IP Library Granted Patent US 10,570,367
Granted Patent B2
US 10,570,367 · App. 14/733,630 · Granted Feb 25, 2020

Seed train processes and uses thereof

Inventors: Michael Bruninghaus (Framingham, MA); Konstantin Konstantinov (Waban, MA); Benjamin Wright (Framingham, MA); Weichang Zhou (Framingham, MA)
Assignee: Genzyme Corporation
C12N5/0062C12N5/00C12N2510/02C12N2511/00
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Quick Facts
Patent No.
US 10,570,367
App. No.
14/733,630
Granted
Feb 25, 2020
Kind
B2
Abstract

Provided herein are seed train processes and methods of producing a recombinant protein that include the use of these seed train processes.

Claims (74)

1. A method of producing a recombinant protein, wherein the method consists of:

(a) disposing a plurality of recombinant mammalian cells into a first culture medium within a vessel to provide a first cell culture;

(b) batch culturing the first cell culture to a cell density range of about 1.0×10 6 cells/mL to about 5.0×10 6 cells/mL;

(c) disposing a volume of the first cell culture of step (b) into a second culture medium within a perfusion bioreactor to provide a second cell culture with an initial cell density in a range of about 0.25×10 6 cells/mL to about 0.5×10 6 cells/mL;

(d) perfusion culturing the second cell culture to a cell density range of about 5×10 6 cells/mL to about 120×10 6 cells/mL;

(e) disposing a volume of the second cell culture of step (d) into a third culture medium within a production bioreactor to provide a production cell culture with an initial cell density in a range of about 0.25×10 6 cells/mL to about 8×10 6 cells/mL;

(f) perfusion culturing the production cell culture under conditions that allow the recombinant mammalian cells to secrete a recombinant protein; and

(g) harvesting the recombinant protein from the production cell culture.

2. The method of claim 1 , wherein the step of disposing the plurality of recombinant mammalian cells in (a) to provide a first cell culture consists of:

thawing a frozen cell bank; and

disposing a volume of the thawed cell bank into the first culture medium.

3. The method of claim 1 , wherein the step of disposing the plurality of recombinant mammalian cells in (a) to provide a first cell culture consists of disposing a volume of cultured recombinant mammalian cells into the first culture medium.

4. The method of claim 1 , wherein:

the first cell culture in (a) has a volume range of about 1.0 L to about 50 L;

the second cell culture in (c) has a volume range of about 5 L to about 600 L; and/or

the production cell culture in (e) has a volume range of about 50 L to about 20,000 L.

5. The method of claim 1 , wherein:

the vessel in (a) has an internal volume range of about 1.5 L to about 100 L;

the perfusion bioreactor in (c) has an internal volume range of about 7.5 L to about 1,000 L; and/or

the production bioreactor in (e) has an internal volume range of about 150 L to about 25,000 L.

6. The method of claim 1 , wherein:

the initial cell density in the production cell culture is in a range of about 2.0×10 6 cells/mL to about 8×10 6 cells/mL; and/or

the initial cell density in the production cell culture is at least 10% of a steady state production cell density.

7. A method of producing a recombinant protein, wherein the method consists of:

(a) disposing a plurality of recombinant mammalian cells into a fourth culture medium within a vessel to provide a third cell culture;

(b) batch culturing the third cell culture of (a) to a cell density range of about 1.0×10 6 cells/mL to about 5.0×10 6 cells/mL;

(c) disposing a volume of the third cell culture of (b) into a first culture medium within a vessel to provide a first cell culture;

(d) batch culturing the first cell culture to a cell density range of about 1.0×10 6 cells/mL to about 5.0×10 6 cells/mL;

(e) disposing a volume of the first cell culture of step (d) into a second culture medium within a perfusion bioreactor to provide a second cell culture with an initial cell density in a range of about 0.25×10 6 cells/mL to about 0.5×10 6 cells/mL;

(f) perfusion culturing the second cell culture to a cell density range of about 5×10 6 cells/mL to about 120×10 6 cells/mL;

(g) disposing a volume of the second cell culture of step (f) into a third culture medium within a production bioreactor to provide a production cell culture with an initial cell density in a range of about 0.25×10 6 cells/mL to about 8×10 6 cells/mL;

(h) perfusion culturing the production cell culture under conditions that allow the recombinant mammalian cells to secrete a recombinant protein; and

(i) harvesting the recombinant protein from the production cell culture.

8. The method of claim 7 , wherein the step of disposing the plurality of the recombinant mammalian cells in (a) to provide the third cell culture consists of:

thawing a frozen cell bank; and

disposing a volume of the thawed cell bank into the fourth culture medium.

9. A method of producing a recombinant protein, wherein the method consists of:

(a) disposing a plurality of recombinant mammalian cells into a first culture medium within a vessel to provide a first cell culture;

(b) batch culturing the first cell culture to a cell density range of about 1.0×10 6 cells/mL to about 5.0×10 6 cells/mL;

(c) disposing a volume of the first cell culture medium of (b) into a second culture medium within a perfusion bioreactor to provide a second cell culture with an initial cell density in a range of about 0.25×10 6 cells/mL to about 0.5×10 6 cells/mL;

(d) perfusion culturing the second cell culture to a cell density range of about 5×10 6 cells/mL to about 60×10 6 cells/mL;

(e) disposing a volume of the second cell culture of (d) into a third culture medium within a production bioreactor to provide a production cell culture with an initial cell density in a range of about 0.5×10 6 cells/mL to about 10×10 6 cells/mL;

(f) perfusion culturing the production cell culture under conditions that allow the recombinant mammalian cells to secrete a recombinant protein; and

(g) harvesting the recombinant protein from the production cell culture.

10. The method of claim 9 , wherein the step of disposing the plurality of recombinant mammalian cells in (a) to provide the first cell culture consists of:

thawing a frozen cell bank; and

disposing a volume of the thawed cell bank into the first culture medium.

11. The method of claim 9 , wherein the step of disposing the plurality of recombinant mammalian cells in (a) to provide the first cell culture consists of disposing a volume of a third cell culture consisting of the plurality of recombinant mammalian cells in a fourth cell culture medium into the first culture medium.

12. The method of claim 9 , wherein:

the first cell culture in (a) has a volume range of about 1.0 L to about 50 L;

the second cell culture in (c) has a volume range of about 5 L to about 600 L; and/or

the production cell culture in (e) has a volume range of about 50 L to about 20,000 L.

13. The method of claim 9 , wherein:

the vessel in (a) has an internal volume range of about 1.5 L to about 100 L;

the perfusion bioreactor in (c) has an internal volume range of about 7.5 L to about 1,000 L; and/or

the production bioreactor in (e) has an internal volume range of about 150 L to about 25,000 L.

14. The method of claim 9 , wherein:

the initial cell density in the production cell culture is in a range of about 2.0×10 6 cells/mL to about 8×10 6 cells/mL; and/or

the initial cell density in the production cell culture is at least 10% of a steady state production cell density.

15. The method of claim 9 , wherein the perfusion culturing in (f) results in the production cell culture reaching a steady state production cell density in a period of about 1 day to about 10 days.

16. The method of claim 9 , wherein the step of harvesting in (g) consists of removing culture medium and recombinant protein of (f) from the production bioreactor.

17. A method of producing a recombinant protein, wherein the method consists of:

(a) disposing a plurality of recombinant mammalian cells into a fourth culture medium within a vessel to provide a third cell culture;

(b) batch culturing the third cell culture in (a) to a cell density range of about 1.0×10 6 cells/mL to about 5.0×10 6 cells/mL,

(c) disposing a volume of the third cell culture into a first culture medium within a vessel to provide a first cell culture;

(d) batch culturing the first cell culture to a cell density range of about 1.0×10 6 cells/mL to about 5.0×10 6 cells/mL;

(e) disposing a volume of the first cell culture medium of (b) (d) into a second culture medium within a perfusion bioreactor to provide a second cell culture with an initial cell density in a range of about 0.25×10 6 cells/mL to about 0.5×10 6 cells/mL;

(f) perfusion culturing the second cell culture to a cell density range of about 5×10 6 cells/mL to about 60×10 6 cells/mL;

(g) disposing a volume of the second cell culture of (f) into a third culture medium within a production bioreactor to provide a production cell culture with an initial cell density in a range of about 0.5×10 6 cells/mL to about 10×10 6 cells/mL;

(h) perfusion culturing the production cell culture under conditions that allow the recombinant mammalian cells to secrete a recombinant protein; and

(i) harvesting the recombinant protein from the production cell culture.

18. The method of claim 17 , wherein the step of disposing the plurality of the recombinant mammalian cells in (a) to provide the third cell culture consists of:

thawing a frozen cell bank; and

disposing a volume of the thawed cell bank into the fourth culture medium.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Aug 11, 2015
From: BRUNINGHAUS, MICHAEL; KONSTANTINOV, KONSTANTIN; WRIGHT, BENJAMIN; ZHOU, WEICHANG
To: GENZYME CORPORATION
Reel/Frame 036298/0192 →
Continuity (2)
Provisional Application 62009553 · Jun 9, 2014
Related Publication 20150353896A1 · Dec 10, 2015
Cited By (3)
US 12,378,517 US 12,668,774 US 12,686,847