US20100292502A1 - Method for preparing high-purity fesoterodine fumarate - Google Patents
Method for preparing high-purity fesoterodine fumarate Download PDFInfo
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- US20100292502A1 US20100292502A1 US12/779,216 US77921610A US2010292502A1 US 20100292502 A1 US20100292502 A1 US 20100292502A1 US 77921610 A US77921610 A US 77921610A US 2010292502 A1 US2010292502 A1 US 2010292502A1
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- fesoterodine
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- MWHXMIASLKXGBU-RNCYCKTQSA-N (e)-but-2-enedioic acid;[2-[(1r)-3-[di(propan-2-yl)amino]-1-phenylpropyl]-4-(hydroxymethyl)phenyl] 2-methylpropanoate Chemical compound OC(=O)\C=C\C(O)=O.C1([C@@H](CCN(C(C)C)C(C)C)C=2C(=CC=C(CO)C=2)OC(=O)C(C)C)=CC=CC=C1 MWHXMIASLKXGBU-RNCYCKTQSA-N 0.000 title claims abstract description 36
- 229960004524 fesoterodine fumarate Drugs 0.000 title claims abstract description 35
- 238000000034 method Methods 0.000 title claims abstract description 26
- VZCYOOQTPOCHFL-OWOJBTEDSA-N Fumaric acid Chemical compound OC(=O)\C=C\C(O)=O VZCYOOQTPOCHFL-OWOJBTEDSA-N 0.000 claims abstract description 30
- DCCSDBARQIPTGU-HSZRJFAPSA-N fesoterodine Chemical compound C1([C@@H](CCN(C(C)C)C(C)C)C=2C(=CC=C(CO)C=2)OC(=O)C(C)C)=CC=CC=C1 DCCSDBARQIPTGU-HSZRJFAPSA-N 0.000 claims abstract description 23
- 229960002978 fesoterodine Drugs 0.000 claims abstract description 22
- VZCYOOQTPOCHFL-UHFFFAOYSA-N trans-butenedioic acid Natural products OC(=O)C=CC(O)=O VZCYOOQTPOCHFL-UHFFFAOYSA-N 0.000 claims abstract description 16
- 239000001530 fumaric acid Substances 0.000 claims abstract description 15
- 239000003960 organic solvent Substances 0.000 claims abstract description 14
- 150000002576 ketones Chemical class 0.000 claims abstract description 8
- 238000006243 chemical reaction Methods 0.000 claims abstract description 7
- 125000000956 methoxy group Chemical group [H]C([H])([H])O* 0.000 claims abstract description 4
- ZWEHNKRNPOVVGH-UHFFFAOYSA-N 2-Butanone Chemical group CCC(C)=O ZWEHNKRNPOVVGH-UHFFFAOYSA-N 0.000 claims description 28
- 239000000203 mixture Substances 0.000 claims description 11
- 238000004090 dissolution Methods 0.000 claims description 6
- 238000001816 cooling Methods 0.000 claims description 5
- 238000010438 heat treatment Methods 0.000 claims description 4
- 125000004432 carbon atom Chemical group C* 0.000 claims description 2
- 238000004519 manufacturing process Methods 0.000 claims description 2
- 239000012535 impurity Substances 0.000 description 29
- 239000000047 product Substances 0.000 description 17
- 239000000243 solution Substances 0.000 description 16
- 150000002148 esters Chemical class 0.000 description 14
- YMWUJEATGCHHMB-UHFFFAOYSA-N Dichloromethane Chemical compound ClCCl YMWUJEATGCHHMB-UHFFFAOYSA-N 0.000 description 12
- UIIMBOGNXHQVGW-UHFFFAOYSA-M Sodium bicarbonate Chemical compound [Na+].OC([O-])=O UIIMBOGNXHQVGW-UHFFFAOYSA-M 0.000 description 10
- 238000004128 high performance liquid chromatography Methods 0.000 description 9
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 8
- 238000002360 preparation method Methods 0.000 description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 7
- 150000005690 diesters Chemical class 0.000 description 6
- 238000003756 stirring Methods 0.000 description 6
- 229910000030 sodium bicarbonate Inorganic materials 0.000 description 5
- 235000017557 sodium bicarbonate Nutrition 0.000 description 5
- 239000000463 material Substances 0.000 description 4
- 229910052757 nitrogen Inorganic materials 0.000 description 4
- 239000012074 organic phase Substances 0.000 description 4
- 239000000725 suspension Substances 0.000 description 4
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- 239000008367 deionised water Substances 0.000 description 3
- 229910021641 deionized water Inorganic materials 0.000 description 3
- 238000002474 experimental method Methods 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- 238000013112 stability test Methods 0.000 description 3
- 230000001960 triggered effect Effects 0.000 description 3
- DGMOBVGABMBZSB-UHFFFAOYSA-N 2-methylpropanoyl chloride Chemical compound CC(C)C(Cl)=O DGMOBVGABMBZSB-UHFFFAOYSA-N 0.000 description 2
- 238000002441 X-ray diffraction Methods 0.000 description 2
- 238000004458 analytical method Methods 0.000 description 2
- 239000006227 byproduct Substances 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 238000002425 crystallisation Methods 0.000 description 2
- 230000008025 crystallization Effects 0.000 description 2
- 239000002050 international nonproprietary name Substances 0.000 description 2
- 230000014759 maintenance of location Effects 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 238000007415 particle size distribution analysis Methods 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 239000011541 reaction mixture Substances 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- 239000007858 starting material Substances 0.000 description 2
- 238000001644 13C nuclear magnetic resonance spectroscopy Methods 0.000 description 1
- 238000005160 1H NMR spectroscopy Methods 0.000 description 1
- BVKZGUZCCUSVTD-UHFFFAOYSA-M Bicarbonate Chemical compound OC([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-M 0.000 description 1
- XBWRSQLUKKEGDF-FAAASRTMSA-N CC(C)C(=O)Cl.CC(C)C(=O)OC1=CC=C(CO)C=C1[C@H](CCN(C(C)C)C(C)C)C1=CC=CC=C1.CC(C)N(CC[C@H](C1=CC=CC=C1)C1=CC(CO)=CC=C1O)C(C)C Chemical compound CC(C)C(=O)Cl.CC(C)C(=O)OC1=CC=C(CO)C=C1[C@H](CCN(C(C)C)C(C)C)C1=CC=CC=C1.CC(C)N(CC[C@H](C1=CC=CC=C1)C1=CC(CO)=CC=C1O)C(C)C XBWRSQLUKKEGDF-FAAASRTMSA-N 0.000 description 1
- WEXBMWHCHBHOMW-RNCYCKTQSA-N CC(C)C(=O)OC1=CC=C(CO)C=C1[C@H](CCN(C(C)C)C(C)C)C1=CC=CC=C1.O=C(O)/C=C/COO Chemical compound CC(C)C(=O)OC1=CC=C(CO)C=C1[C@H](CCN(C(C)C)C(C)C)C1=CC=CC=C1.O=C(O)/C=C/COO WEXBMWHCHBHOMW-RNCYCKTQSA-N 0.000 description 1
- CHEHSUCSZOKLSO-LECGRMGRSA-N CC(C)C(=O)OC1=CC=C(COC(=O)/C=C/C(=O)O)C=C1[C@H](CCN(C(C)C)C(C)C)C1=CC=CC=C1 Chemical compound CC(C)C(=O)OC1=CC=C(COC(=O)/C=C/C(=O)O)C=C1[C@H](CCN(C(C)C)C(C)C)C1=CC=CC=C1 CHEHSUCSZOKLSO-LECGRMGRSA-N 0.000 description 1
- DUXZAXCGJSBGDW-HXUWFJFHSA-N Desfesoterodine Chemical compound C1([C@@H](CCN(C(C)C)C(C)C)C=2C(=CC=C(CO)C=2)O)=CC=CC=C1 DUXZAXCGJSBGDW-HXUWFJFHSA-N 0.000 description 1
- 206010020853 Hypertonic bladder Diseases 0.000 description 1
- 208000009722 Overactive Urinary Bladder Diseases 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- 239000004480 active ingredient Substances 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000012455 biphasic mixture Substances 0.000 description 1
- 238000012790 confirmation Methods 0.000 description 1
- 239000002270 dispersing agent Substances 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 238000004108 freeze drying Methods 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000010899 nucleation Methods 0.000 description 1
- 208000020629 overactive bladder Diseases 0.000 description 1
- 239000012071 phase Substances 0.000 description 1
- PIZOACXKIKXRDJ-UHFFFAOYSA-N phenyl 2-methylpropanoate Chemical compound CC(C)C(=O)OC1=CC=CC=C1 PIZOACXKIKXRDJ-UHFFFAOYSA-N 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 239000002243 precursor Substances 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
- 239000000741 silica gel Substances 0.000 description 1
- 229910002027 silica gel Inorganic materials 0.000 description 1
- 239000012265 solid product Substances 0.000 description 1
- 238000004611 spectroscopical analysis Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 208000011580 syndromic disease Diseases 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 229940001407 toviaz Drugs 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C227/00—Preparation of compounds containing amino and carboxyl groups bound to the same carbon skeleton
- C07C227/14—Preparation of compounds containing amino and carboxyl groups bound to the same carbon skeleton from compounds containing already amino and carboxyl groups or derivatives thereof
- C07C227/16—Preparation of compounds containing amino and carboxyl groups bound to the same carbon skeleton from compounds containing already amino and carboxyl groups or derivatives thereof by reactions not involving the amino or carboxyl groups
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C219/00—Compounds containing amino and esterified hydroxy groups bound to the same carbon skeleton
- C07C219/26—Compounds 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
- C07C219/28—Compounds 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
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C59/00—Compounds having carboxyl groups bound to acyclic carbon atoms and containing any of the groups OH, O—metal, —CHO, keto, ether, groups, groups, or groups
- C07C59/40—Unsaturated compounds
Definitions
- the object of the present invention is a process for preparing fesoterodine fumarate comprising the salification reaction of fesoterodine with fumaric acid in an organic solvent, preferably a ketone, at a temperature not greater than 45° C.
- Fesoterodine fumarate is the international nonproprietary name (INN) of the active principle 2-((R)-3-diisopropylammonium-1-phenylpropyl)-4-(hydroxymethyl)phenyl isobutyrate hydrogen fumarate, whose structure formula is reported hereinbelow.
- Fesoterodine fumarate was described for the first time in U.S. Pat. No. 6,858,650, which reports the preparation of the active ingredient by the salification of fesoterodine with fumaric acid, according to scheme 1 reported below.
- fesoterodine also called fesoterodine base
- (R)-feso deacyl i.e. (R)-2-[3-(diisopropylamino)-1-phenylpropyl]-4-(hydroxymethyl)phenol, according to scheme 2 reported hereinbelow.
- Such impurity can increase up to values greater than 1% if the salification conditions are not suitable controlled.
- the feso fumaric ester impurity has been synthesized and characterized, and salification conditions of fesoterodine with fumaric acid have been identified (constituting the object of the present invention) such that the quantity of feso fumaric ester impurity in the finished product is maintained below the ICH limits allowed for known impurities ( ⁇ 0.15% by mole).
- Both the process for the preparation of fesoterodine fumarate via salification of fesoterodine with fumaric acid and the fesoterodine fumarate thus obtained constitute the object of the present invention; and in particular, a fesoterodine fumarate having a content of feso fumaric ester impurity below 0.15% by mole.
- the process according to the present invention comprises the salification reaction of fesoterodine with fumaric acid in at least one suitable organic solvent at a temperature not higher than 45° C., preferably at a temperature comprised between 30 and 40° C., still more preferably at about 35° C.
- such salification reaction is carried out by heating a mixture of fesoterodine and fumaric acid at the aforesaid temperature in the aforesaid at least one organic solvent, until complete dissolution; such operation normally requires from 10 minutes to two hours, preferably from 30 minutes to one hour.
- the solution thus obtained is then cooled at a temperature lower than 25° C., preferably comprised between 5 and 20° C., still more preferably between 15 and 20° C.
- the precipitation of the salt can be triggered with methods known in the art, for example via addition of a crystalline fesoterodine fumarate seed or by means of addition of solid fesoterodine fumarate obtained via lyophilization of an aqueous solution of fesoterodine fumarate.
- the fesoterodine usable in the process of the present invention can be obtained according to one of the methods reported in the literature, for example according to the method reported in U.S. Pat. No. 6,713,464, incorporated herein by reference; it can also be used either in pure or crude form.
- the organic solvent is preferably a polar aprotic organic solvent, preferably a ketone, still more preferably a ketone having from three to six carbon atoms; according to the more preferred embodiment, such ketone is methylethylketone (i.e. 2-butanone).
- fumaric acid is used in molar ratios comprised between 0.9 and 1.5 (preferably between 1.0 and 1.1) with respect to fesoterodine; fesoterodine, in turn, is used in a weight/volume ratio (g/l) comprised between 2 and 50, preferably between 3 and 10, with respect to said at least one organic solvent.
- Fesoterodine fumarate thus obtained can then be isolated with conventional methods; it is preferably filtered, washed (generally with the same solvent used in the salification reaction) and then dried under vacuum.
- the product thus obtained is therefore preferably micronized by using conventional techniques, until a PSD is obtained with d (0.9) ⁇ 20 microns, i.e. a Particle Size Distribution in which 90% of the particles have a size that does not exceed 20 microns.
- the experiment related to Table 1 consists of dissolving fesoterodine fumarate in methylethylketone at 40° C., drawing samples of the freshly dissolved solution (time 0), after 1, 3 and 20 hours of maintenance at 40° C. and analyzing them in HPLC in order to verify their purity.
- the experiment consists of introducing a sample of fesoterodine fumarate in an oven capable of maintaining a temperature of 60° C. and 60% relative humidity, drawing samples of the freshly introduced substance (time 0) after 24, 48, 72 and 144 hours staying in such conditions, and analyzing them in HPLC in order to verify their purity.
- the fesoterodine thus obtained can be recrystallized by dissolving it in 21 ml of methylethylketone, bringing the mixture to 40° C. (with dissolution of the suspended material), cooling the solution at 20° C., and seeding the solution with 2 mg of crystalline fesoterodine fumarate. After further cooling at 0-5° C. and keeping in such conditions for two hours, the obtained solid is filtered and washed with methylethylketone, obtaining 3.03 g of moist fesoterodine fumarate, which is dried at 35° C.
- fesoterodine fumarate prepared according to example 1 are inserted into a Mc One® Fluid Jet Mill micronization apparatus at a nitrogen pressure of the micronization chamber of 4 atmospheres and at a nitrogen pressure of the Venturi tube of 6 atmospheres.
- the recovered product is subjected to Particle Size Distribution analysis by using a Malvern Mastersizer 2000 Ver. 5.22, Tegiloxan 3 instrument as dispersing agent and a dispersing speed in the instrument of 3000 rpm.
- the d(0.9) of the product is equal to 24 microns.
- the product is analyzed for HPLC purity and has identical purity to the starting product (99.8%, with (R)-feso deacyl not detectable, diester impurity 0.10% and feso fumaric ester impurity 0.07%.).
- the obtained product is also analyzed by means of X ray diffraction of powders and the analysis confirms that the micronized material has the same crystalline form as the starting material.
- a second 30 g aliquot of the product prepared according to the example 1 is micronized in the same above-described apparatus, at a nitrogen pressure of the micronization chamber of 6 atmospheres and at a nitrogen pressure of the Venturi tube of 8 atmospheres.
- the recovered product is subjected to Particle Size Distribution analysis by using a Malvern 2000 instrument.
- the d(0.9) of the product is equal to 15 microns and the purity of the product remains unchanged with respect to the material inserted in the micronizer.
- the obtained product is also analyzed by means of X ray diffraction of powders and the analysis confirms that the micronized material has the same crystalline form as the starting material.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Inorganic Compounds Of Heavy Metals (AREA)
Abstract
A process is described for preparing fesoterodine fumarate comprising the salification reaction of fesoterodine with fumaric acid in an organic solvent, preferably a ketone, at a temperature not greater than 45° C. Such process allows obtaining products with high yields and purities, and in particular a product having a content of (2E)-4-[(3-(3-diisopropylamino-1-phenylpropyl)-4-(2-isobutyroyloxyphenyl)methoxy]-4-oxobut-2-enoic acid less than or equal to 0.15% by mole.
Description
- This application claims priority to and benefit of Italian Application No. MI2009A000845 filed on May 15, 2009, the content of which is incorporated herein by reference in its entirety.
- The object of the present invention is a process for preparing fesoterodine fumarate comprising the salification reaction of fesoterodine with fumaric acid in an organic solvent, preferably a ketone, at a temperature not greater than 45° C.
- Fesoterodine fumarate is the international nonproprietary name (INN) of the active principle 2-((R)-3-diisopropylammonium-1-phenylpropyl)-4-(hydroxymethyl)phenyl isobutyrate hydrogen fumarate, whose structure formula is reported hereinbelow.
- Fesoterodine fumarate was approved in Europe and in the U.S.A. for the treatment of overactive bladder syndrome with the commercial name of TOVIAZ®.
- Fesoterodine fumarate was described for the first time in U.S. Pat. No. 6,858,650, which reports the preparation of the active ingredient by the salification of fesoterodine with fumaric acid, according to scheme 1 reported below.
- In turn, fesoterodine (also called fesoterodine base) is described in U.S. Pat. No. 6,713,464, where it is prepared starting from a deacylated precursor, (R)-feso deacyl, i.e. (R)-2-[3-(diisopropylamino)-1-phenylpropyl]-4-(hydroxymethyl)phenol, according to scheme 2 reported hereinbelow.
- The preparation of (R)-feso deacyl is instead described in U.S. Pat. No. 5,559,7269.
- During the salification experiments of fesoterodine with fumaric acid, it was found that in the salification reaction, variable quantities of a by-product can be formed that is not reported in the literature. Such by-product was identified as a fesoterodine monofumarate, i.e. (2E)-4-[(3-(3-diisopropylamino-1-phenylpropyl)-4-(2-isobutyroyloxyphenyl)methoxy]-4-oxobut-2-enoic acid, whose structure formula is reported hereinbelow.
- Such impurity, named “feso fumaric ester” impurity for convenience, can increase up to values greater than 1% if the salification conditions are not suitable controlled.
- The feso fumaric ester impurity has been synthesized and characterized, and salification conditions of fesoterodine with fumaric acid have been identified (constituting the object of the present invention) such that the quantity of feso fumaric ester impurity in the finished product is maintained below the ICH limits allowed for known impurities (≦0.15% by mole).
- Both the process for the preparation of fesoterodine fumarate via salification of fesoterodine with fumaric acid and the fesoterodine fumarate thus obtained constitute the object of the present invention; and in particular, a fesoterodine fumarate having a content of feso fumaric ester impurity below 0.15% by mole.
- The process according to the present invention comprises the salification reaction of fesoterodine with fumaric acid in at least one suitable organic solvent at a temperature not higher than 45° C., preferably at a temperature comprised between 30 and 40° C., still more preferably at about 35° C.
- In practice, such salification reaction is carried out by heating a mixture of fesoterodine and fumaric acid at the aforesaid temperature in the aforesaid at least one organic solvent, until complete dissolution; such operation normally requires from 10 minutes to two hours, preferably from 30 minutes to one hour. The solution thus obtained is then cooled at a temperature lower than 25° C., preferably comprised between 5 and 20° C., still more preferably between 15 and 20° C.
- The precipitation of the salt can be triggered with methods known in the art, for example via addition of a crystalline fesoterodine fumarate seed or by means of addition of solid fesoterodine fumarate obtained via lyophilization of an aqueous solution of fesoterodine fumarate.
- The fesoterodine usable in the process of the present invention can be obtained according to one of the methods reported in the literature, for example according to the method reported in U.S. Pat. No. 6,713,464, incorporated herein by reference; it can also be used either in pure or crude form.
- According to one aspect of the invention, the organic solvent is preferably a polar aprotic organic solvent, preferably a ketone, still more preferably a ketone having from three to six carbon atoms; according to the more preferred embodiment, such ketone is methylethylketone (i.e. 2-butanone).
- According to a further aspect of the invention, fumaric acid is used in molar ratios comprised between 0.9 and 1.5 (preferably between 1.0 and 1.1) with respect to fesoterodine; fesoterodine, in turn, is used in a weight/volume ratio (g/l) comprised between 2 and 50, preferably between 3 and 10, with respect to said at least one organic solvent.
- Fesoterodine fumarate thus obtained can then be isolated with conventional methods; it is preferably filtered, washed (generally with the same solvent used in the salification reaction) and then dried under vacuum.
- The product thus obtained is therefore preferably micronized by using conventional techniques, until a PSD is obtained with d (0.9)≦20 microns, i.e. a Particle Size Distribution in which 90% of the particles have a size that does not exceed 20 microns.
- In the following tables, the results of two stability tests are reported that were conducted on samples of fesoterodine fumarate obtained by following the teachings of example 1.
- In detail, the experiment related to Table 1 consists of dissolving fesoterodine fumarate in methylethylketone at 40° C., drawing samples of the freshly dissolved solution (time 0), after 1, 3 and 20 hours of maintenance at 40° C. and analyzing them in HPLC in order to verify their purity.
-
TABLE 1 Solution stability in methylethylketone at T = 40° C. HPLC Purity (R)-feso- Impurity Impurity Feso fumaric ester Diester Area % deacyl RRt = 1.05 RRt = 1.34 impurity impurity RRt = 1.86 t = 0 99.87 n.d. n.d. 0.06 0.07 — — t = 1 hour 99.85 n.d. n.d. 0.06 0.09 — — t = 3 hours 99.77 0.01 n.d. 0.06 0.12 0.04 — t = 20 hours 99.70 0.02 n.d. 0.08 0.14 0.06 n.d. RRt = Relative Retention time (HPLC) n.d. = not detectable - From the conducted test, it was observed that the feso fumaric ester impurity increases over time until it stabilizes at about 0.14% by mole, i.e. below the specification limit, after 20 hours.
- In confirmation thereof, another stability test was carried out at 60° C. on the crystallized solid product, whose results are reported in Table 2. In detail, the experiment consists of introducing a sample of fesoterodine fumarate in an oven capable of maintaining a temperature of 60° C. and 60% relative humidity, drawing samples of the freshly introduced substance (time 0) after 24, 48, 72 and 144 hours staying in such conditions, and analyzing them in HPLC in order to verify their purity.
-
TABLE 2 Solid stability at T = 60° C. in atmosphere with 60% relative humidity HPLC Purity (R)-feso- Impurity Impurity Feso fumaric ester Diester Area % deacyl RRt = 1.05 RRt = 1.34 impurity impurity RRt = 1.86 t = 0 99.85 0.02 n.d. n.d. 0.09 0.04 n.d. t = 24 h 99.83 0.02 n.d. n.d. 0.11 0.04 n.d. t = 48 h 99.74 0.02 n.d. 0.08 0.12 0.04 n.d. t = 72 h 99.72 0.03 0.02 0.06 0.13 0.04 n.d. t = 144 h 99.64 0.05 0.03 0.07 0.14 0.04 0.03 RRt = Relative Retention time (HPLC) n.d. = not detectable - Also from this stability test, it is confirmed that crystalline fesoterodine fumarate maintained at 60° C. loses purity over time via formation of the feso fumaric ester impurity, which stabilizes after 144 hours (6 days) at around 0.14% by mole.
- The following examples clarify in detail the conditions used for obtaining high-purity fesoterodine fumarate according to the present invention; such examples are intended as non-limiting and exemplifying of the present invention.
- In a 2-liter reactor, 31.2 g of sodium bicarbonate and 1250 ml of deionized water (pH 8.1) are charged. Stirring is performed until complete dissolution of the salt. In a 10-liter reactor, 250 g of (R)-Feso deacyl and 7500 ml of dichloromethane are charged. Stirring is performed until a complete solution is obtained. Then, the aqueous bicarbonate solution is added to the organic solution and the biphasic mixture is cooled at 5° C. 86 g of isobutyryl chloride are then added dropwise to the mixture, which is once again stirred for one hour from the end of the addition. Then, 1250 ml of a solution of 5% w/w sodium bicarbonate in water are added to the reaction mixture and the mixture is heated at 20° C., still under stirring. The lower organic phase is separated and is first washed with 2500 ml of a solution of 5% w/w sodium bicarbonate in water then twice with 2×2500 ml of deionized water. The obtained organic phase is concentrated to a small volume and 1000 ml of 2-butanone are added thereto. The mixture is once again evaporated to half the initial volume, then 1000 ml of 2-butanone are added again and 80.4 g fumaric acid are added to the solution. The suspension is heated at 35° C. until complete dissolution is obtained. It is cooled at 20° C.; the crystallization is triggered with crystalline fesoterodine fumarate seeds. Stirring is maintained for 1 hour at 20° C. and for 2 hours at 0° C. The suspension is then filtered over a Buchner funnel and the pad is washed with 600 ml of 2-butanone. 621 g of moist product are obtained, which are dried at t=35° C. for 15 hours, obtaining 331 g of crystalline fesoterodine fumarate (85.7% yield). The purity of the product is 99.8%, with (R)-feso deacyl not detectable, diester impurity 0.10% and feso fumaric ester impurity 0.07%.
- In a 250 milliliter flask, 3.0 g of (R)-Feso deacyl and 60 ml of dichloromethane are charged. Stirring is performed until a complete solution is obtained. The temperature of the solution is brought to 0-5° C. 1.02 g of isobutyryl chloride dissolved in 30 ml of dichloromethane are added dropwise on the mixture and the mixture is again stirred for ten minutes from the end of the addition. Then, 15 ml of a solution of 2.5% w/w sodium bicarbonate in water (pH 8.1) are added to the reaction mixture and the mixture is stirred at 0-5° C. for another 2 hours. It is then left to warm at room temperature and the lower organic phase is separated, washing it first with 30 ml of a solution of 5% w/w sodium bicarbonate in water and then twice with 2×50 ml of deionized water. The obtained organic phase is concentrated to small volume and 30 ml of 2-butanone are added thereto. The mixture is once again evaporated to half the initial volume, then another 30 ml of 2-butanone are added, and 0.9 g of fumaric acid are added to the solution. The suspension is heated at 35° C. until complete dissolution is obtained. It is cooled at 20° C.; the crystallization is triggered with seeds of crystalline fesoterodine fumarate. Stirring is maintained for 1 hour at 20° C. and for 2 hours at 0° C. Then, the suspension is filtered over a Buchner filter and the pad is washed with 10 ml of 2-butanone. 3.41 g of moist product are obtained, which are dried at t=35° C. for 15 hours, obtaining 3.13 g of crystalline fesoterodine fumarate (85.7% yield). The purity of the product is 99.8%, with (R)-feso deacyl 0.12%, diester impurity 0.07% and feso fumaric ester impurity 0.02%.
- The fesoterodine thus obtained can be recrystallized by dissolving it in 21 ml of methylethylketone, bringing the mixture to 40° C. (with dissolution of the suspended material), cooling the solution at 20° C., and seeding the solution with 2 mg of crystalline fesoterodine fumarate. After further cooling at 0-5° C. and keeping in such conditions for two hours, the obtained solid is filtered and washed with methylethylketone, obtaining 3.03 g of moist fesoterodine fumarate, which is dried at 35° C. for 15 hours, obtaining 2.75 g of fesoterodine fumarate (89% yield), having HPLC purity equal to 99.9%, containing (R)-feso deacyl 0.09%, non-detectable diester impurity and feso fumaric ester impurity 0.03%.
- 30 g of fesoterodine fumarate prepared according to example 1 are inserted into a Mc One® Fluid Jet Mill micronization apparatus at a nitrogen pressure of the micronization chamber of 4 atmospheres and at a nitrogen pressure of the Venturi tube of 6 atmospheres. The recovered product is subjected to Particle Size Distribution analysis by using a Malvern Mastersizer 2000 Ver. 5.22, Tegiloxan 3 instrument as dispersing agent and a dispersing speed in the instrument of 3000 rpm. The d(0.9) of the product is equal to 24 microns. The product is analyzed for HPLC purity and has identical purity to the starting product (99.8%, with (R)-feso deacyl not detectable, diester impurity 0.10% and feso fumaric ester impurity 0.07%.). The obtained product is also analyzed by means of X ray diffraction of powders and the analysis confirms that the micronized material has the same crystalline form as the starting material.
- A second 30 g aliquot of the product prepared according to the example 1 is micronized in the same above-described apparatus, at a nitrogen pressure of the micronization chamber of 6 atmospheres and at a nitrogen pressure of the Venturi tube of 8 atmospheres. The recovered product is subjected to Particle Size Distribution analysis by using a Malvern 2000 instrument. The d(0.9) of the product is equal to 15 microns and the purity of the product remains unchanged with respect to the material inserted in the micronizer. The obtained product is also analyzed by means of X ray diffraction of powders and the analysis confirms that the micronized material has the same crystalline form as the starting material.
- 5 g of fesoterodine fumarate prepared as in example 1 are dissolved in 150 ml of methylethylketone and the mixture is heated under reflux for a week. At the end, the HPLC analysis detects shows a content of feso fumaric ester impurity of 15%. The solvent is evaporated and the residue is chromatographed on silica gel column, eluting with a mobile phase constituted by 80% dichloromethane and 20% methanol. The column fractions containing the desired impurity are collected and by drying the pooled fractions, 600 mg of the desired impurity are obtained. The spectroscopic data reported below, related to the isolated impurity, confirm the identity of the obtained product.
- 1H-NMR: 6 (DMSOd6): 6.60-7.45 (m, 10H); 5.15 (d, 2H); 4.01 (m, 1H); 3.59-3.52 (m, 4H); 2.87-2.71 (m, 5H); 1.35-1.24 (m, 18H).
- 13C-NMR: 6 (DMSOd6): 175.86, 169.55, 166.25, 148.68, 142.19, 141.28, 135.42, 134.79, 129.05, 128.99, 128.08, 127.87, 127.69, 127.17, 123.05, 65.86, 54.54, 46.17, 41.74, 34.37, 31.91, 19.38, 19.23, 18.04, 17.83.
- MS (positive ionization): (M+1) 510.54 (100%), 511.40 (36%), 512.35 (7%). Calculated for C30H39NO6: 510.29 (100), 511.29 (36%), 510.29 (7%).
Claims (20)
1. Process for preparing fesoterodine fumarate comprising reacting fesoterodine with fumaric acid, wherein said reaction step is carried out in at least one organic solvent at a temperature not higher than 45° C.
2. Process according to claim 1 , wherein said temperature is comprised between 30 and 40° C.
3. Process according to claim 2 , wherein said temperature is about 35° C.
4. Process according to claim 1 , further comprising heating a mixture of fesoterodine and fumaric acid in said at least one organic solvent until complete dissolution, and cooling the solution thus obtained at a temperature lower than 25° C.
5. Process according to claim 4 , wherein said heating step is carried out for a period comprised between 10 minutes and two hours.
6. Process according to claim 5 , wherein said heating step is carried out for a period comprised between 30 minutes and one hour.
7. Process according to claim 4 , wherein said cooling step is carried out at a temperature comprised between 5 and 20° C.
8. Process according to claim 7 , wherein said cooling step is carried out at a temperature comprised between 15 and 20° C.
9. Process according to claim 1 , wherein said at least one organic solvent is a polar aprotic organic solvent.
10. Process according to claim 1 , wherein said at least one organic solvent is a ketone.
11. Process according to claim 10 , wherein said ketone has from three to six carbon atoms.
12. Process according to claim 10 , wherein said ketone is methylethylketone.
13. Process according to claim 1 , wherein said fumaric acid is used in molar ratios comprised between 0.9 and 1.5 with respect to fesoterodine.
14. Process according to claim 13 , wherein said fumaric acid is used in molar ratios comprised between 1.0 and 1.1 with respect to fesoterodine.
15. Process according to claim 1 , wherein said fesoterodine is used in a weight/volume ratio comprised between 2 and 50 with respect to said at least one organic solvent.
16. Process according to claim 15 , wherein said fesoterodine is used in a weight/volume ratio comprised between 3 and 10 with respect to said at least one organic solvent.
17. Process according to claim 1 , wherein the fesoterodine fumarate thus obtained is filtered, washed, dried under vacuum and/or micronized.
18. Process according to claim 17 , wherein the fesoterodine fumarate is micronized until obtaining a PSD with d (0.9)≦20 micron.
19. Fesoterodine fumarate having a content of (2E)-4-[(3-(3-diisopropylamino-1-phenylpropyl)-4-(2-isobutyroyloxyphenyl)methoxy]-4-oxobut-2-enoic acid less than or equal to 0.15% by mole.
20. Micronized fesoterodine fumarate having a content of (2E)-4-[(3-(3-diisopropylamino-1-phenylpropyl)-4-(2-isobutyroyloxyphenyl)methoxy]-4-oxobut-2-enoic acid less than or equal to 0.15% by mole and a PSD with d (0.9)≦20 micron.
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US20110086103A1 (en) * | 2008-04-04 | 2011-04-14 | Actavis Group Ptc Ehf | Novel mandelate salt of fesoterodine |
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SE9203318D0 (en) | 1992-11-06 | 1992-11-06 | Kabi Pharmacia Ab | NOVEL 3,3-DIPHENYL PROPYLAMINES, THEIR USE AND PREPARATION |
EP0957073A1 (en) | 1998-05-12 | 1999-11-17 | Schwarz Pharma Ag | Novel derivatives of 3,3-diphenylpropylamines |
US20100297241A1 (en) * | 2007-10-01 | 2010-11-25 | Actavis Group Ptc Ehf | Amorphous Fesoterodine Fumarate |
WO2010018484A1 (en) * | 2008-08-14 | 2010-02-18 | Pfizer Limited | New uses of diisopropylamine derivatives |
WO2011029005A1 (en) * | 2009-09-03 | 2011-03-10 | Teva Gyogyszergyar Zartkoruen Mukodo Reszvenytarsasag | Crystalline forms of fesoterodine fumarate and fesoterodine base |
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US20110086103A1 (en) * | 2008-04-04 | 2011-04-14 | Actavis Group Ptc Ehf | Novel mandelate salt of fesoterodine |
US8049031B2 (en) * | 2008-12-10 | 2011-11-01 | Chemi S.P.A. | Solid forms of fesoterodine fumarate |
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ITMI20090845A1 (en) | 2010-11-16 |
ES2590027T3 (en) | 2016-11-17 |
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US20140303396A1 (en) | 2014-10-09 |
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