Claims for Patent: 6,150,366
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Summary for Patent: 6,150,366
Title: | Ziprasidone formulations |
Abstract: | Compositions comprising crystalline ziprasidone free base or crystalline ziprasidone hydrochloride particles having a mean particle size less than 85 .mu.m, and a pharmaceutically acceptable carrier, are substantially bioequivalent and can be used to treat psychoses such as schizophrenia. |
Inventor(s): | Arenson; Daniel R. (East Lyme, CT), Busch; Frank Robert (Gales Ferry, CT), Hausberger; Angela G. (East Lyme, CT), Rasadi; Bijan (Groton, CT) |
Assignee: | Pfizer Inc. (New York, NY) |
Application Number: | 09/320,985 |
Patent Claims: |
1. A composition comprising crystalline ziprasidone free base or crystalline ziprasidone hydrochloride particles having a mean particle size equal to or less than about 85
.mu.m and a pharmaceutically acceptable diluent or carrier.
2. A composition as defined in claim 1, wherein said composition comprises ziprasidone hydrochloride monohydrate. 3. A composition as defined in claim 1, wherein said mean particle size is equal to or less than 50 .mu.m. 4. A composition as defined in claim 3, wherein said mean particle size is from 5 to 50 .mu.m. 5. A composition as defined in claim 4, wherein said mean particle size is from 5 to 40 .mu.m. 6. A composition as defined in claim 5, wherein said mean particle size is from 5 to 30 .mu.m. 7. A composition as defined in claim 1 which exhibits an AUC and/or C.sub.max that is at least 80% of the mean AUC and/or C.sub.max observed for an equivalent formulation differing only in that the ziprasidone hydrochloride mean particle size is 20 .mu.m. 8. A composition as defined in claim 1, wherein, when an amount of said dosage form equivalent to 100 mgA or less of ziprasidone is placed in a USP-2 apparatus containing 900 ml of aqueous NaH.sub.2 PO.sub.4 buffer, pH 7.5, containing 2% (w/v) sodium dodecyl sulfate, and equipped with paddles stirring at 75 rpm, at least 70% of the ziprasidone therein dissolves within 45 minutes. 9. A method of treating a psychosis, comprising administering to a patient in need of such treatment an effective amount of a composition as defined in claim 1. 10. A method as defined in claim 9, wherein said composition comprises ziprasidone hydrochloride monohydrate. 11. A method as defined in claim 9, wherein said mean particle size is equal to or less than 50 .mu.m. 12. A method as defined in claim 11, wherein said mean particle size is from 5 to 50 .mu.m. 13. A method as defined in claim 12, wherein said mean particle size is from 5 to 40 .mu.m. 14. A method as defined in claim 13, wherein said mean particle size is from 5 to 30 .mu.m. 15. A method as defined in claim 9 wherein said composition exhibits an AUC and/or C.sub.max that is at least 80% of the mean AUC and/or C.sub.max observed for an equivalent composition differing only in that the ziprasidone hydrochloride particle size is 20 .mu.m. 16. A method as defined in claim 9 wherein, when an amount of said composition equivalent to 100 mgA or less of ziprasidone is placed in a USP-2 apparatus containing 900 ml of aqueous NaH.sub.2 PO.sub.4 buffer, pH 7.5, containing 2% (w/v) sodium dodecyl sulfate, and equipped with paddles stirring at 75 rpm, at least 70% of the ziprasidone therein dissolves within 45 minutes. 17. A composition comprising crystalline ziprasidone free base or crystalline ziprasidone hydrochloride particles having a mean particle size equal to or less than about 85 .mu.m, as measured by Malvern light scattering, and a pharmaceutically acceptable carrier, said composition exhibiting a mean AUC and/or C.sub.max which is at least 80% of the mean AUC exhibited by a composition equivalent thereto but differing only in that it has a crystalline ziprasidone hydrochloride mean particle size of 20 .mu.m. 18. A composition as defined in clam 17, which comprises crystalline ziprasidone hydrochloride monohydrate. 19. A composition as defined in claim 17, wherein said mean particle size is equal to or less than 50 .mu.m. 20. A composition as defined in claim 19, wherein said mean particle size is from 5 to 50 .mu.m. 21. A composition as defined in claim 20, wherein said mean particle size is from 5 to 40 .mu.m. 22. A composition as defined in claim 21, wherein said mean particle size is from 5 to 30 .mu.m. 23. A composition as defined in claim 17, wherein, when an amount of said composition equivalent to 100 mgA or less of ziprasidone is placed in a USP-2 apparatus containing 900 ml of aqueous NaH.sub.2 PO.sub.4 buffer, pH 7.5, containing 2% (w/v) sodium dodecyl sulfate, and equipped with paddles stirring at 75 rpm, at least 70% of the ziprasidone hydrochloride therein dissolves within 45 minutes. 24. A method of treating a psychosis, comprising administering to a patient in need of such treatment an effective amount of a composition as defined in claim 17. 25. A method as defined in claim 24, which comprises ziprasidone hydrochloride monohydrate. 26. A method as defined in claim 24, wherein said mean particle size is equal to or less than 50 .mu.m. 27. A method as defined in claim 26, wherein said mean particle size is from 5 to 50 .mu.m. 28. A method as defined in claim 27, wherein said mean particle size is from 5 to 40 .mu.m. 29. A method as defined in claim 28, wherein said mean particle size is from 5 to 30 .mu.m. 30. A method as defined in claim 24, wherein, when an amount of said composition equivalent to 100 mgA or less of ziprasidone is placed in a USP-2 apparatus containing 900 ml of aqueous NaH.sub.2 PO.sub.4, pH 7.5, containing 2% (w/v) sodium dodecyl sulfate, and equipped with paddles stirring at 75 rpm, at least 70% of the ziprasidone therein dissolves within 45 minutes. 31. A process of preparing large crystals of ziprasidone hydrochloride monohydrate, comprising the steps of: 1) dissolving ziprasidone free base in a solvent comprising THF and water, in a volume ratio of about 22-35 unit volumes of THF to about 1.5-8 volumes of water; 2) heating the solution resulting from step (1); 3) adding HCl to the solution resulting from step (2); and 4) cooling the solution resulting from step (3). 32. A process as defined in claim 31, wherein the volume ratio of THF to water in said solvent is 24-30 to 2-6. 33. A process as defined in claim 31, wherein, in said step (3), the temperature of said solution is maintained below reflux. 34. A process as defined in claim 33, wherein said temperature is 60-64.degree. C. |
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