Manufacturing of bupivacaine multivesicular liposomes

Patent metadata

Field	Value
Publication number	US-11819574-B2
Application number	US-202217719716-A
Country	US
Kind code	B2
Filing date	Apr 13, 2022
Priority date	Jan 22, 2021
Publication date	Nov 21, 2023
Grant date	Nov 21, 2023

Abstract

Embodiments of the present application relate to batches of bupivacaine multivesicular liposomes (MVLs) prepared by a commercial manufacturing process using independently operating dual tangential flow filtration modules.

First claim

What is claimed is:

1. Batches comprising compositions of bupivacaine encapsulated multivesicular liposomes (MVLs) prepared by a process, the process of preparing a batch comprising:
(a) mixing a first aqueous solution comprising phosphoric acid with a volatile water-immiscible solvent solution to form a first water-in-oil emulsion, wherein the volatile water-immiscible solvent solution comprises bupivacaine, 1, 2-dierucoylphosphatidylcholine (DEPC), 1, 2-dipalmitoyl- sn-glycero-3 phospho-rac-(1-glycerol) (DPPG), and at least one neutral lipid;
(b) mixing the first water-in-oil emulsion with a second aqueous solution to form a second water-in-oil-in-water emulsion, wherein the second aqueous solution comprises lysine;
(c) removing the volatile water-immiscible solvent from the second water-in-oil-in-water emulsion to form a first aqueous suspension of bupivacaine encapsulated MVLs having a first volume;
(d) reducing the first volume of the first aqueous suspension of bupivacaine encapsulated MVLs by microfiltration to provide a second aqueous suspension of bupivacaine encapsulated MVLs having a second volume;
(e) exchanging the aqueous supernatant of the second aqueous suspension with a saline solution by diafiltration to provide a third aqueous suspension of bupivacaine encapsulated MVLs having a third volume; and
(f) further reducing the third volume of the third aqueous suspension by microfiltration to provide a final aqueous suspension of bupivacaine encapsulated MVLs having a bupivacaine concentration from about 11.3 mg/mL to about 17.0 mg/mL;
wherein each batch has a volume of about 100 L to about 250 L; and
wherein an average erucic acid concentration of at least three batches prepared by the process is about 105 μg/mL or less when measured after the compositions are stored at 25° C. for six months.

2. The batches of claim 1 , wherein the average erucic acid concentration of the at least three batches is about 99 μg/mL or less when measured after the compositions are stored at 25° C. for six months.

3. The batches of claim 1 , wherein the average erucic acid concentration of the at least three batches is greater than about 53 μg/mL, when measured after the compositions are stored at 25° C. for six months.

4. The batches of claim 2 , wherein the average erucic acid concentration of the at least three batches is greater than about 53 μg/mL, when measured after the compositions are stored at 25° C. for six months.

5. The batches of claim 1 , wherein the compositions of the batches have an initial pH of about 7.0 to about 7.4.

6. The batches of claim 1 , wherein the compositions of the batches have a pH of about 6.5 when measured after the compositions are stored at 25° C. for six months.

7. The batches of claim 1 , wherein the at least one neutral lipid in the volatile water-immiscible solvent solution comprises tricaprylin.

8. The batches of claim 1 , wherein the volatile water-immiscible solvent solution further comprises cholesterol.

9. The batches of claim 1 , wherein the bupivacaine concentration in the compositions of the batches is about 13.3 mg/mL.

10. The batches of claim 1 , wherein the compositions of the batches comprise less than 5% by weight unencapsulated bupivacaine.

11. The batches of claim 1 , wherein the d 50 of the MVLs in the compositions of the batches is about 24 μm to about 31 μm.

12. The batches of claim 1 , wherein the percent packed particle volume (% PPV) of the bupivacaine encapsulated MVLs in the compositions of the batches is about 35% to about 40%.

13. The batches of claim 1 , wherein the DEPC and DPPG in the compositions of the batches are in a mass ratio of about 7:1 to about 10:1.

14. The batches of claim 1 , wherein the bupivacaine is in a salt form.

15. The batches of claim 14 , wherein the bupivacaine is in the form of bupivacaine phosphate.

16. The batches of claim 1 , wherein the final aqueous suspension comprises a saline solution.

17. The batches of claim 1 , wherein the mixing in step (a) is performed using a first mixer at a high shear speed from about 1100 rpm to about 1200 rpm.

18. The batches of claim 17 , wherein the high sheer speed is about 1150 rpm.

19. The batches of claim 17 , wherein a mixing time in step (a) is about 65 to about 75 minutes.

20. The batches of claim 1 , wherein the mixing in step (b) is performed using a second mixer at a low shear speed from about 450 rpm to about 510 rpm.

21. The batches of claim 20 , wherein the low shear speed is about 495 rpm.

22. The batches of claim 20 , wherein a mixing time in step (b) is about 60 to about 65 seconds.

23. A method of treating or ameliorating pain in a subject in need thereof, comprising administering a composition of a batch of claim 1 to the subject.

24. The method of claim 23 , wherein the administration is via local infiltration to a surgical site to provide postsurgical local analgesia.

25. The method of claim 23 , wherein the administration is via interscalene brachial plexus nerve block or femoral nerve block to provide postsurgical regional analgesia.

26. The method of claim 23 , wherein the composition has a volume of 10 mL or 20 mL for a single-dose administration.

27. The batches of claim 17 , wherein the first mixer has a blade diameter of about 8 inches to about 10 inches.

28. The batches of claim 20 , wherein the second mixer has a blade diameter of about 10 inches to about 15 inches.

29. The batches of claim 1 , wherein the compositions of the batches comprise lysine encapsulated in the internal aqueous chambers of the MVLs, and the encapsulated lysine concentrations in the compositions of the batches are at least about 5% higher than the encapsulated lysine concentration of a bupivacaine encapsulated MVL product (Exparel®) manufactured by a 45 L commercial process.

30. The batches of claim 29 , wherein the encapsulated lysine concentration in the compositions of the batches is about 0.03 mg/mL.

31. The batches of claim 30 , wherein the compositions of the batches have an initial pH of about 7.0 to about 7.4.

32. The batches of claim 31 , the compositions of the batches have a pH of about 6.5 when measured after the compositions are stored at 25° C. for six months.

33. The batches of claim 30 , wherein the bupivacaine concentration in the compositions of the batches is about 13.3 mg/mL.

34. The batches of claim 30 , wherein the compositions of the batches comprise less than 5% by weight unencapsulated bupivacaine.

35. The batches of claim 30 , wherein the mixing in step (a) is performed using a first mixer at a high shear speed from about 1100 rpm to about 1200 rpm.

36. The batches of claim 35 , wherein a mixing time in step (a) is about 65 to about 75 minutes.

37. The bathes of claim 35 , wherein the first mixer has a blade diameter of about 8 inches to about 10 inches.

38. The batches of claim 30 , wherein the mixing in step (b) is performed using a second mixer at a low shear speed from about 450 rpm to about 510 rpm.

39. The batches of claim 38 , wherein a mixing time in step (b) is about 60 to about 65 seconds.

40. The batches of claim 38 , wherein the second mixer has a blade d

Assignees

• Pacira Pharmaceuticals Inc

Inventors

• Hall Jeffrey S
• Turnbull David J
• Grigsby Jr John J
• Ardekani Soroush M
• Los Kathleen D A

Classifications

• B01D61/1471

  comprising multiple microfiltration steps · CPC title

• A61K9/1277 Primary

  Preparation processes; Proliposomes · CPC title

• A61K31/451 Primary

  having a carbocyclic group directly attached to the heterocyclic ring, e.g. glutethimide, meperidine, loperamide, phencyclidine, piminodine · CPC title

• B01D61/146

  comprising multiple ultrafiltration steps · CPC title

• B01D61/147

  Microfiltration · CPC title