Process for concentration of antibodies and therapeutic products thereof

Patent metadata

Field	Value
Publication number	US-10370456-B2
Application number	US-201414257907-A
Country	US
Kind code	B2
Filing date	Apr 21, 2014
Priority date	Sep 9, 2004
Publication date	Aug 6, 2019
Grant date	Aug 6, 2019

Abstract

The present disclosure provides a process for concentrating proteins including an ultrafiltering, a diafiltering, and a second ultrafiltering sequence, at elevated temperatures, such as above about 30° C. The disclosure also includes a process for preparing highly concentrated antibody compositions, and highly concentrated antibody products.

First claim

The claimed invention is:

1. A process for preparing highly concentrated monoclonal antibody in a pharmaceutical formulation comprising:
a) concentrating a first purified antibody preparation by a first ultrafiltering to provide a second antibody preparation comprising the retentate of the first ultrafiltration in a first buffer, wherein the first purified antibody preparation has an antibody concentration of from about 0.1 to about 10 grams per liter, wherein the second antibody preparation has an antibody concentration of from about 10 to about 50 grams per liter, and wherein the first purified antibody preparation has been purified with ion-exchange chromatography prior to step a);
b) exchanging the first buffer of the second antibody preparation generated in step a) into a second buffer by a diafiltering to provide a diafiltered intermediate antibody preparation comprising the retentate of the diafiltration, wherein the second buffer comprises excipients desired in the pharmaceutical formulation;
c) concentrating the diafiltered intermediate antibody preparation generated in step b) by a second ultrafiltering to provide a third antibody preparation comprising the retentate of the second ultrafiltration, wherein the third antibody preparation is substantially free from aggregates and wherein the third antibody preparation has an antibody concentration of from about 150 to about 200 grams per liter; and
d) formulating the third antibody preparation generated in step c) into the pharmaceutical formulation suitable for therapeutic administration;
wherein the first ultrafiltering, second ultrafiltering, and the diafiltering are accomplished at 35° C. to about 50° C., and wherein the first and the second ultrafiltering are accomplished with an ultra-filter membrane having a nominal pore size of about 5 to about 50 kilo Daltons.

2. The process of claim 1 wherein one or more of the first ultrafiltering, the second ultrafiltering, and the diafiltering are accomplished at about 45° C.

3. The process of claim 1 wherein one or more of the first ultrafiltering, the second ultrafiltering, and the diafiltering are accomplished at 45° C. plus or minus 5° C.

4. The process of claim 1 wherein the first purified antibody preparation has an antibody concentration of about 1 to about 5 grams per liter.

5. The process of claim 1 wherein the second antibody preparation has an antibody concentration of about 20 to about 40 grams per liter.

6. The process of claim 1 wherein the third antibody preparation has an antibody concentration of from about 170 to about 200 grams per liter.

7. The process of claim 1 wherein the intermediate antibody preparation has an antibody concentration of about 25 to about 35 grams per liter and the third antibody preparation has an antibody concentration of from about 170 to about 200 grams per liter.

8. The process of claim 1 wherein the antibody preparation comprises an anti-IgE antibody.

9. The process of claim 1 wherein the process is accomplished in from about 1 to 10 hours.

10. The process of claim 1 wherein the process is accomplished in from about 2 to 5 hours.

11. The process of claim 1 wherein the process is accomplished in about 3 hours.

12. The process of claim 1 wherein the first and the second ultrafiltering are accomplished with an ultra-filter membrane having a nominal pore size of about 10 to about 30 kilo Daltons.

13. The process of claim 1 wherein the antibody in the first purified antibody preparation has an apparent molecular weight of about 100 to about 200 kilo Daltons.

14. The process of claim 1 wherein the antibody in the first purified antibody preparation has an apparent molecular weight of about 150 kilo Daltons.

15. The process of claim 1 wherein the first ultrafiltering concentrates the first purified antibody preparation to provide the second antibody preparation having an antibody concentration of about 30 grams per liter and the second ultrafiltering concentrates the intermediate antibody preparation to provide the third antibody preparation having an antibody concentration of about 170 to about 200 grams per liter.

16. The process of claim 1 wherein the first ultrafiltering and the second ultrafiltering are accomplished with the same ultra-filter membrane.

17. The process of claim 1 wherein the first ultrafiltering and the second ultrafiltering are accomplished with a regenerated cellulose composite ultra-filter membrane.

18. The process of claim 1 wherein the diafiltering accomplishes a buffer exchange at constant volume, constant concentration, or both.

19. The process of claim 1 wherein the diafiltering accomplishes a buffer exchange of from about 5 to about 15 fold volumes.

20. The process of claim 1 wherein the diafiltering accomplishes a buffer exchange of from about 8 fold volumes.

21. The process of claim 1 wherein the first buffer comprises a mixture of aqueous sodium chloride and a TRIS buffer, and the second buffer comprises a mixture of aqueous histidine chloride and arginine chloride.

22. The process of claim 1 wherein the first ultrafiltering, the second ultrafiltering, and the diafiltering are accomplished with tangential flow filtration across an ultra-filter membrane.

23. The process of claim 1 wherein the first ultrafiltering, the second ultrafiltering, and the diafiltering are accomplished with tangential flow filtration across the same ultra-filter membrane.

24. The process of claim 1 wherein the yield of the third antibody preparation is greater than about 70 weight percent based on the weight of antibodies in the first purified antibody preparation.

25. The process of claim 24 wherein the yield of the third antibody preparation is from about 80 to about 100 weight percent based on the weight of antibodies in the first purified antibody preparation.

26. The process of claim 1 wherein the first ultrafiltering has a recirculation rate of from about 0.5 L/min/ft 2 to about 5 L/min/ft 2 .

27. The process of claim 1 wherein the ultrafiltering and diafiltering are accomplished at a transmembrane pressure of from about 10 to about 50 p.s.i.

28. The process of claim 1 wherein there is provided an antibody concentrate with a detectable bio-burden of less than about 100 CFU/mL.

29. The process of claim 1 wherein one or more of steps a), b), and c) are accomplished at a temperature of about 40° C. to about 50° C.

30. The process of claim 1 wherein throughput for step c) is at about 80 g/ft 2 /hr, about 120 g/ft 2 /hr, about 135 g/ft 2 /hr, about 145 g/ft 2 /hr, about 175 g/ft 2 /hr, about 180 g/ft 2 /hr, about 265 g/ft 2 /hr, about 285 g/ft 2 /hr, or about 290 g/ft 2 /hr.

31. The process of claim 1 wherein the yield of the third antibody preparation is greater than about 98 weight percent based on the weight of the antibody in the first purified antibody preparation.

32. The process of claim 1 wherein steps a), b), and c) utilize an ultra-filtration membrane.

33. The process of claim 1 wherein an ultra-filtration membrane utilized in step a) is used in step b) and in step c).

34. The process of claim 1 wherein the third antibody preparation has a detectible bioburden of 1.8 CFU/ml.

35. The process of claim 1 wherein the third antibody pr

Assignees

• Genentech Inc
• Novartis Ag

Inventors

• Winter Charles M

Classifications

• B01D61/16

  Feed pretreatment · CPC title

• A61K39/39591

  Stabilisation, fragmentation · CPC title

• B01D2311/16

  Flow or flux control · CPC title

• C07K1/34 Primary

  by filtration, ultrafiltration or reverse osmosis · CPC title

• B01D2311/04

  Specific process operations in the feed stream; Feed pretreatment · CPC title