IP Library Granted Patent US 11,384,378
Granted Patent B2
US 11,384,378 · App. 15/316,147 · Granted Jul 12, 2022

Methods for harvesting mammalian cell cultures

Inventors: Chetan Goudar (Newbury Park, CA); Sean Cole (Ventura, CA); Nicole Le (Camarillo, CA); Henry Lin (Fremont, CA); Jonathan Lull (Thousand Oaks, CA); Tharmala Tharmalingam (Thousand Oaks, CA)
Assignee: AMGEN INC.
C12P21/00C07K16/00C12M29/04C12M29/10C12M29/16C12M33/14C12M41/48C12M47/02C12N5/0018C07K2317/14C12N2510/02C12N2511/00
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Quick Facts
Patent No.
US 11,384,378
App. No.
15/316,147
Granted
Jul 12, 2022
Kind
B2
Abstract

The invention provides methods and materials for culturing mammalian cells and harvesting recombinant protein.

Claims (20)

1. A method for harvesting a recombinant protein comprising

establishing a cell culture by inoculating a bioreactor with mammalian cells expressing a recombinant protein,

maintaining the cell culture by perfusing the cell culture with fresh cell culture media formulated or supplemented to achieve a concentration of at least 1 g/L of a non-ionic block copolymer and passing the cell culture through a hollow fiber filter having a pore size or molecular weight cut off that retains the recombinant protein in the bioreactor, and;

once a predetermined parameter is reached perfusing the cell culture with fresh cell culture medium formulated or supplemented to achieve a concentration of at least 2, 3, 4, or 5 g/L of a non-ionic block copolymer and passing the cell culture through a hollow fiber filter having a pore size or molecular weight cut off that does not retain the recombinant protein in the bioreactor and

collecting a permeate containing the recombinant protein.

2. The method according to claim 1 , wherein the hollow fiber filter having a pore size or molecular weight cut off that retains the recombinant protein in the bioreactor and the hollow fiber filter having a pore size or molecular weight cut off that does not retain the recombinant protein in the bioreactor are components of a single unit filter system.

3. The method of claim 1 , wherein the non-ionic block copolymer is polyoxypropylene-polyoxyethylene.

4. The method of claim 1 , wherein the non-ionic block copolymer is poloxamer 188.

5. The method of claim 1 , wherein the cell culture medium used for perfusion further comprises a non-ionic surfactant.

6. The method of claim 1 , wherein the cell culture medium used for perfusion further comprises polyvinyl alcohol, polyethylene glycosl, alkyl poly(ethylene oxide), copolymers of poly(ethylene oxide), copolymers of poly(propylene oxide), poly(vinylpyrrolidone), alkyl polyglucosides, fatty alcohols, or cocamides.

7. The method of claim 1 or 2 , wherein the hollow fiber filter having a pore size or molecular weight cut off that does not retain the recombinant protein in the bioreactor is a microfilter.

8. The method of claim 7 , wherein the molecular weight cutoff of the microfilter is at least 500 kDa.

9. The method of claim 7 , wherein the molecular weight cutoff of the microfilter is 750 kDa.

10. The method of claim 7 , wherein the pore size of the microfilter is 0.1 micrometers to 10 micrometers.

11. The method of claim 1 or 2 , wherein the hollow fiber filter having a pore size or molecular weight cut off that retains the recombinant protein in the bioreactor is an ultrafilter.

12. The method of claim 11 , wherein the molecular weight cutoff of the ultrafilter is 300 kDa or less.

13. The method of claim 11 , wherein the molecular weight cutoff of the ultrafilter is 30 kDa.

14. The method of claim 11 , wherein the pore size of the ultrafilter is 0.01 micrometers to 0.1 micrometers.

15. The method of claim 2 , wherein the single unit filter system is contained within a housing.

16. The method of claim 2 , wherein the single unit filter system further comprises a spacer between at least two of the hollow fiber filter components.

Continuity (2)
Provisional Application 62007588 · Jun 4, 2014
Related Publication 20170114381A1 · Apr 27, 2017