WO2008104956A2 - Procédé de préparation de cabergoline amorphe - Google Patents
Procédé de préparation de cabergoline amorphe Download PDFInfo
- Publication number
- WO2008104956A2 WO2008104956A2 PCT/IB2008/050735 IB2008050735W WO2008104956A2 WO 2008104956 A2 WO2008104956 A2 WO 2008104956A2 IB 2008050735 W IB2008050735 W IB 2008050735W WO 2008104956 A2 WO2008104956 A2 WO 2008104956A2
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- cabergoline
- amorphous
- organic solvent
- process according
- thin film
- Prior art date
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D457/00—Heterocyclic compounds containing indolo [4, 3-f, g] quinoline ring systems, e.g. derivatives of ergoline, of the formula:, e.g. lysergic acid
- C07D457/04—Heterocyclic compounds containing indolo [4, 3-f, g] quinoline ring systems, e.g. derivatives of ergoline, of the formula:, e.g. lysergic acid with carbon atoms having three bonds to hetero atoms with at the most one bond to halogen, e.g. ester or nitrile radicals, directly attached in position 8
- C07D457/06—Lysergic acid amides
Definitions
- the present invention relates to processes for the preparation of amorphous cabergoline by agitated thin film drying or spray drying.
- Cabergoline is indicated for the treatment of hyperprolactinemic disorders, either idiopathic or due to pituitary adenomas.
- GB 2,074,566 B provides a process for preparing cabergoline, wherein the final product is isolated as a diphosphate salt.
- WO 03/078433 provides a process for preparing a mixture of amorphous cabergoline and Form I, by drying the toluene solvate Form V.
- WO 04/094368 provides processes for preparing amorphous cabergoline from tert-butyl methyl ether solvate Form A by vacuum drying or lyophilization.
- WO 05/085243 provides a process for preparing amorphous cabergoline, wherein the process involves dissolving chromatographically purified oily cabergoline in acetone and partially removing the solvent several times in vacuum.
- the present inventors have developed novel processes for preparing amorphous cabergoline.
- the present processes do not require lyophilization or repeated crystallizations.
- the present process is simple and provides amorphous cabergoline in a single step by agitated thin film drying or spray drying.
- the present processes also provide amorphous cabergoline substantially free from crystalline contamination.
- collecting includes unloading, amassing, gathering, scaling and/or piling.
- a process for the preparation of amorphous cabergoline comprises, a) dissolving cabergoline in an organic solvent, b) removing the solvent from the solution obtained in step a) by agitated thin film drying, and c) collecting amorphous cabergoline from the agitated thin film dryer.
- Cabergoline present in any solid or solvated form known to the person skilled in the art can be used as a starting material.
- Cabergoline present in oily form can also be used as a starting material.
- the starting material of cabergoline can be prepared according to the methods provided in the prior art references, for example, WO 03/078433.
- the cabergoline is dissolved in an organic solvent.
- the organic solvent is selected from a group consisting of acetone, diethyl ether, cyclohexane and isopropanol.
- the organic solvent is preferably acetone.
- the solution so obtained is filtered and fed to an agitated thin film dryer.
- the solvent is subsequently removed from the solution by agitated thin film drying.
- the drying process is accompanied by heating at a temperature of about 35 0 C or above.
- the feeding rate of the solution is controlled in such a way to facilitate the thin film formation and the evaporation rate.
- the rotor and vapor duct can have a sealing system so that the drying can preferably be carried under vacuum. Vacuum operation also facilitates amorphous cabergoline to be obtained without degradation.
- the amorphous cabergoline is collected from the agitated thin film dryer.
- the amorphous cabergoline can optionally be further dried under vacuum to obtain amorphous cabergoline with desired residual solvent content.
- the amorphous cabergoline so obtained has substantially the same XRPD pattern as depicted in Figure 1.
- a process for the preparation of amorphous cabergoline comprises, a) dissolving cabergoline in an organic solvent, b) removing the solvent from the solution obtained in step a) by spray drying, and c) collecting amorphous cabergoline from the spray dryer.
- Cabergoline for use as the starting material in the processes described herein can be prepared according to the methods provided in the prior art references, for example, WO
- Cabergoline is dissolved in an organic solvent.
- the organic solvent is selected from a group consisting of acetone, diethyl ether, cyclohexane and isopropanol.
- the organic solvent is preferably acetone.
- the solution is filtered and fed to a spray dryer.
- the inlet and outlet temperatures, feed rate, and atomizer type can be adjusted to optimize output and particle size.
- the air inlet temperature is preferably controlled from about 5O 0 C to about 80 0 C.
- the outlet temperature is preferably controlled from about 35 0 C to about 45 0 C.
- an inert gas for example, nitrogen gas can be used as a carrier gas.
- the cabergoline is collected from the spray dryer and optionally further dried under vacuum to obtain amorphous cabergoline with desired residual solvent content.
- the amorphous cabergoline so obtained has substantially the same XRPD pattern as depicted in Figure 2.
- Figure 1 depicts XRPD of amorphous cabergoHne obtained by agitated thin film drying.
- Figure 2 depicts XRPD of amorphous cabergoline obtained by spray drying.
- Powder XRD of the samples were determined by using X-Ray Difractometer, Rigaku Corporation, RU-H3R, Goniometer CN2155A3, X-Ray tube with Cu target anode, Divergence slits 1 0, Receiving slit 0.15mm, Scatter slit 1°, Power: 40 KV, 100 mA, Scanning speed: 2 deg/min step: 0.02 deg, Wave length: 1.5406 A.
- Nozzle Diameter 0.5 mm
- Carrier gas Nitrogen at 2 to 2.2 kg/cm 2 Air inlet temperature: 50°-52°C Outlet temperature: 45°C
- Type of atomizer Two fluids nozzle
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Pharmaceuticals Containing Other Organic And Inorganic Compounds (AREA)
- Nitrogen Condensed Heterocyclic Rings (AREA)
Abstract
L'invention concerne des procédés de préparation de cabergoline amorphe par séchage de film mince par agitation ou par séchage par pulvérisation.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
IN450DE2007 | 2007-02-28 | ||
IN450/DEL/2007 | 2007-02-28 |
Publications (2)
Publication Number | Publication Date |
---|---|
WO2008104956A2 true WO2008104956A2 (fr) | 2008-09-04 |
WO2008104956A3 WO2008104956A3 (fr) | 2009-08-13 |
Family
ID=39672747
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/IB2008/050735 WO2008104956A2 (fr) | 2007-02-28 | 2008-02-28 | Procédé de préparation de cabergoline amorphe |
Country Status (1)
Country | Link |
---|---|
WO (1) | WO2008104956A2 (fr) |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2004094368A2 (fr) * | 2003-04-21 | 2004-11-04 | Finetech Laboratories, Ltd. | Formes nouvelles de cabergoline |
WO2005085243A2 (fr) * | 2004-03-04 | 2005-09-15 | Richter Gedeon Vegyészeti Gyár Rt. | Nouveau procede de production de la cabergoline |
-
2008
- 2008-02-28 WO PCT/IB2008/050735 patent/WO2008104956A2/fr active Application Filing
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2004094368A2 (fr) * | 2003-04-21 | 2004-11-04 | Finetech Laboratories, Ltd. | Formes nouvelles de cabergoline |
WO2005085243A2 (fr) * | 2004-03-04 | 2005-09-15 | Richter Gedeon Vegyészeti Gyár Rt. | Nouveau procede de production de la cabergoline |
Non-Patent Citations (1)
Title |
---|
ASHFORD S W ET AL: "A practical synthesis of cabergoline" JOURNAL OF ORGANIC CHEMISTRY, vol. 67, no. 20, 4 October 2002 (2002-10-04), pages 7147-7150, XP002491857 USA ISSN: 0022-3263 cited in the application * |
Also Published As
Publication number | Publication date |
---|---|
WO2008104956A3 (fr) | 2009-08-13 |
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