IP Library Granted Patent US 10,865,224
Granted Patent B2
US 10,865,224 · App. 15/654,876 · Granted Dec 15, 2020

Purification of biological molecules

Inventors: Alex Xenopoulos (Cambridge, MA); Michael Phillips (Billerica, MA); Wilson Moya (Carlisle, MA); Jad Jaber (Sudbury, MA); Mikhail Kozlov (Lexington, MA); Ajish Potty (Missouri City, TX); Matthew T. Stone (Arlington, MA); William Cataldo (Bradford, MA); Christopher Gillespie (Shirley, MA)
Assignee: EMD Millipore Corporation
C07K1/36B01D15/125B01D15/1871B01D15/362B01D15/363C07K16/00C12M29/04C12M43/00C12M47/12C12N7/00B01D15/3809B01D15/3847C07K2317/14
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Quick Facts
Patent No.
US 10,865,224
App. No.
15/654,876
Granted
Dec 15, 2020
Kind
B2
Abstract

The present invention relates to improved processes and systems for purification of biological molecules, where the processes can be performed in a continuous manner.

Claims (36)

1. A continuous process for the purification of a target molecule comprising the steps of:

a) providing a sample comprising the target molecule and one or more impurities;

b) adding at least one precipitant to the sample and removing one or more impurities, thereby to recover a clarified sample;

c) subjecting the clarified sample from step (b) to a bind and elute chromatography step comprising at least two separation units, thereby to obtain an eluate comprising the target molecule; and

d) subjecting the eluate to flow-through purification comprising use of two or more media, one of which is activated carbon and the other(s) are selected from anion-exchange chromatography media and cation-exchange chromatography media;

wherein at least two steps are performed concurrently for at least a portion of their duration, wherein the process comprises only one bind and elute chromatography step, and wherein the process is a continuous process,

wherein the process comprises use of one or more surge tanks and/or one or more static mixers, wherein the flow-through purification is carried out as: activated carbon followed by anion-exchange chromatography media followed by cation-exchange chromatography media, and

wherein the in-line static mixer and/or surge tank is used between anion-exchange chromatography media and cation-exchange chromatography media to change pH.

2. The process of claim 1 , comprising a virus inactivation step between steps (c) and (d).

3. The process of claim 2 , wherein the virus inactivation step comprises use of a virus inactivating agent selected from acid, detergent, solvent and temperature change.

4. The process of claim 2 , wherein virus inactivation step comprises use of one or more in-line static mixers.

5. The process of claim 2 , wherein virus inactivation comprises use of one or more surge tanks.

6. The process of claim 1 , wherein the target molecule is an antibody.

7. The process of claim 6 , wherein the antibody is selected from a monoclonal antibody or a polyclonal antibody.

8. The process of claim 1 , wherein the precipitant in step (b) is a stimulus responsive polymer.

9. The process of claim 8 , wherein the stimulus responsive polymer is a modified polyallylamine polymer.

10. The process of claim 1 , wherein the precipitant in step (b) is selected from the group consisting of an acid, caprylic acid, a flocculant and a salt.

11. The process of claim 1 , wherein removing impurities in step (b) comprises use of one or more depth filters.

12. The process of claim 1 , wherein removing impurities in step (b) comprises use of centrifugation.

13. The process of claim 1 , wherein the bind and elute chromatography step in (c) employs continuous multi-column chromatography.

14. The process of claim 1 , wherein the bind and elute chromatography step in (c) is selected from the group consisting of affinity chromatography, cation exchange chromatography and mixed-mode chromatography.

15. The process of claim 1 , wherein the bind and elute chromatography step in (c) employs Protein A affinity chromatography.

16. The process of claim 15 , wherein Protein A affinity chromatography employs a Protein A ligand coupled to a matrix selected from the group consisting of rigid hydrophilic polyvinylether polymer, controlled pore glass and agarose.

17. The process of claim 1 , wherein the sample in step (a) is a cell culture.

18. The process of claim 17 , wherein the cell culture is provided in a bioreactor.

19. The process of claim 18 , wherein the bioreactor is a single use bioreactor.

20. The process of claim 17 , wherein the cell culture is provided in a vessel other than a bioreactor.

21. The process of claim 1 , wherein the precipitant in step (b) is added to a bioreactor comprising a cell culture.

22. The process of claim 21 , wherein the precipitant is added using a static mixer.

23. The process of claim 1 , wherein the precipitant in step (b) is added to a vessel other than a bioreactor which comprises the sample comprising the target molecule.

24. The process of claim 1 , wherein the flow-through purification in step (d) further comprises use of a virus filtration membrane.

25. The process of claim 1 , wherein the cation exchange chromatography media is in the form of a membrane, a bead or a fiber.

26. The process of claim 1 , wherein the process comprises use of one or more surge tanks and does not employ any pool tanks between process steps.

27. The process of claim 1 , further comprising a formulation step.

28. The process of claim 27 , wherein formulation comprises diafiltration, concentration and sterile filtration.

29. The process of claim 28 , further concentration comprises tangential flow filtration.

Assignments (1)
CHANGE OF ADDRESS Recorded Feb 15, 2018
From: EMD MILLIPORE CORPORATION
To: EMD MILLIPORE CORPORATION
Reel/Frame 045341/0166 →