Continuous microsphere process

• US 5,945,126 A
• Filed: 02/13/1997
• Issued: 08/31/1999
• Est. Priority Date: 02/13/1997
• Status: Expired due to Term

• Current Assignee: Oakwood Laboratories LLC
• Original Assignee: Oakwood Laboratories LLC
• Inventors: Thanoo, Bagavathikanun Chithambara, Murtagh, James
• Primary Examiner(s): Page, Thurman K.
• Assistant Examiner(s): Benston, Jr., William E.
• Application Number:
  US08/800,924
• Time in Patent Office: 929 Days
• Field of Search: 424/497, 424/489, 424/486, 424/425
• US Class Current: 424/489
• CPC Class Codes: A61K 9/1647 Polyesters, e.g. poly(lactide-co-glycolide)
• CPC Class Codes: A61K 9/1694 resulting in granules or microspheres of the matrix type containing more than 5% of excipient
• CPC Class Codes: B01J 13/02 Making microcapsules or microballoons for medical preparations A61K9/50

Abstract

A continuous process for producing microspheres wherein small particle sizes can be obtained without the problem of foaming. A drug and polymer containing dispersed phase is continuously introduced into a high intensity emulsification vessel along with a continuous phase. An emulsion of the dispersed phase is formed in the continuous phase by high intensity mixing effective to quickly solidify the dispersed phase polymer without having to take steps to address foaming.

Claims

1. A continuous method of making active agent containing polymer bodies comprising:

a) forming a dispersed phase comprising active agent and polymer;

b) providing a continuous phase in which said dispersed phase will form an emulsion;

c) continuously introducing dispersed phase into a reactor vessel at a dispersed phase feed rate, and continuous phase into said reactor vessel at a continuous phase feed rate, said reactor vessel including means for forming an emulsion, and forming an emulsion of said dispersed phase in said continuous phase;

d) continuously transporting said emulsion from said reactor vessel to a solvent removal vessel to remove solvent.

2. The method of claim 1 wherein said dispersed phase is fed to said reaction vessel at a rate of from about 4 ml/min to about 400 ml/min, and said continuous phase is fed to said reactor vessel at a rate of from about 1000 ml/min. to about 20,000 ml/min.

3. The method according to claim 1 wherein said dispersed phase includes a hydrophilic peptide active agent and a copolymer of lactide and glycolide, and comprising emulsifying said dispersed and continuous phases in a manner effective to provide an average particle size of from about 5 μ

m to about 40 μ

m, and an active agent load of at least about 9%.

4. The method according to claim 1 wherein said dispersed phase includes a hydrophilic peptide active agent and a copolymer of lactide and glycolide, and comprising emulsifying said dispersed and continuous phases in a manner effective to provide an average particle size of from about 5 μ

m to about 40 μ

m, and an active agent load of at least about 15%.

5. The method of claim 1 wherein said continuous phase and dispersed phase are introduced into said reactor in a ratio of from 5:

1 to 500;

1.

6. The method of claim 1 wherein said continuous phase and dispersed phase are introduced into said reactor in a ratio of from 40:

1 to 200;

1.

7. The method of claim 1 wherein said means for forming an emulsion comprises an impeller.

8. The method of claim 1 wherein said means for forming an emulsion comprises an impeller and said mixing is performed by running said impeller in excess of about 5,000 revolutions per minute.

9. The method of claim 1 wherein said means for forming an emulsion comprises an impeller, said impeller having a diameter defining a diameter of a cylindrical zone extending axially from said impeller, and wherein said dispersed phase is introduced into said axially extending zone.

10. The method of claim 1 wherein said means for forming an emulsion produces a mixing zone effective to cause solidification of dispersed phase polymer within about 10 seconds, and said dispersed phase is introduced into said reaction vessel in said mixing zone.

11. The method of claim 1 wherein said dispersed phase is a homogeneous solution.

12. The method of claim 1 wherein said dispersed phase is an emulsion.

13. The method according to claim 1 wherein the average residence time of said dispersed phase in said reactor is less than about 5 seconds.

14. The method of claim 1 comprising emulsifying said dispersed and continuous phases in a manner adapted to cause solidification of said dispersed phase polymer within about 10 seconds.

15. The method of claim 1 comprising emulsifying said dispersed and continuous phases in a manner adapted to cause solidification of said dispersed phase polymer within about 5 seconds.

16. The method of claim 1 wherein said means for forming an emulsion comprises an impeller and said step of forming said emulsion comprises running said impeller in excess of from about 6,000 to about 10,000 revolutions per minute.

17. The method according to claim 1 wherein said method steps are carried out for a period sufficient to produce a desired population of microspheres, and wherein microspheres produced at the beginning of said period have substantially the same size and agent load as microspheres produced at the end of said period.

18. A microsphere made by the method of claim 1.

19. A microsphere made by the method of claim 3.

20. A microsphere made by the method of claim 14.

21. The method of claim 1 comprising providing an aqueous continuous phase.

22. The method of claim 1 comprising carrying out said steps for a period sufficient to produce a desired population of polymer bodies, and wherein said polymer bodies produced at the beginning of said period have substantially the same size distribution as the polymer bodies produced at the end of said period.

23. The method of claim 1 comprising carrying out said steps for a period sufficient to produce a desired population of polymer bodies, and wherein said polymer bodies produced at the beginning of said period have substantially the same agent load as the polymer bodies produced at the end of said period.

24. The method of claim 1 comprising providing an aqueous continuous phase, and forming said dispersed phase to include LHRH or an analog thereof and a copolymer of lactide and glycolide, and wherein solidification of said dispersed phase commences within about 10 seconds.

25. The method of claim 1 wherein said continuous phase and dispersed phase feed rates are controlled independently of said means of forming said emulsion.

26. The method of claim 1 wherein said means of forming said emulsion comprises an in-line mixer, and a mixing intensity for forming said emulsion is controlled independently of said continuous phase and dispersed phase feed rates.