Claims
- 1. A process for preparing amorphous paroxetine hydrochloride, which comprises mixing a carboxylic acid salt of paroxetine with hydrogen chloride and isolating the amorphous paroxetine hydrochloride.
- 2. The process of claim 1, wherein about 1.0 to about 4.0 mole equivalents of the hydrochloric acid to the paroxetine salt is utilized.
- 3. The process of claim 1, wherein the carboxylic acid salt of paroxetine and the hydrogen chloride are mixed in a solvent.
- 4. The process of claim 3, wherein the solvent is a low boiling linear alkanol or ester thereof.
- 5. The process of claim 4, wherein the solvent is ethanol.
- 6. The process of claim 1, wherein the carboxylic acid salt of paroxetine is selected from the group consisting of paroxetine formate, paroxetine acetate, paroxetine propionate, and paroxetine trifluoroacetate.
- 7. The process of claim 6, wherein the carboxylic acid salt of paroxetine is paroxetine acetate.
- 8. The process of claim 3, wherein the solvent is an alkanol and wherein the process further comprises conversion of a free carboxylic acid to an ester corresponding to the solvent alkanol.
- 9. The process of claim 8, wherein the free carboxylic acid is converted to the ester in the presence of excess hydrochloric acid in an amount of 0.01 to 0.1 mole equivalents of the paroxetine salt.
- 10. The process of claim 8, wherein the amount of solvent utilized maintains the solubility of the paroxetine hydrochloride in solution at 14° C. to 75° C.
- 11. The process of claim 3, further comprising removal of all or a portion of the solvent.
- 12. The process of claim 11, wherein the solvent is removed by evaporation.
- 13. The process of claim 12, wherein the evaporation is carried out at an elevated temperature, reduced pressure, or elevated temperature and reduced pressure.
- 14. The process of claim 12, wherein the evaporation is carried out by a rotary evaporator.
- 15. The process of claim 12, wherein the evaporation is carried out at a temperature of 35° C. to 75° C. and a pressure of 300 Torr to 10 Torr.
- 16. The process of claim 12, wherein the evaporation yields the paroxetine hydrochloride in the form of an oil.
- 17. The process of claim 16, wherein the oil is formed and maintained at about 60 Torr to 10 Torr and at 35 to 75° C.
- 18. The process of claim 16, which further comprises removing all or part of the solvent from the oil to yield the amorphous paroxetine hydrochloride in the form of a foam.
- 19. The process of claim 18, wherein the solvent is removed at a temperature of 35° C. to 75° C. and a pressure of 60 Torr to 0.01 Torr.
- 20. The process of claim 18, wherein the temperature is about 60° C. and the pressure is about 30 to about 0.1 Torr.
- 21. The process of claim 18, wherein a rotary evaporator is used for the production of foam.
- 22. The process of claim 18, which further comprises drying the foam to produce the amorphous paroxetine hydrochloride as a free flowing solid.
- 23. The process of claim 22, wherein the drying is carried out in an oven.
- 24. The process of claim 23, wherein the oven is a vacuum oven.
- 25. The process of claim 1, wherein the paroxetine hydrochloride amorphous is substantially pure.
- 26. The process of claim 1, wherein the paroxetine hydrochloride comprises less than 10% wt/wt of an alkanol.
- 27. The process of claim 26, wherein the alkanol is ethanol.
- 28. The process of claim 1, wherein the paroxetine hydrochloride comprises about 0.01% to about 3% wt/wt of water.
- 29. A process for purifying paroxetine free base, which comprises
mixing paroxetine free base in a water immiscible organic solvent with water and an acid to yield a water soluble paroxetine salt in water, removing the organic solvent, mixing the water soluble paroxetine salt in water with a water immiscible organic solvent and an aqueous base to yield purified paroxetine free base in the organic solvent; and separating the organic solvent having purified paroxetine free base from the mixture.
- 30. The process of claim 29, wherein the acid is a carboxylic acid and the water soluble paroxetine salt is a carboxylic acid salt of paroxetine.
- 31. The process of claim 30, wherein the carboxylic acid is acetic acid or formic acid and the carboxylic acid salt is paroxetine acetate or paroxetine formate.
- 32. The process of claim 29, wherein the water immiscible organic solvent is toluene.
- 33. A process for determining the content of paroxetine free base in a solution, which comprises
removing an aliquot from the solution; evaporating solvent from the aliquot to yield paroxetine free base as an oil that is substantially free of solvent; and calculating the amount of free base in the solution from the amount of paroxetine free base obtained as the oil in the aliquot.
- 34. A process for preparing a solid paroxetine salt, which comprises
mixing paroxetine free base in a water immiscible organic solvent with water and a first acid to yield a water soluble paroxetine salt in water, removing the organic solvent, mixing the water soluble paroxetine salt in water with a water immiscible organic solvent and an aqueous base to yield purified paroxetine free base in the water immiscible solvent; separating the organic solvent having purified paroxetine free base from the mixture; and mixing the purified paroxetine free base with a second acid in a solvent and isolating the solid paroxetine salt.
- 35. The process of claim 34, wherein the solvent is toluene.
- 36. The process of claim 34, wherein the second acid is a carboxylic acid.
- 37. The process of claim 36, wherein the carboxylic acid is selected from the group consisting of formic acid, acetic acid, propionic acid, and trifluoroacetic acid.
- 38. The process of claim 36, wherein the ratio of the volume of purified free base in solvent to the weight of purified free base is about 7.5 to about 10 milliliters per gram and the amount of the carboxylic acid is about 1 mole equivalent to paroxetine free base in the solution.
- 39. The process of claim 34, wherein the acid is selected from the group consisting of sulfuric acid, phosphoric acid, and carbonic acid.
- 40. The process of claim 39, wherein the acid is sulfuric acid, the solvent is an alcohol, and the molar ratio of sulfuric acid to paroxetine free base is about 0.5.
- 41. The process of claim 39, wherein the acid is phosphoric acid and the molar ratio of phosphoric acid to paroxetine free base is about 1.0.
- 42. A composition of matter comprising paroxetine acetate, characterized as having IR absorption bands at 653, 785, 795, 841, 935, 985, 1036, 1105, 1141, 1187, 1219, 1241, 1269, 1382, 1421, 1471, 1489, 1503, 1512, 1629, 1654, 2888, 2934, 3056, 3083±4 cm−1, and having X-ray powder diffraction peaks at 19.1, 20.4 and 21.5 (2 Theta degree).
- 43. A composition of matter comprising paroxetine formate, characterized as having IR absorption bands at 762, 785, 837, 934, 1040, 1138, 1188, 1218, 1245, 1269, 1343, 1365, 1382, 1471, 1489, 1505, 1571, 1634, 1689, 1784, 1891, 3045±4 cm−1, and having X-ray powder diffraction peaks at 19.4, 20.1 and 23.1 (2 Theta degree).
- 44. A composition of matter comprising paroxetine trifluoroacetate.
- 45. The composition of matter of claim 44, wherein the paroxetine trifluoroacetate has a melting point that is less than or equal to 117° C.
- 46. A composition of matter comprising paroxetine carbonate or paroxetine hydrogen carbonate.
- 47. A composition of matter comprising paroxetine sulfate or paroxetine hydrogen sulfate.
- 48. The composition of claim 47, wherein the composition of matter comprises paroxetine sulfate having a melting point that is less than or equal to 245° C.
- 49. A composition of matter comprising paroxetine phosphate, paroxetine hydrogen phosphate, or paroxetine dihydrogen phosphate.
- 50. The composition of claim 51, wherein the composition comprises paroxetine dihydrogen phosphate having a melting point that is less than or equal to 208° C.
- 51. A process for preparing a paroxetine salt, comprising
contacting paroxetine free base in an organic solvent with an acid selected from the group consisting of sulfuric acid, phosphoric acid, propionic acid, trifluoroacetic acid, and carbonic acid; and isolating the paroxetine salt.
CROSS-REFERENCE TO RELATED APPLICATIONS
[0001] This application claims the benefit of the Apr. 25, 2001 filing date of U.S. application Ser. No. 60/286,590, the May 11, 2001 filing date of U.S. application Ser. No. 60/290,411, and the Jun. 1, 2001 filing date of U.S. application Ser. No. 60/295,471, each of which is entitled “Paroxetine Salts And Processes For The Manufacture Of Paroxetine Salts” and names S. Upadhyaya and B. Ronsen as inventors. This application also claims the benefit of the Nov. 20, 2001 filing date for U.S. application Ser. No. 60/333,530, which is entitled “Optimized Procedures for the Manufacture of Paroxetine Salts” and names S. Upadhyaya and B. Ronsen as inventors. Each of these applications is incorporated herein by reference in its entirety.
Provisional Applications (4)
|
Number |
Date |
Country |
|
60333530 |
Nov 2001 |
US |
|
60295471 |
Jun 2001 |
US |
|
60290411 |
May 2001 |
US |
|
60286590 |
Apr 2001 |
US |