IP Library › Granted Patent US 8,513,393
Granted Patent B2
US 8,513,393 · App. 12/377,122 · Granted Aug 20, 2013

Process for the purification of Fc-containing proteins

Inventors: Alex Eon-Duval (Vevey, CH); Alain Lamproye (Bouloz, CH)
Assignee: Ares Trading S.A.
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Quick Facts
Patent No.
US 8,513,393
App. No.
12/377,122
Granted
Aug 20, 2013
Kind
B2
Abstract

The invention relates to a process for reducing the concentration of free Fc-moieties in a fluid comprising an Fc-containing protein comprising a cation exchange chromatography step.

Claims (32)

1. A method for reducing the content of free Fc-moieties in a fluid comprising an Fc-containing protein and free Fc-moieties and having a pH of at least one unit below the isoelectric point (pI) of the Fc-containing protein, the method comprising cation exchange chromatography comprising the steps of loading said fluid onto a cation exchange resin to absorb the Fc-containing protein, washing the cation exchange resin with a first buffer having a conductivity of 8.2 to 9.2 mS/cm and a pH of 6.0 to 7.0 to remove free Fc-moieties, and eluting the Fc-containing protein with a second buffer to produce an eluate comprising the Fe-containing protein, whereby the level of free Fe-moieties in said eluate relative to the level of Fe-containing protein has been reduced from said fluid by a factor of 5 to 15.

2. The method according to claim 1 , wherein the first buffer has a conductivity of 8.2 to 8.6 mS/cm.

3. The method according to claim 1 or 2 , wherein the first buffer comprises 75 to 125 mM sodium phosphate.

4. The method according to claim 1 , wherein the second buffer has a pH ranging from 7.0 to 8.5.

5. The method according to claim 4 , wherein the second buffer has a conductivity of 15 to 22 mS/cm.

6. The method according to claim 1 or 4 , wherein the cation exchange resin is a strong cation exchange resin.

7. The method according to claim 6 , wherein the cation exchange resin comprises SO 3 − groups.

8. The method according to claim 6 , wherein the resin comprises a cross-linked methacrylate matrix.

9. The method according to claim 1 or 4 , further comprising a purification step selected from affinity chromatography, anion exchange chromatography and hydroxyapatite chromatography.

10. The method according to claim 1 or 4 , wherein the Fc-containing protein comprises an Immunoglobulin (Ig) constant region.

11. The method according to claim 10 , wherein the constant region is a human constant region.

12. The method according to claim 10 , wherein the immunoglobulin is an IgG 1 .

13. The method according to claim 10 , wherein the constant region comprises a CH2 and a CH3 domain.

14. The method according to claim 1 or 4 , wherein the Fc-containing protein comprises an immunoglobulin variable region.

15. The method according to claim 14 , wherein the Fe-containing protein is an antibody.

16. The method according to claim 1 or 4 , wherein the Fc-containing protein is an Fc-fusion protein.

17. The method according to claim 16 , wherein the Fe-fusion protein comprises an extracellular domain of a member of the tumor necrosis factor receptor (TNFR) superfamily selected from the group consisting of TNFR1 and TNFR2.

18. The method according to claim 16 , wherein the Fe-fusion protein comprises an extracellular domain of BAFF-R, BCMA, or TACI.

19. The method according to claim 16 , wherein the Fe-fusion protein comprises a polypeptide selected from

a. amino acids 30 to 110 of SEQ ID NO: 2;

b. SEQ ID NO: 3; and

c SEQ ID NO: 4.

20. The method according to claim 1 , wherein free Fc-moieties constitute less than 5% of the total protein concentration of said eluate.

21. The method according to claim 1 , wherein free Fc-moieties constitute less than 2% of the total protein concentration of said eluate.

22. The method according to claim 1 , wherein free Fc-moieties constitute less than 1% of the total protein concentration of said eluate.

23. The method according to claim 1 , wherein free Fe-moieties constitute less than 0.5% of the total protein concentration of said eluate.

24. The method according to claim 1 , wherein free Fe-moieties constitute less than 0.2% of the total protein concentration of said eluate.

25. The method according to claim 1 , wherein free Fc-moieties constitute less than 0.1% of the total protein concentration of said eluate.

26. The method according to claim 9 , wherein said fluid comprising an Fc-containing protein is an eluate from an affinity chromatography purification step.

27. The method according to claim 26 , wherein said eluate having a reduced level of free Fc-moieties is subjected to anion exchange chromatography to produce an anion exchange chromatography flow-through comprising the Fc-containing protein.

28. The method according to claim 27 , wherein the anion exchange chromatography flow-through comprising the Fc-containing protein is subjected to hydroxyapatite chromatography to produce a hydroxyapatite chromatrography eluate comprising the Fc-containing protein.

29. The method according to claim 1 , wherein the first buffer has a conductivity of 8.4 to 9.2 mS/cm.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Apr 26, 2021
From: EON-DUVAL, ALEX; LAMPROYE, ALAIN
To: ARES TRADING S.A.
Reel/Frame 056043/0594 →
Continuity (1)
Related Publication 20100190961A1 · Jul 29, 2010