phcnylpropylJ-^hydroxy mcthylphcnyi isobutyrate.

2. A solid state form of fesoterodine mandelate salt 3. The solid fesoterodine mandelate salt of claim 2, wherein the solid state form is a crystalline form or an amorphous form.

4. The solid fesoterodine mandelate salt of claim 2, which is in a crystalline form. 5. The solid feaoterodine mandelate salt of claim 2, wherein the solid state form is anhydrous and/or solvent-free form or as a hydrate and/or a solvate 6. The fesoterodine mandelate salt of any one of claims 1 to 5, characterized by at least one, or more, of the following properties: i) a powder X-ray diffraction pattern substantially in accordance with Figure 1 ; ii) a powder X-ray diffraction pattern having peaks at about 4.98, 10.0, 14.29, 19.46 and

25.22 ± 0.2 degrees 2-theta substantially as depicted in Figure 1 ; iii) a powder X-ray diffraction pattern having additional peaks at about 9.49, 10.33, 11.03, 13.10, 13.47, 15.04, 17.56, 20.51, 20.92, 21.40, 22.09 and 28.37 ± 0.2 degrees 2-theta substantially as depicted in Figure 1; iv) a DSC thermogram having an endotherm peak at about 144°C substantially as depicted in Figure 2; v) an IR spectrum substantially in accordance with Figure 3; and vi) an IR spectrum having absorption bands at about 3361, 2985, 2972, 2399, 1753, 1616, 1495, 1388, 1328, 1195, 1188, 1134, 1119, 1056, 1027, 929, 918, 733, 743 and 705 ± 2 cm- 1 .

7. A process for the preparation of fesoterodine mandelate salt of any one of claims 1 and 2, comprising: a) providing a first solution of fesoterodine free base in an organic solvent; b) combining the first solution with mandelic acid to produce a second solution containing fesoterodine mandelate; and c) isolating a solid state form of fesoterodine mandelate from the second solution. 8. The process of claim 7, wherein the organic solvent used in step-(a) is selected from the group consisting of alcohols, ketones, chlorinated hydrocarbons, esters, nitrites, polar aprotic solvents, and mixtures thereof. 9. The process of claim 8, wherein the organic solvent is selected from the group consisting of methanol, ethanol, n-propanol, isopropyi alcohol, isobutanol, n-butanol, tert-butanol,

amyi aloohol, isoamyl alcohol, hexanol, acetone, methyl ethyl ketone, methyl isobutyl ketone, methyl tert-butyt ketone, acetonitrile, ethyl acetate, methyl acetate, isopcopyl acetate, tot-butyl methyl acetate, ethyl formate, methylene chloride, ethylene dichloride, chloroform, N.N-dimethylformamide, N ^ N-dimethylacetamide, dimcthylsulfoxide, and mixtures thereof. 10. The process of claim 9, wherein the organic solvent is selected from the group consisting of methanol, ethanol, isopropyl alcohol, acetone, and mixtures thereof. 11. The process of claim 7, wherein the first solution in step-(a) is prepared by dissolving fesoterodine free base in the organic solvent at a temperature below a boiling temperature of the organic solvent 12. The process of claim 11, wherein the fesoterodine free base is dissolved in the organic solvent at a temperature of about 30 4 C to about 110°C. 13. The process of claim 7, wherein the first solution in step-(a) is prepared by reacting (R>2- (3^isopropylamino-1-pnenylpropyl)^hydroxymemylphenol with iaobutyry! chloride in a reaction inert solvent to produce a reaction mass containing crude fesoterodine free base; subjecting the reaction mass to washings, extractions or evaporations; and dissolving or extracting the fesoterodine free base residue in the organic solvent at a temperature of below boiling temperature of the organic solvent. 14. The process of claim 7, wherein the first solution in step-(a) is prepared by treating an acid addition salt of fesoterodine with a base to produce fesoterodine free base; and extracting or dissolving the fesoterodine free base in the organic solvent at a temperature below a boiling temperature of the organic solvent 15. The process of claim 7, wherein the first solution obtained in step-(a) is optionally stirred at a temperature of about 30°C to a boiling temperature of the organic solvent for at least 20 minutes. 16. The process of claim IS, wherein the solution is stirred at a temperature of about 40°C to a reflux temperature of the organic solvent for about 30 minutes to about 10 hours. 17. The process of claim 7, wherein the first solution obtained in step-(a) is optionally subjected to carbon treatment or silica gel treatment 18. The process of claim 7, wherein the mandelic acid used in step-(b) is L-( + )-mandelic acid or D-(-)-mandeHc acid. 19. The process of claim 18, wherein the mandelic acid is L-(+)-mandclic acid. 0. The process of claim 7, wherein the mandelic acid in step-(b) is used in a molar ratio of about 0.8S to 1.2 moles per mole of fesoterodine free base.

21. The process of claim 20, wherein (he mandelic acid is used in a molar ratio of about 0.95 to 1.05 moles per mole of fesoterodine free base.

22. The process of claim 7, wherein the combining in stcp-(b) is accomplished by adding the first solution to the mandelic acid or by adding the mandelic acid to the first solution. 23. The process of claim 22, wherein the addition is carried out at a temperature of about

3VC to about 100KJ.

24. The process of claim 22, wherein the reaction mass obtained after completion of the addition process is stirred at a temperature of about 30°C to about 100°C for at least 10 minutes. 25. The process of claim 24, wherein the reaction mass obtained after completion of the addition process is stirred at a temperature of about 30°C to about 100 4 C for at least 10 minutes to produce (he second solution. 26. The process of claim 25, wherein the reaction mass is stirred at a temperature of about

40"C to about 8O°C for about 30 minutes to about 8 hours. 27. The process of claim 7, wherein the second solution obtained in step-(b) is optionally subjected to carbon treatment or silica gel treatment.

28. The process of claim 7, wherein the second solution obtained in step-(b) is optionally cooled at a temperature of about 2O°C to about 40"C for about 30 minutes to about 10 hours. 29. The process of claim 7, wherein isolating in step-(c) is carried out by forcible or spontaneous crystallization.

30. The process of claim 29, wherein the forcible crystallization is initiated by cooling, seeding, partial removal of the solvent from the solution, by adding an anti-solvent to the solution, or a combination thereof. 31. The process of claim 30, wherein the crystallization is carried out by cooling (he solution at a temperature of below 20*C for at least 15 minutes.

32. The process of claim 31, wherein the crystallization is carried out by cooling the solution at about 0°C to about 20°C for about 30 minutes to about 20 hours.

33. The process of claim 32, wherein the crystallization is carried out by cooling the solution at about 5°C to about 15*C for about 1 hour to about 8 hours.

34. The process of claim 7, wherein die solid obtained in step-(c) is recovered by filtration, filtration under vacuum, decantation, centrifugation, filtration employing a filtration media of a silica gel or celite, or a combination thereof.

35. The process of claim 7, wherein the substantially pure solid state form of fcsotcrodine mandeiate obtained in step-(c) is further dried under vacuum or at atmospheric pressure, at a temperature of about 35°C to about 70°C.

36. The process of claim 7, wherein the solid state form of fesoterodine manddate obtained in steppe) has a purity of about 99% to about 99.95% as measured by HPLC.

37. Use of the solid state form of fesoterodine mandeiate in the process for preparation of fesoterodine or a pharmaceutically acceptable salt thereof.

38. Use of the fesoterodine mandeiate, produced according to die process of claim 7, in the process for preparation of fesoterodine or a pharmaceutically acceptable salt thereof. 39. A process for preparing substantially pure fesoterodine or a pharmaceutically acceptable salt thereof, comprising: a) contacting fesoterodine mandeiate with a base and/or an acid in a solvent to provide a reaction mass containing fesoterodine free base or a pharmaceutically acceptable salt thereof, and b) isolating highly pure fesoterodine free base or a pharmaceutically acceptable salt thereof from the reaction mass.

40. The process of claim 39. wherein the solvent used in step-<a) is selected from the group consisting of water, alcohols, ketones, chlorinated hydrocarbons, hydrocarbons, nitrites, esters, ethers, polar aprotic solvents, and mixtures thereof! 41. The process of claim 40, wherein die solvent is selected from the group consisting of water, methanol, ethanol, n-propanol, isopropyl alcohol, n-butanol, isobutanol, tert- butanol, amyi alcohol, hexanol, acetone, methyl ethyl ketone, methyl isobutyi ketone, methyl tcrt-butyl ketone, acctonitrile, ethyl acetate, methyl acetate, isopropyl acetate, lcrt- butyl methyl acetate, ethyl formate, methylene chloride, ethylene dichloride, chloroform, carbon tetrachloride, tetrahydrofuran, dioxane, diethyl ether, diisopropyl ether, monoglyme, diglymc, n-pentane, n-hcxane, n-heptane, cyclohexane, toluene, xylene, H v Ni<4imemy]fonnamide, N,N-duncthylacctamidc, dimethylsulfoxide, and mixtures thereof.

42. The process of claim 41, wherein die solvent is selected from the group consisting of water, methanol ethanol, isopropyl alcohol, acetone, methyl ethyl ketone, cyclohexane, diisopropyl ether, and mixtures thereof.

43. The process of claim 39, wherein the base used in stcp-(a) is an organic or inorganic base.

44. The process of claim 43, wherein the organic base is selected from the group consisting of triethyl amine, dimethyl amine and tert-butyl amine.

45. The process of claim 43, wherein the inorganic base is selected from the group consisting of aqueous ammonia, sodium hydroxide, calcium hydroxide, magnesium hydroxide, potassium hydroxide, lithium hydroxide, sodium carbonate, potassium carbonate, lithium carbonate, sodium tert-butoxide, sodium isopropoxide and potassium tert-butoxide. 46. The process of claim 39, wherein the acid used in step-(a) is an organic or inorganic acid.

47. The process of claim 46, wherein the acid is selected from the group consisting of hydrochloric acid, bydrobromic acid, hydroiodic acid, acetic acid, oxalic acid, fumaric acid, maleic acid, tartaric acid, di-p-toluoyi-L-(+)-tartaric acid, succinic acid, benzenesulfonic acid, toluenesulfbnic acid and methanesulfbnic acid 48. The process of claim 47, wherein the acid is hydrochloric acid or fumaric acid.

49. The process of claim 39, wherein the reaction in step-(a) is carried out at a temperature of -25°C to the reflux temperature of the solvent. 50. The process of claim 39, wherein isolating in step-(b) is carried out by forcible or spontaneous crystallization. 51. A pharmaceutical composition comprising solid state form of fesoterodine mandelate and one or more pharmaceutically acceptable exctpients. 52. The pharmaceutical composition of claim 51, wherein the pharmaceutical composition is a solid dosage form, an oral suspension, a liquid, a powder, an elixir, an aerosol, syrups or an injectable solution. S3. The pharmaceutical composition of claim 51 , wherein the solid state form of fesoterodine mandelate has a Dw particle size of less than or equal to about 500 microns. 54. The pharmaceutical composition of claim 53, wherein the 90 volume-% of the particles (Dw) have a size of less than or equal to about 300 microns; less man or equal to about 100 microns; less than or equal to about 60 microns; or less than or equal to about 15 microns. 55. A method of treating a patient suffering from diseases caused by urinary incontinence, gastrointestinal hyperactivity (irritable bowel syndrome) and other smooth muscle contractile conditions, comprising administering the solid state form of fesoterodine mandelate, or a pharmaceutical composition that comprises the solid state form of fesoterodine mandelate along with pharmaceutically acceptable excipients.

Description:

NOVEL MANDELATE SALT OF FESOTERODINE

CROSS REFERENCE TO RELATED APPLICATION

This application claims the benefit of priority to Indian provisional application No. 862/CHE/2008, filed on April 4, 2008, which is incorporated herein by reference in its entirety.

FIEIJ) OF THE DISCLOSURE

The present disclosure relates to novel salts of fesoterodine, process for preparation, pharmaceutical compositions, and method of treating thereof.

BACKGROUND

U.S. Patent No. 6,713,464 discloses a variety of 3,3-diphenylpropylaminc derivatives, processes for their preparation, pharmaceutical compositions comprising them, and method of use thereof. These compounds arc anti-muscarinic agents with superior pharmacokinetic properties compared to existing drugs such as oxybutynin and tolterodine and useful in the treatment of urinary incontinence, gastrointestinal hyperactivity (irritable bowel syndrome) and other smooth muscle contractile conditions. Among them, Fesoterodine 2-((lR)-3- p>is(l-nM^ylemyl)amino)-l-phenylpropyl]^hydroxymethylphen yl isobutyrate, is a new, potent and competitive muscarinic antagonist and useful in the potential treatment of urinary incontinence. Fesoterodine is represented by the following structural formula I:

Processes for the preparation of fesoterodine and its related compounds, and their pharmaceutically acceptable salts are disclosed in U.S. Patent Nos. 6,713,464 and 6,858,650; U.S. Patent Application No.2006/0270738 and PCT Publication No. WO 2007/138440.

According to the U.S. Patent No. 6,713,464 Bl (herein after referred to as the * 464 patent), fesoterodine is prepared by the reaction of (±)-6-bromo-4-phenylchroman-2-one with benzyl chloride in the presence of sodium iodide and anhydrous potassium carbonate in methanol and acetone to produce (±)-3K2-berιzyloxy-S-bπ>mophenyl)-3-phenylpropionic

acid methyl ester as a light yellow oil. This product is reduced with lithium aluminium hydride in tctrahydroiuran at room temperature (reaction time: 18 hours) to produce (±>-3-(2- bcnzyloxy-5-broinophcnyl)-3-Dhenylpropan-1-ol, which is then treated with p- toluenesulphonyi chloride in the presence of pyridine in dichloromcthane to afford (±)- toIuenc-4-sulphonic acid 3<2-bcnzyloxy-5-broinophenyl)-3-phenylpropyl ester. This product is then reacted with N,N-diisopropylamine in acetonitrile at reflux temperature (i.e., 75-8O°C) for 97 hours to produce (±)-(3K2-bcnzyloxy-5-brcmκ)phcny1)-3-phcnylρτopyl]- diisopropylamine as a brown and viscous syrup. This product is resolved to produce (R)-[3- (2-benzyloxy-S-biomophertyl)-3-phenylpiopyl]^ii8opropytaniin c t which is men subjected to Grignard reaction with ethylbromide and magnesium in the presence of solid carbon dioxide in tetrahydroruran to produce (R)^ben2^oxy>3K3Htiisopropylamirκ>-l-phenylpropyl)- benzoic acid hydrochloride, followed by esteriftcation with methanol in the presence of sulphuric acid to produce (R)^benzyloxy-3^3^ii8opropylamirκ>-l-phenylpropyl>ben zoic acid methyl ester. This product is reduced with lithium aluminium hydride (reaction time: 18 hours) to produce (RH4-beri^oxy-3K3^isopnφylamino-l-phenylpτDpyl)-phenyl]- mcthanol, which is then subjected to deprolection with Raney-Nickel to produce (R)-2-(3- diisopropylamino-l-phenylpropyl)^hydroxyrncthylphenol, followed by condensation with isobutyryl chloride in an inert solvent in the presence of a base to produce fesoterodine.

While the *464 patent mentions that some of the disclosed compounds which can form a salt with physiologically acceptable organic and inorganic acids such as hydrochloride and hydrobromide, only the hydrochloride salts of the disclosed compounds have been prepared.

U.S. Patent No. 6,858,650 (herein after referred to as the '650 patent) describes various acid addition salts of 3,3-dipbenylpropylamine derivatives such as hydrochloric acid, hydrobromic acid, phosphoric acid, sulphuric add, nitric add, acetic add, propionic add, palmitic add, stearic add, malcic add, tumeric add, oxalic add, succinic add, DL-malic add, L-(-)-malic add, D-(+)-τnalic acid, DL-tartaric add, L-(+)-tartaric add, D-(-)-tartaric add, dtric acid, L-aspartic acid, M+)-βscorbic add, D-( + ^glucuronic acid, 2-oxopropionic acid (pyruvic add), furan-2-carboxylic add (mudc add), benzoic add, 4-hydroxybenzoic add, salicyclic acid, vanillic add, 4-hydroxycinammic add, gallic acid, hippuric add, aceturic acid, phloretinic add, phmalic add, methanesulfonic add or orotic add. Although the '650 patent teaches several physiologically compatible add addition salts, only hydrogen fumarate and hydrochloride hydrate salts of the disdosed compounds have been prepared. There remains a need for new addition salts of fesoterodine.

SUMMARY

The manddate salt of fesoterodine has not been reported, isolated, or characterized in the literature. The present inventors have surprisingly and unexpectedly found that mandelate salt of 24(lR>3^s(l4nethylethyl)amiiκ>]-l-r4ie^ isobutyrate, i.e., fesoterodine manddate, can be isolated in a pure solid state form.

It has also been found that the solid state form of fesoterodine manddate is useful intermediate in the preparation of fesoterodine free base, or a pharmaceuHcally acceptable salt thereof, preferably fesoterodine fumarate, in high purity. The manddate salt of fesoterodine has good flow properties and is far more stable than the prior art salts at room temperature, enhanced temperature, at relative high humidities, in aqueous media. The novd mandelate salt is suitable for formulating fesoterodine.

In one aspect, a novd manddate salt of fesoterodine is provided. In another aspect, fesoterodine mandelate in a solid state form is provided. In another aspect, the solid state form of fesoterodine manddate exists in an amorphous form or a crystalline form. In yet another aspect, the solid state form of fesoterodine manddate exists in an anhydrous and/or solvent-free form or as a hydrate and/or a solvate form.

In another aspect, encompassed herein is a process for preparing the fesoterodine manddate salt comprising contacting fesoterodine free base with manddic acid in a suitable solvent under suitable conditions, and isolating the fesoterodine manddate as a solid.

In another aspect, encompassed herein is a process for preparing substantially pure fesoterodine free base or a pharmaceutically acceptable salt thereof by using the solid state form of fesoterodine manddate salt disclosed herein. In another aspect, provided herein is a method for treating a patient suffering from diseases caused by urinary incontinence, gastrointestinal hyperactivity (irritable bowd syndrome) and other smooth muscle contractile conditions, comprising administering the solid state form of fesoterodine manddate, or a pharmaceutical composition that comprises the solid state form of fesoterodine manddate along with pharmaceutically acceptable excipients.

In another aspect, provided herein is a pharmaceutical composition comprising solid state form of fesoterodine mandelate, and one or more pharmaceutically acceptable excipients.

In still another aspect, provided herein is a pharmaceutical composition comprising a solid state form of fesoterodinc mandclate made by the process disclosed herein, and one or more pharmaceutically acceptable excipients.

In still further aspect, encompassed is a process for preparing a pharmaceutical formulation comprising combining a solid state form of fesoterodinc mandelatc with one or more pharmaceutically acceptable excipients.

In another aspect, the solid state form of fesoterodine mandelate disclosed herein for use in the pharmaceutical compositions has a 90 volume-percent of the particles (D 90 ) having a size of less than or equal to about 500 microns, specifically less than or equal to about 300 microns, more specifically less than or equal to about 100 microns, still more specifically less than or equal to about 60 microns, and most specifically less man or equal to about IS microns.

BRIEF DESCRIPTION OF THE DRAWINGS Figure 1 is a characteristic powder X-ray diffraction (XRD) pattern of fesoterodine mandelate.

Ftøpre 2 is a characteristic differential scanning calorimctric (DSC) thermogram of fesoterodine mandelate. Figure 3 is a characteristic infra red (IR) spectrum of fesoterodine mandelate.

DETAILED DESCRIPTION

Disclosed herein is the unexpected discovery that fesoterodine mandelate can be obtained as a solid.

In the formulation of drug compositions, it is important for the active pharmaceutical ingredient to be in a form in which it can be conveniently bandied and processed. Convenient handling is important not only from the perspective of obtaining a commercially viable manufacturing process, but also from the perspective of subsequent manufacture of pharmaceutical formulations (e.g., oral dosage forms such as tablets) comprising the active pharmaceutical ingredient Chemical stability, solid state stability, and "shelf life" of me active pharmaceutical ingredient are important properties for a pharmaceutically active compound. The active pharmaceutical ingredient, and compositions containing it, should be capable of being effectively stored over appreciable periods of time, without exhibiting a significant change in the physico-chemical characteristics of the active pharmaceutical ingredient, e.g., its chemical

composition, density, hygrosoopicity and solubility. Thus, in the manufacture of commercially viable and pharmaceutically acceptable drug compositions, it is important, wherever possible, to provide the active pharmaceutical ingredient in a stable form.

New salt forms of a pharmaceutical agent can former the development of formulations for the treatment of illnesses. For instance, solid forms of a compound are known in the pharmaceutical arts to affect, for example, the solubility, dissolution rate, bioavailability, chemical and physical stability, flowabiliry, fractability, and compressibility of the compound, as well as the safety and efficacy of drug products based on the compound.

The discovery of novel sails in solid state forms, including amorphous and crystalline forms, of pharmaceutically useful compound provides a new opportunity to improve the performance characteristics of a pharmaceutical product, h also adds value to the material that a formulation scientist can use Ae same for designing, for example, a pharmaceutical dosage form of a drug with a targeted release profile or other desired characteristic.

A novel mandelate salt of fesoterodine and its solid state forms have now been discovered.

The mandelate salt of fesoterodine has the following advantages when compared to die fumarate salt: i) during filtration, the fumarate salt absorbs moisture, while mandelate does not absorb moisture; and H) isolation of the mandelate salt is very easy and it takes a shorter time period; alcoholic solvents can be used for isolation, whereas the isolation of fumarate salt involves the use of a solvent mixture containing alcohol and diisopropyl ether, and during isolation, the fumarate salt initially separates as a sticky mass and then slowly becomes solid over a period. According to one aspect, provided herein is a novel manddate salt of 2-[(lR)-3-

|>is(l-meAyl<Hhyl)aminoJ-1-phenylpropylJ^hyό^xymet hylphcnyl isobutyrate, i.e., fesoterodine manddate.

According to another aspect, there is provided a novel and stable solid state form of fesoterodine mandelate. In one embodiment, the solid state form of fesoterodine mandelate is an amorphous form or a crystalline form.

In another embodiment, the solid state form of fesoterodine mandelate exists in an anhydrous and/or solvent-free form or as a hydrate and/or a solvate form. Such solvated or hydrated forms may be present as hemi-, mono-, sesqui-, di- or tri- solvates or hydrates.

Solvates and hydrates may be formed as a result of solvents used during the formation of the fesoterodine mandelate becoming imbedded in the solid lattice structure. Because formation of the solvates and hydrates occurs during the preparation of fesoterodine mandelate, formation of a particular sorvated or hydrated form depends greatly on the conditions and method used to prepare the salt. Solvents should be phaπnaceuticaUy acceptable.

According to another aspect, the solid state form of fesoterodine mandelate is characterized by at least one, or more, of the following properties: i) a powder X-ray diffraction pattern substantially in accordance with Figure 1 ; ii) a powder X-ray diffraction pattern having peaks at about 4.98, 10.0, 14.29, 19.46 and 25.22 ± 0.2 degrees 2-theta substantially as depicted in Figure 1 ; in) a powder X-ray diffraction pattern having additional peaks at about 9.49, 10.33, 11.03, 13.10, 13.47, 15.04, 17.56, 20.51, 20.92, 21.40, 22.09 and 28.37 ± 0.2 degrees 2- theta substantially as depicted in Figure 1 ; iv) a DSC thermogram having an endotherm peak at about 144°C substantially as depicted in Figure 2; v) an IR spectrum substantially in accordance with Figure 3; and/or vi) an IR spectrum having absorption bands at about 3361, 2985, 2972, 2399, 1753, 1616, 1495, 1388, 1328, 1195, 1188, 1134, 1119, 1056, 1027, 929, 918, 733, 743 and 705 ± 2 cm *1 . The solid fesoterodine mandelate is stable, consistently reproducible, and is particularly suitable for bulk preparation and handling. Moreover, the solid state form of fesoterodine mandelate is a useful intermediate in the preparation of fesoterodine tree base or a pharmaceutically acceptable salt thereof, preferably fesoterodine fumarate, in high purity.

The solid state form of fesoterodine mandelate has good flow properties and is far more stable than the prior art salts at room temperature, enhanced temperature, at relative high humidities, and in aqueous media. The novel solid state form of fesoterodine mandelate is suitable for formulating fesoterodine.

According to another aspect, there is provided a process for the preparation of fesoterodine mandelate salt, comprising: a) providing a first solution of fesoterodine free base in an organic solvent; b) combining the first solution with mandelic acid to produce a second solution containing fesoterodine mandelate; and c) isolating solid state form of fesoterodine mandelate from the second solution.

Hie fcsotcrodinc mandelate obtained by the process disclosed herein is optionally converted into fesoterodine free base or a pharmaceutically acceptable salt thereof.

The process can produce solid state form of fesoterodine mandelate in substantially pure form. The term ''substantially pure solid state form of fesoterodine mandelate" refers to the solid state form of fesoterodine mandelate having a purity of greater man about 99 wt%, specifically greater than about 99.S wt%, more specifically greater than about 99.8 wt%, and still more specifically greater than about 99.9 wt%. The purity is preferably measured by High Performance Liquid Chromatography (HPLC). For example, the purity of solid state form of fesoterodine mandelate obtained by the process disclosed herein can be about 99% to about 99.95%, or about 99.5% to about 99.99%, as measured by HPLC.

In one embodiment, the process disclosed herein provides stable crystalline form of fesoterodine mandelate. The term "stable crystalline form" refers to stability of the crystalline form under the standard temperature and humidity conditions of testing of pharmaceutical products, wherein the stability is indicated by preservation of the original polymorphic form.

Exemplary organic solvents used in step-(a) include, but are not limited to, alcohols, ketones, chlorinated hydrocarbons, esters, rάtriles, polar aprotic solvents, and mixtures thereof. The term solvent also includes mixtures of solvents. In one embodiment, the organic solvent is selected from Ae group consisting of methanol, ethanol, n-propanol, isopropyl alcohol, isobutanoL n-butanol, tert-butanot, amyl alcohol, isoamyl alcohol, hexanol, acetone, methyl ethyl ketone, methyl isobutyl ketone, methyl tert-butyl ketone, acetonitrile, ethyl acetate, methyl acetate, isopropyl acetate, tert- butyl methyl acetate, ethyl formate, methylene chloride, ethylene dichloride, chloroform, N.N-dimethylfbrmamide, N,N-dimethytacetamidc, dimethylsulfoxide, and mixtures thereof; more specifically the solvent is selected from the group consisting of methanol, ethanol, isopropyl alcohol, acetone, and mixtures thereof; and most specifically the solvent is isopropyl alcohol.

Step-(β) of providing a first solution of fesoterodine free base includes dissolving fesoterodine free base in the organic solvent, or obtaining an existing solution from a previous processing step.

In one embodiment, the fesoterodine free base is dissolved in the organic solvent at a temperature of below boiling temperature of the solvent used, specifically at about 30°C to about 110°C, and more specifically at about 40*C to about 80*C.

In another embodiment, the first solution in step-(a) is prepared by reacting (R>2-<3- diisopropyiamiro-l-phenylpropyO^hy^ with isobutyryl chloride in a reaction inert solvent under suitable conditions to produce a reaction mass containing crude feβoterodine free base, followed by usual work up such as washings, extractions, evaporations, etc In one embodiment, the work-up includes dissolving or extracting die resulting fesoterodine free base residue in the organic solvent at a temperature of below boiling temperature of the solvent used, specifically at about 3O°C to about 110 19 C, and more specifically at about 40°C to about 8O°C.

Exemplary reaction inert solvents suitable for facilitating the reaction between (R>2- (3wliisoprcφylamino-1-phenylpropyl)^hvόVoxvmethylphenol and isobutyryl chloride include, but are not limited to, water, alcohols, ketones, cyclic ethers, aliphatic ethers, hydrocarbons, chlorinated hydrocarbons, nitrites, esters, polar aprotic solvents, and the like, and mixtures thereof. In one embodiment, the solvent is selected from the group consisting of water, methanol, ethanol, n-propβnol, isopropanol, n-butanol, isobutanol, tert-butanol, amyi alcohol, hexanol, acetone, methyl ethyl ketone, methyl isobutyl ketone, methyl tert- butyl ketone, acctonitrile, ethyl acetate, methyl acetate, isopropyl acetate, tert-butyl methyl acetate, ethyl formate, methylene chloride, dichioroethane, chloroform, carbon tetrachloride, tetrahydrofuran, dioxane, diethyl ether, diisopropyl ether, monoglyme, diglyme, n-pcntane, n- hexane, n-heptane, cyclohexane, toluene, xylene, N,N-dimethylfbrmamide, N,N- dimethylacetamide, dimethylsulfόxide, and mixtures thereof A specific reaction inert solvent is methylene chloride.

Alternatively, the first solution in step-(a) is prepared by treating an acid addition salt of fesoterodine with a base to liberate fesoterodine free base, followed by extracting or dissolving the fesoterodine free base in the organic solvent at a temperature of below boiling temperature of the solvent used, specifically at about 30°C to about 110°C, and more specifically at about 40°C to about 80°C.

In another embodiment, the acid addition salt of fesoterodine is derived from a therapeutically acceptable acid such as hydrochloric acid, hydrobromic acid, acetic acid, propionic acid, sulfuric acid, nitric acid, phosphoric add, succinic acid, maldc acid, fumaric acid, citric acid, glυtaric add, citraconic add, ghitaconic add, tartaric add, malic add, and ascorbic add. A spedfic add addition salt is fesoterodine fumarate.

The treatment of an add addition salt with a base is carried out in a solvent A wide variety of solvents such as chlorinated solvents, alcohols, ketones, hydrocarbon solvents, esters, ether solvents etc., can be used.

In one embodiment, the base is an organic or inorganic base. Specific organic bases are triethyl amine, dimethyl amine and tert-butyl amine.

In another embodiment, the base is an inorganic base. Exemplary inorganic bases include, but are not limited to, aqueous ammonia; hydroxides, carbonates and bicarbonates of alkali or alkaline earth metals. Specific inorganic bases are aqueous ammonia, sodium hydroxide, calcium hydroxide, magnesium hydroxide, potassium hydroxide, lithium hydroxide, sodium carbonate, potassium carbonate, lithium carbonate, sodium tert-butoxide, sodium isopropoxide and potassium tert-butoxide, and more specifically sodium hydroxide, potassium hydroxide, sodium carbonate and potassium carbonate. The first solution obtained in stcp-(a) is optionally stirred at a temperature of about

30°C to the reflux temperature of the solvent used for at least 20 minutes, and specifically at a temperature of about 40°C to the reflux temperature of the solvent used for about 30 minutes to about 10 hours.

The first solution obtained in step-(a) is optionally subjected to carbon treatment or silica gel treatment The carbon treatment or silica gel treatment is carried out by methods known in the art, for example, by stirring the solution with finely powdered carbon or silica gel at a temperature of below about 70°C for at least 1 S minutes, specifically at a temperature of about 40 4 C to about 70 4 C for at least 30 minutes; and filtering the resulting mixture through hyflo to obtain a filtrate containing fesoterodine free base by removing charcoal or silica gel. Preferably, finely powdered carbon is an active carbon. A specific mesh size of silica gel is 40-500 mesh, and more specifically 60-120 mesh.

In one embodiment, the mandelic acid used in stcp-(b) is an optically active manddic acid, i.e., L-(+)-mandelic acid or D-(-)-mandelic acid. A specific optically active mandelic acid is L-(+)-mandclic acid. In another embodiment, the mandelic acid used in 8tep-(b) in the molar ratio of about

0.85 to 1.2 moles, specifically about 0.95 to 1.05 moles, per mole of fesoterodine free base.

Combining of the first solution with mandelic acid in step-(b) is done in a suitable order, for example, the first solution is added to the mandelic acid, or alternatively, the mandelic acid is added to the first solution. The addition is, for example, carried out drop wise or in one portion or in more than one portion. The addition is specifically carried out at a temperature of about 30 4 C to about 100°C, more specifically at about 40 4 C to about 90°C, and most specifically at about 40°C to about 80 4 C under stirring. After completion of addition process, the resulting mass is stirred at a temperature of about 3O°C to about 100°C

for at least 10 minutes and specifically at a temperature of about 4O°C to about 80*C for about 30 minutes to about 8 hours to produce a second solution.

The second solution obtained in step-(b) is optionally subjected to carbon treatment or silica gel treatment. The carbon treatment or silica gel treatment is carried out by methods known in the art, for example, by stirring the solution with finely powdered carbon or silica gel at a temperature of below about 70°C for at least IS minutes, specifically at a temperature of about 4O°C to about 70°C for at least 30 minutes; and filtering the resulting mixture through hyflo to obtain a filtrate containing fesotcrodinc mandelate by removing charcoal or silica gel. Preferably, finely powdered carbon is an active carbon. A specific mesh size of silica gel is 40*500 mesh, and more specifically 60-120 mesh.

The second solution obtained in step-(b) is optionally cooled at a temperature of about 2O 41 C to about 4O 41 C, and specifically at a temperature of about 25°C to about 30°C while stirring. In one embodiment, the stirring is performed for at least about 30 minutes, and specifically for about 30 minutes to about 10 hours. The isolation of pure fesoterodine mandelate in βtcp-(c) is carried out by forcible or spontaneous crystallization.

Spontaneous crystallization refers to crystallization without the help of an external aid such as seeding, cooling etc., and forcible crystallization refers to crystallization with the help of an externa) aid. Forcible crystallization may be initiated by a method usually known in the art such as cooling, seeding, partial removal of the solvent from the solution, by adding an anti-solvent to the solution, or a combination thereof.

In one embodiment, the crystallization is carried out by cooling the solution at a temperature of below 20°C for at least 15 minutes, specifically at about O°C to about 20°C for about 30 minutes to about 20 hours, and more specifically at about 5°C to about 15°C for about 1 hour to about 8 hours.

The substantially pure solid state form of fesoterodine mandelate obtained in step-(c) may be recovered by methods such as filtration, filtration under vacuum, decatitation, centrifugation, or a combination thereof. In one embodiment, solid state form of fesoterodine mandelate is isolated by filtration employing a filtration media of, for example, a silica gel or cclitc

The pure solid state form of fesoterodine mandelate obtained by above process may be further dried in, for example, a Vacuum Tray Dryer, Rotocon Vacuum Dryer, a Vacuum Paddle Dryer or a pilot plant Rota vapor, to further lower residual solvents. Drying can be

earned out under reduced pressure until the residual solvent content reduces to the desired amount such as an amount that is within the limits given by the International Conference on Harmonization of Technical Requirements for Registration of Pharmaceuticals for Human Use r OH guidelines.

S In one embodiment, the drying is carried out at atmospheric pressure or reduced pressures, such as below about 200 mm Hg, or below about SO mm Hg, at temperatures such as about 3S 0 C to about 70°C. The drying can be carried out for any desired time period mat achieves the desired result, such as about 1 to 20 hours. Drying may also be carried out for shorter or longer periods of time depending on the product specifications. Temperatures and 10 pressures will be chosen based on the volatility of the solvent being used and the foregoing should be considered as only a general guidance. Drying can be suitably carried out in a tray dryer, vacuum oven, air oven, or using a fluidized bed drier, spin flash dryer, flash dryer and the like. Drying equipment selection is well within the ordinary skill in the art

The purity of the fesoterodine manddate obtained by the process disclosed herein is

I S greater than about 99%, specifically greater man about 99.5%, more specifically greater than about 99.9%, and most specifically greater than about 99.95% as measured by HPLC. For example, the purity of the fesoterodinc mandelate can be about 99% to about 99.95%, or about 99.5% to about 99.99%.

Fesoterodine and pharmaceutically acceptable salts of fesoterodine can be prepared in

20 high purity by using the substantially pure fesoterodine mandelate obtained according to the process disclosed herein.

According to another aspect, there is provided a process for preparing substantially pure fesoterodine free base or a pharmaceutically acceptable salt thereof; comprising: a) contacting fesoterodine manddate with a base and/or an acid in a solvent to 25 provide a reaction mass containing fesoterodine free base or a pharmaceutically acceptable salt thereof; and b) isolating highly pure fesoterodine free base or a pharmaceutically acceptable salt thereof from the reaction mass.

Exemplary solvents used in step-(a) include, but are not limited to, water, alcohols, 30 ketones, chlorinated hydrocarbons, hydrocarbons, nitriles, esters, ethers, polar aptotic solvents, and mixtures thereof. The term solvent includes mixtures of solvents.

In one embodiment, the solvent is sdected from the group consisting of water, methanol, ethanol, n-propanol, isopropyl alcohol, n-butanol, isobutanol, tert-butanol, amyl alcohol, hβxanol, acetone, methyl ethyl ketone, methyl isobutyl ketone, methyl tcrt-butyl

ketone, acetonitrile, ethyl acetate, methyl acetate, isopropyl acetate, tert-butyl methyl acetate, ethyl formate, methylene chloride, ethylene dichloride, chloroform, carbon tetrachloride, tetrahydrofuran, dioxane, diethyl ether, diisopropyi ether, monoglyme, diglymc, n-pentane, n- hexane, n-heptanc, cyclohexane. toluene, xylene, N^-dimcthylfbrmamidc, N,N- dimcthylacetamide, dimethyiaulfoxide, and mixtures thereof; more specifically the solvent is selected from the group consisting of water, methanol, ethanol, isopropyl alcohol, acetone, methyl ethyl ketone, methyl isobutyl ketone, methylene chloride, n-pentane, n-hexane, n- hcptane, cyclohexane, toluene, diethyl ether, diisopropyl ether and mixtures thereof; and most specifically the solvent is selected from the group consisting of water, methanol, ethanol, Lsopropyi alcohol, acetone, methyl ethyl ketone, cyclohexane, diisopropyl ether, and mixtures thereof.

In one embodiment, the base used in step-<a) is an organic or inorganic base. Exemplary organic bases include, but arc not limited to, triethyl amine, dimethyl amine and tert-butyl amine. Ih another embodiment, the base is an inorganic base. Exemplary inorganic bases include, but are not limited to, aqueous ammonia; hydroxides, carbonates and bicarbonates of alkali or alkaline earth metals. Specific inorganic bases are aqueous ammonia, sodium hydroxide, calcium hydroxide, magnesium hydroxide, potassium hydroxide, lithium hydroxide, sodium carbonate, potassium carbonate, lithium carbonate, sodium tert-butoxide, sodium isopropoxide and potassium tert-butoxide, and more specifically sodium hydroxide, potassium hydroxide, sodium carbonate and potassium carbonate.

If the reaction in step-(a) is carried out in the presence of a base, the product obtained is fesoterodine base, which can be converted in-situ into a pharmaceutically acceptable acid addition salt of fesoterodine using a suitable add in a suitable solvent. In one embodiment, the pharmaceutically acceptable acid addition salts of fesoterodine can be obtained directly in step-(a) by carrying out the reaction in the presence of a suitable acid.

Exemplary acids used in stcp-<a) include, but are not limited to, organic and inorganic adds, for example, hydrochloric acid, hydrobromic acid, hydroiodic add, acetic acid, oxalic add, fumaric add, maleic add, tartaric add, φ-p-toluoyi-M+Vuutaric add, succinic acid, benzenesulfonic add, toluenesulfonic add and methanesulfonic acid; and more preferable adds are hydrochloric add and fumaric add.

The reaction in step-(a) is carried out at a temperature of -25°C to the reflux temperature of the solvent used, spedffcally at a temperature of 0°C to the reflux temperature

of the solvent used, more specifically at a temperature of 25°C to the reflux temperature of (he solvent used, and most specifically at the reflux temperature of the solvent used.

Ae used herein, "reflux temperature" means the temperature at which the solvent or solvent system refluxes or boils at atmospheric pressure. The reaction mass containing the pure fesoterodine or a pharmaceutically acceptable salt thereof may be subjected to usual work up such as washings, extractions, evaporations etc., followed by isolation from a suitable organic solvent by methods known in the art

The isolation of highly pure fesoterodine or a pharmaceutically acceptable salt thereof in step-(b) is carried out by forcible or spontaneous crystallization. In one embodiment, the crystallization is carried out by cooling the solution at a temperature of below 30°C for at least 1 S minutes, specifically at about O°C to about 3O°C for about 30 minutes to about 20 hours, and more specifically at about O°C to about 2S°C for about I hours to about 5 hours.

The pure fesoterodine or a pharmaceutically acceptable salt thereof obtained by above process is recovered and optionally further dried as described above.

Exemplary pharmaceutically acceptable salts of fesoterodine include hydrochloride, hydrobromidc, sulfate, fumarate and tartarate, and more preferably fumarate.

The purity of the fesoterodine or a pharmaceutically acceptable salt thereof obtained by the process disclosed herein is of greater than about 99%, specifically greater than about 99.5%, more specifically greater than about 99.9%, and most specifically greater than about 99.95% as measured by HPLC. For example, the purity of the fesoterodine or a pharmaceutically acceptable salt thereof can be about 99% to about 99.95%, or about 99.5% to about 99.99%.

Further encompassed herein is the use of the solid state form of fesoterodine mandelate for the manufacture of a pharmaceutical composition together with a pharmaceutically acceptable carrier.

A specific pharmaceutical composition of the solid state form of fesoterodine mandelate is selected from a solid dosage form and an oral suspension.

In one embodiment, the solid state form of fesoterodine mandelate has a Dw particle size of less than or equal to about 500 microns, specifically less than or equal to about 300 microns, more specifically less than or equal to about 100 microns, still more specifically less than or equal to about 60 microns, and most specifically less than or equal to about IS microns.

Ia another embodiment, the particle sizes of the solid state form of fesotcrodine mandelatc are produced by a mechanical process of reducing the size of particles which includes any one or more of cutting, chipping, crushing, milling, grinding, micronizing, trituration or other particle size reduction methods known in the art, to bring the solid state form to the desired particle size range.

According to another aspect, there is provided pharmaceutical compositions comprising solid state form of feaoterodine manddate salt and one or more pharmaceutically acceptable excipients.

According to another aspect, mere is provided pharmaceutical compositions comprising the solid state form of fesoterodinc manddate prepared according to processes disclosed herein and one or more pharmaceutically acceptable excipients.

According to another aspect, mere is provided a process for preparing a pharmaceutical formulation comprising combining the solid state form of fesoterodine manddate prepared according to processes disclosed herein, with one or more pharmaceutically acceptable excipients.

According to another aspect, there is provided a method for treating a patient suffering from diseases caused by urinary incontinence, gastrointestinal hyperactivity (irritable bowel syndrome) and other smooth muscle contractile conditions, comprising administering the solid state form of fesoterodine manddate, or a pharmaceutical composition that comprises the solid state form of fesoterodine manddate along with pharmaceutically acceptable excipients.

Yet in another embodiment, pharmaceutical compositions comprise at least a therapeutically effective amount of solid state form of fesoterodine manddate. Such pharmaceutical compositions may be administered to a mammalian patient in a dosage form, e.g., solid, liquid, powder, elixir, aerosol, syrups, injectable solution, etc. Dosage forms may be adapted for administration to the patient by oral, buccal, parenteral, ophthalmic, rectal and transdermal routes or any other acceptable route of administration. Oral dosage forms include, but are not limited to, tablets, pills, capsules, syrup, troches, sachets, suspensions, powders, lozenges, dixirs and the like. The solid state form of fesoterodine manddate may also be administered as suppositories, ophthalmic ointments and suspensions, and parenteral suspensions, which are administered by other routes.

The pharmaceutical compositions further contain one or more pharmaceutically acceptable excipients. Suitable excipients and the amounts to use may be readily determined by the formulation scientist based upon experience and consideration of standard procedures

and reference works in the field, e.g., the buffering agents, sweetening agents, binders, diluents, fillers, lubricants, wetting agents and disintegrants described hereinabove.

In one embodiment, capsule dosage forms contain solid state form of fesotcrodine mandelate within a capsule which may be coated with gelatin. Tablets and powders may also be coated with an enteric coating. Suitable enteric coating include phthalic acid cellulose acetate, hydroxypropyhnethyl cellulose phthalate, polyvinyl alcohol phthalate, carboxy methyl ethyl cellulose, a copolymer of styrenc and maleic acid, a copolymer of methacrylic acid and methyl methacrytate, and like materials, and if desired, the coating agents may be employed with suitable plasticizers and/or extending agents. A coated capsule or tablet may have a coating on the surface thereof or may be a capsule or tablet comprising a powder or granules with an enteric-coating.

Tableting compositions may have lew or many components depending upon the tableting method used, the release rate desired and other factors. For example, the compositions described herein may contain diluents such as cellulose-derived materials like powdered cellulose, microcrystalline cellulose, microfine cellulose, methyl cellulose, ethyl cellulose, hydroxyethyl cellulose, hydroxypropyl cellulose, hydroxypropylmethyl cellulose, carboxymethyl cellulose salts and other substituted and unsubstituted celluloses; starch; pregelatinia∞d starch; inorganic diluents such calcium carbonate and calcium diphosphate and other diluents known to one of ordinary skill in the art Yet other suitable diluents include waxes, sugars (e.g. lactose) and sugar alcohols such as matmitol and sorbitol, acrylate polymers and copolymers, as well as pectin, dextrin and gelatin.

Other exdpients include binders, such as acacia gum, pregclatinized starch, sodium alginate, glucose and other binders used in wet and dry granulation and direct compression tableting processes; disintegrants such as sodium starch glycolate, crospovidone, low- substituted hydroxypropyl cellulose and others; lubricants like magnesium and calcium stearate and sodium stearyt fomarate; flavorings; sweeteners; preservatives; pharmaceutically acceptable dyes and glidants such as silicon dioxide.

INSTRUMENTAL DETAILS: X-IUv Powder Diffraction (P-XRD):

The X-Ray powder diffraction was measured by an X-ray powder Diftractomcter equipped with CuKα-radiations (4OkV, 40 mA) in wide-angle X-ray Diffractomcter of BRUKER axs,

D8 ADVANCE. The sample was analyzed using the following instrument parameters: measuring range∞ 3-45° 2-theta; step width-O.01579°; and measuring time per step « 0.11 sec.

Differential Srenntwg CfrfφriBWtrv flJSCI* DSC (Differential Scanning Calorimetry) measurements were performed with a Differentia) Scanning Calorimeter (Diamond DSC, Perkm-Elmcr) at a scan rate of 5°C per minute. The nitrogen gas purge was at 40 ml/min. The instrument was calibrated for temperature and heat flow using indium as standards. The samples were encapsulated in to closed aluminium pans without hole subsequently crimped to ensure a tight seal. Data acquisition and analysis were performed using pyris software.

Imfra-Red Spectroscopy (FT-IR):

FT-IR spectroscopy was carried out with a Perktn Elmer Spectrum 100 series spectrometer. For the production of the KBr compacts approximately 2 mg of sample was powdered with 200 mg of KBr. The spectra were recorded in transmission mode ranging from 3800 to 650 cm .

The following examples are given for the purpose of illustrating the present disclosure and should not be considered as limitation on the scope or spirit of the disclosure.

EXAMPLES Example 1

Preparation of Fesoterodine Maaddate

(R)-2^3-Diisopπ>py]amino-1-phenylpropyl>^hyό^xymediy lphonol (100 g) was added to methylene chloride (1200 ml) at 25 - 30°C under stirring and the resulting mass was cooled to -10°C. A solution of isobutyryl chloride (33 g) in methylene chloride (800 ml) was added drop wise to the above mass at -10°C to -5°C over a period of 1 hour and the resulting mass was stirred for 30 minutes at the same temperature. The temperature of the mass was raised to 0°C followed by the addition of water (400 ml). The resulting mass was stirred for 5 minutes. The organic layer was separated followed by the addition of aqueous sodium bicarbonate solution (28.5 g in 400 ml water) and men stirred for 15 minutes. The resulting organic layer was separated and washed with water (500 ml). The organic layer was distilled completely under vacuum followed by the addition of isopropyl alcohol (500 ml). The temperature of the resulting mass was raised to 55°C followed by the addition of M + )- mandelic add (42.5 g) and stirred for 30 minutes at the same temperature. The resulting mass was cooled to 25-30°C and then stirred for 6 hours at the same temperature. The

resulting mass was farther cooled 10-15°C and stirred for 1 hour. The precipitated solid was filtered, washed with chilled isopropyl alcohol (100 ml) and then dried the product under vacuum at 50°C to produce 85 g of fesoterodine mandelate. (Purity by HPLC: 99.72%).

Example 2

Preparation of Fetoterodine Fumarate

Fesoterodine mandelate (100 g, obtained according to example 1) was added to methylene chloride (500 ml) at 25-30°C. The resulting mixture was stirred for 10 minutes and then washed with 10% sodium hydroxide solution (200 ml). The resulting layers were separated and the organic layer was washed with water (200 ml). The organic layer was separated and dried over sodium sulfate (10 g) followed by distillation of methylene chloride under vacuum to produce fcsoterodinc as oily mass. This oily mass was followed by the addition of methyl ethyl ketone (170 ml) at 25-30°C, stirred for 10 minutes and then heated to 80°C. Fumaric acid (21.5 g) was added to the resulting mass, stirred for 1 hour at 80°C followed by the drop wise addition of cyclohexanc (70 ml) at 80°C and stirred for 1 hour. The resulting mass was slowly cooled to 25-30°C and stirred for 12 hours at the same temperature. The resulting mass was then cooled to 0-5°C and stirred for 12 hours at 0-5°C. The separated solid was filtered, washed with the mixture of cyclohexane (135 ml) and methyl ethyl ketone (15 ml), and then dried under vacuum at 45-50°C to produce 80 g of fesoterodine fumarate (Purity by HPLC: 99.76%)

Example 3 Preparation of Fesoterodine Famarate

Fesoterodine mandelate (100 g, obtained according to example 1) was added to methylene chloride (500 ml) at 25-30°C. The resulting mixture was stirred for 10 minutes and then washed with aqueous sodium carbonate solution (28 g in 500 ml of water). The resulting layers were separated and the organic layer was washed with water (200 ml). The organic layer was separated and dried over sodium sulfate (10 g) followed by distillation of methylene chloride under vacuum to produce fesoterodme as oily mass. This oily mass was followed by the addition of isopropyl alcohol (250 ml) at 25-30°C, stirred for 10 minutes and then heated to 55-60°C. Fumaric acid (20.6 g) was added to the resulting mass and stirred for 30 minutes at 55-60°C. The resulting mass was cooled to 25-30°C followed by the dropwise addition of diisopropyl ether (900 ml) at 25-3O°C and then stirred for 12 hours at the same temperature. The separated solid was filtered, washed with diisopropyl ether (300 ml) and

then dried under vacuum at 45-S(TC to produce 84 g of fesotetodine fumarate (Purity by HPLC: 99.86%)

Example 4 Stability of Solid state form of Fesoterodiae mandelate

Fesotetodine mandelate was prepared according to the process exemplified in Example 1 and was packed in a self-sealing low-density polyethylene (LDPE) bag. The material was stored for 3 months under normal atmospheric conditions at room temperature and checked for polymorphic stability. The material was found to retain its polymorphic form after three months of holding, as indicated by maintenance of the original P-XRD pattern.

Unless otherwise indicated, the following definitions are set forth to illustrate and define the meaning and scope of the various terms used to describe the invention herein.

The term "fesoterodine mandelate**, as used herein, means a salt comprised of fesoterodine cations and mandelate anions. For instance, solid as well as dissolved forms are included, and so are crystalline and amorphous forms. Fesoterodine mandelate may exist in an anhydrous and/or solvent-free form or as a hydrate and/or a solvate.

Further, the term "fesoterodine mandelate", as used herein, encompasses stoichiometric as well as non-stoichiometric ratios of fesoterodine cations and mandelate anions. In a particular embodiment, fesoterodine mandelate is formed as a salt having a 1:1 molar ratio between fesoterodine cation and mandelate anion even when an excess of fesoterodine or an excess of mandelic acid is used in the salt formation.

The term "solid form of fesoterodine mandelate disclosed herein" includes crystalline forms, amorphous forms, hydrated, and solvated forms of fesoterodine mandelate. The term "crystalline polymorph*' refers to a crystal modification that can be characterized by analytical methods such as X-ray powder diffraction, IR-spectroscopy, differential scanning calorimetry (DSC) or by its melting point

The term "pharmaceutically acceptable" means that which is useful in preparing a pharmaceutical composition that is generally non-toxic and is not biologically undesirable and includes that which is acceptable for veterinary use and/or human pharmaceutical use.

The term ''pharmaceutical composition" is intended to encompass a drug product including the active ingredients), pharmaceutically acceptable cxcipients that make up the carrier, as well as any product which results, directly or indirectly, from combination, complexation or aggregation of any two or more of the ingredients. Accordingly, the

pharmaceutical compositions encompass any composition made by admixing the active ingredient, active ingredient dispersion or composite, additional active ingredients), and pharmaceutically acceptable exάpients.

The term "therapeutically effective amount* * as used herein means the amount of a compound that, when administered to a mammal for treating a state, disorder or condition, is sufficient to effect such treatment The "therapeutically effective amount" will vary depending on the compound, the disease and its severity and the age, weight, physical condition and responsiveness of the mammal to be treated.

The term "delivering" as used herein means providing a therapeutically effective amount of an active ingredient to a particular location within a host causing a therapeutically effective blood concentration of the active ingredient at the particular location. This can be accomplished, e.g., by topical, local or by systemic administration of the active ingredient to the host.

The term ''buffering agent" as used herein is intended to mean a compound used to resist a change in pH upon dilution or addition of acid of alkali. Such compounds include, by way of example and without limitation, potassium metaphosphate, potassium phosphate, monobasic sodium acetate and sodium citrate anhydrous and dehydrate and other such material known to those of ordinary skill in the art

The term "sweetening agent" as used herein is intended to mean a compound used to impart sweetness to a formulation. Such compounds include, by way of example and without limitation, aspartame, dextrose, glycerin, mannitol, saccharin sodium, sorbitol, sucrose, fructose and other such materials known to those of ordinary skill in the art.

The term "binders" as used herein is intended to mean substances used to cause adhesion of powder particles in granulations. Such compounds include, by way of example and without limitation, acacia, alginic acid, tragacanth, carboxymethylcellulose sodium, polyvinylpyrrolidone, compressible sugar (e.g., NuTab), ethylcellulose, gelatin, liquid glucose, methylcellulosc, pregdatinized starch, starch, polyethylene glycol, guar gum, polysaccharide, bentonites, sugars, invert sugars, poloxamers (PLURONICC™) F68,

PLURONlCi 1 ") F 127), collagen, albumin, celluloses in non-aqueous solvents, polypropylene glycol, polyoxyethylene-polypropylene copolymer, polyethylene ester, polyethylene soibitan ester, polyethylene oxide, microcrystaUine cellulose, combinations thereof and other material known to those of ordinary skill in the art

The term "diluent" or "filler'' as used herein is intended to mean inert substances used as fillers to create the desired bulk, flow properties, and compression characteristics in the

preparation of solid dosage formulations. Such compounds include, by way of example and without limitation * dibasic calcium phosphate, kaolin, sucrose, mannitol, microcrystalline cellulose, powdered cellulose, precipitated calcium carbonate, sorbitol, starch, combinations thereof and other such materials known to those of ordinary skill in die ait Hie term "glidant" as used herein is intended to mean agents used in solid dosage formulations to improve flow-properties during tablet compression and to produce an anti- caking effect. Such compounds include, by way of example and without limitation, colloidal silica, calcium silicate, magnesium silicate, silicon hydrogel, cornstarch, talc, combinations thereof and other such materials known to those of ordinary skill in the ail The term "lubricant" as used herein is intended to mean substances used in solid dosage formulations to reduce friction during compression of the solid dosage. Such compounds include, by way of example and without limitation, calcium stearate, magnesium stearate, mineral oil, stearic acid, zinc stearate, combinations thereof and other such materials known to those of ordinary skill in the art The term "disintegranf ' as used herein is intended to mean a compound used in solid dosage formulations to promote the disruption of the solid mass into smaller particles which are more readily dispersed or dissolved. Exemplary disintegrants include, by way of example and without limitation, starches such as corn starch, potato starch, pregdatinized, sweeteners, clays, such as bentonite, microcrystalline cellulose (e.g., λvicd(™)), carsium (eg., Ambcrlitef™)), alginates, sodium starch glycolate, gums such as agar, guar, locust bean, karaya, pectin, tragacanth, combinations thereof and other such materials known to those of ordinary skill in the art.

The term "wetting agent" as used herein is intended to mean a compound used to aid in attaining intimate contact between solid particles and liquids. Exemplary wetting agents include, by way of example and without limitation, gelatin, casein, lecithin (phosphatides), gum acacia, cholesterol, tragacanth, stearic acid, benzalkonium chloride, calcium stearate, glycerol monostearate, cetostearyi alcohol, cetomacrogol emulsifying wax, sorbitan esters, polyoxyethylene alkyl ethers (e.g., macrogol ethers such as cetomacrogol 1000), polyoxyethylene castor oil derivatives, polyoxyethylene sorbitan fatty acid esters, (e.g., TWEEN( 1 ^)S), polyethylene glycols, polyoxyethylene stearates colloidal silicon dioxide, phosphates, sodium dodecylsulfate, carboxymethylcelhilose calcium, carboxvmethyicdlulosc sodium, methylcellulose, hydroxyethylcellulose, hydroxy! propylcelhilose, hydroxypropymiethyiceUulose phthalate, noncrystalline cellulose, magnesium aluminum silicate, triethanolamine, polyvinyl alcohol, and polyvinylpyrrolidone (PVP). Tyioxapol (a

nonionic liquid polymer of the alkyl aryl polyether alcohol type) is another useful wetting agent, combinations thereof and other such materials known to those of ordinary skill in the art

The term *inicronization M used herein means a process or method by which the size of S a population of particles is reduced.

As used herein, the term "micron" or M μm" bom are same refers to "micrometer" which is 1x10"* meter.

As used herein, "crystalline particles" means any combination of single crystals, aggregates and agglomerates. 0 As used herein, "Particle Size Distribution (P.SJD)" means the cumulative volume size distribution of equivalent spherical diameters as determined by laser diffraction in Malvem Master Sizer 2000 equipment or its equivalent

As used herein, Dx means that X percent of the particles have a diameter less man a specified diameter D. Thus, a D*» or d(0.9) of less than 300 microns means that 90 volume- S percent of the particles in a composition have a diameter less than 300 microns.

The use of the terms "a" and "an * * and 4 HhC * * and similar referents in the context of describing the invention (especially in the context of the following claims) are to be construed to cover bom (he singular and the plural, unless otherwise indicated herein or clearly contradicted by context The terms "comprising," "having," 'including, ** and0 "containing" are to be construed as open-ended terms (i.e., meaning "including, but not limited to,' * ) unless otherwise noted. Recitation of ranges of values herein are merely intended to serve as a shorthand method of referring individually to each separate value falling within the range, unless otherwise indicated herein, and each separate value is incorporated into the specification as if it were individually recited herein. The term wt%5 refers to percent by weight AU methods described herein can be performed in any suitable order unless otherwise indicated herein or otherwise clearly contradicted by context The use of any and all examples, or exemplary language (eg., "such as") provided herein, is intended merely to better illuminate the invention and does not pose a limitation on the scope of the invention unless otherwise claimed. No language in die specification should be construed as0 indicating any non-claimed element as essential to the practice of the invention.

Preferred embodiments of this invention are described herein, including die best mode known to the inventors for carrying out the invention. Variations of those preferred embodiments may become apparent to those of ordinary skill in the art upon reading the foregoing description. The inventors expect skilled artisans to employ such variations as

appropriate, and the inventors intend for the invention to be practiced otherwise than as specifically described herein. Accordingly, this invention includes all modifications and equivalents of the subject matter recited in the claims appended hereto as permitted by applicable law. Moreover, any combination of the above-described elements in all possible variations thereof is encompassed by the invention unless otherwise indicated herein or otherwise dearly contradicted by context.