Agglomerates by crystallization
The present invention describes novel agglomerates in crystalline form of β-lactam compounds. Furthermore, a process for the preparation of said agglomerates, wherein a solution or suspension of at least one β-lactam compound in a solvent is mixed with one or more anti-solvents has been described.
1. A process for preparing an agglomerate of potassium clavulanate, comprising;
a) dissolving or suspending a potassium clavulanate crystal in a solvent or mixture of solvents in the presence of water to form a solution or suspension;
b) contacting said solution or suspension with an anti-solvent using a nozzle sprayer and under stirring using a stirring device
thereby precipitating an agglomerate of potassium clavulanate having a weight percentage of between 0% and 10% potassium clavulanate crystals in the needle form, and with the proviso that the rosette-like crystalline form of potassium clavulanate is excluded.
2. A process according to claim 1 , wherein the ratio of the weight of the solution containing the potassium clavulanate to the anti-solvent is about 0.05 to 10 wt. %.
3. A process according to claim 1 , wherein the solvent is water, ethanol, or a mixture thereof.
4. A process according to claim 1 , wherein the anti-solvent is a ketone, an ester, or an alcohol, or a mixture thereof, optionally containing water.
5. A process according to claim 1 , wherein the stirring is performed by applying stirring devices in one or more vessels, in-line mixers or a combination thereof.
6. A process according to claim 5 , wherein the stirring device is a high shear mixer.
7. A process according to claim 1 , wherein said stirring is performed by combining and permuting different stirring devices, the speeds of said devices, the type and amount of the solvents used, and mixing one or more solvents and anti-solvents.
8. A process according to claim 1 , wherein the agglomerate has an average particle size between about 1 μm and 1500 μm.
9. A process according to claim 1 , wherein the process comprises dissolving the potassium clavulanate in a solvent, adjusting the pH to about neutral and mixing with the anti-solvent.
10. A process according to claim 8 , wherein the agglomerate has an average particle size about 100 μm.
11. A process according to claim 8 , wherein the agglomerate has an average particle size about 1000 μm.
12. A process according to claim 1 , wherein the agglomerate has a bulk density between about 0.20 g/mL and 0.60 g/mL.
13. A process according to claim 1 , wherein the agglomerate has a compressibility between about 10% and 40%, calculated as 100 times the ratio of the difference between tapped bulk density and loose bulk density to the tapped bulk density.
14. A process according to claim 1 , wherein the agglomerate further comprises amoxicillin.
15. A process according to claim 1 , wherein the agglomerate optionally contains one or more excipients.
16. A process according to claim 15 , wherein the one or more excipients are selected from the group consisting of microcrystalline cellulose and silica.
17. The process of claim 1 , wherein the solvent is aqueous acetone.
18. A process for preparing potassium clavulanate in the form of an agglomerate, comprising contacting a potassium clavulanate crystal in water or ethanol in the presence of water, and contacting the resulting solution with an anti-solvent using a nozzle sprayer and under stirring using a stirring device to cause precipitation of an agglomerate comprising potassium clavulanate,
wherein said agglomerate has a weight percentage of between 0% and 10% potassium clavulanate crystals in the needle form, and with the proviso that the rosette-like crystalline form of potassium clavulanate is excluded.
19. The process of claim 18 , wherein the potassium clavulanate in water further comprises acetone.
20. The process of claim 18 , wherein said anti-solvent is acetone or ethyl acetate.
21. The process of claim 1 , wherein said solution or suspension is pumped through said nozzle to a vessel containing said antisolvent.
22. The process of claim 21 , wherein said vessel is equipped with a stirring device.
23. The process of claim 22 , wherein said stirring device is a high shear mixer.
24. The process of claim 21 , wherein an additional portion of antisolvent is simultaneously added to the vessel.