Production of a polypeptide in a serum-free cell culture liquid containing plant protein hydrolysate
The invention concerns a method for large-scale production of a polypeptide in eukaryote cells contained in a serum-free culture liquid, said method comprising (i) a propagation phase for said cells, where the cells are propagated in a first cell culture liquid, and (ii) a production phase for said cells, where the cells are present in a second cell culture medium liquid, wherein each of the cell culture liquids comprise a plant protein hydrolysate, and wherein the ratio between the concentration of the plant protein hydrolysate (C 1 ) in the first cell culture liquid and the concentration of the plant protein hydrolysate (C 2 ) in the second cell culture liquid is at least 1.5:1 (C 1 :C 2 ).
1. A method for large-scale production of a polypeptide in eukaryote cells contained in a serum-free culture liquid, said method comprising
(i) a propagation phase for said cells, where the cells are propagated in a first cell culture liquid, and
(ii) a production phase for said cells, where the cells are present in a second cell culture liquid,
wherein each of the cell culture liquids comprise a plant protein hydrolysate, and wherein the ratio between the concentration of the plant protein hydrolysate (C 1 ) in the first cell culture liquid and the concentration of the plant protein hydrolysate (C 2 ) in the second cell culture liquid is at least 1.5:1 (C 1 :C 2 ).
2. The method according to claim 1 , wherein the ratio C 1 :C 2 is in the range of 2:1 to 10:1.
3. The method according to claim 2 , wherein the concentration C 2 is in the range of 0.2-3.5 g/L.
4. The method according to claim 3 , wherein the concentration C 1 is in the range of 4.0-10.0 g/L.
5. The method according to claim 4 , wherein the plant protein hydrolysate is soy protein hydrolysate.
6. The method according to claim 5 , wherein the polypeptide is a Factor VII polypeptide.
7. A method for large-scale production of a Factor VII polypeptide in eukaryote cells contained in a serum-free culture liquid, said method comprising
(i) a propagation phase for said cells, where the cells are propagated in a first cell culture liquid, and
(ii) a production phase for said cells, where the cells are present in a second cell culture liquid,
wherein the first cell culture liquid comprises a soy protein hydrolysate in a concentration of 4.0-10.0 g/L, the second cell culture liquid comprises a soy protein hydrolysate in a concentration of 0.2-3.5 g/L, and wherein the ratio between the concentration of the soy protein hydrolysate (C 1 ) in the first cell culture liquid and the concentration of the soy protein hydrolysate (C 2 ) in the second cell culture liquid is at least 1.5:1 (C 1 :C 2 ).
8. A method for large-scale production of a Factor VII polypeptide in eukaryote cells contained in a serum-free culture liquid, said method comprising
(i) a propagation phase for said cells, where the cells are propagated in a first cell culture liquid, and
(ii) a production phase for said cells, where the cells are present in a second cell culture liquid,
wherein each of the cell culture liquids comprise a plant protein hydrolysate, and wherein the concentration of the plant protein hydrolysate (C 2 ) in the second cell culture liquid is in the range of 0.7-3.0 g/L.
9. The method according to claim 8 , wherein the concentration C 2 is in the range of 0.9-2.5 g/L.
10. The method according to claim 9 , wherein each of the cell culture liquids comprise a plant protein hydrolysate, and wherein the ratio between the concentration of the plant protein hydrolysate (C 1 ) in the first cell culture liquid and the concentration of the plant protein hydrolysate (C 2 ) in the second cell culture liquid is at least 1.5:1.
11. The method according to claim 10 , wherein the concentration C 1 is in the range of 4.0-10.0 g/L.
12. The method according to claim 1 , wherein the concentration of the plant protein hydrolysate observed against time of fermentation has the following profile:
high concentration in the propagation phase (C 1 );
low concentration in the production phase—low level A (C 2A );
low concentration in the production phase—low level B (C 2B );
low concentration in the production phase—low level A (C 2A );
low concentration in the production phase—low level B (C 2B );
where C 1 >>C 2B >C 2A and the concentrations C 2A and C 2B are within the concentration ranges specified for C 2 , and wherein a first switch from low level A (C 2A ) to low level B (C 2B ) is conducted when a decrease in the cell number is observed and a subsequent switch from low level B (C 2B ) to low level A (C 2A ) is conducted when the cell number has been restored to a level approximately corresponding to the level before the decrease.
13. The method according to claim 6 , wherein the concentration of the plant protein hydrolysate observed against time of fermentation has the following profile:
high concentration in the propagation phase (C 1 );
low concentration in the production phase—low level A (C 2A );
low concentration in the production phase—low level B (C 2B );
low concentration in the production phase—low level A (C 2A );
low concentration in the production phase—low level B (C 2B );
where C 1 >>C 2B >C 2A and the concentrations C 2A and C 2B are within the concentration ranges specified for C 2 , and wherein a first switch from low level A (C 2A ) to low level B (C 2B ) is conducted when a decrease in the cell number is observed and a subsequent switch from low level B (C 2B ) to low level A (C 2A ) is conducted when the cell number has been restored to a level approximately corresponding to the level before the decrease.
14. The method according to claim 7 , wherein the concentration of the plant protein hydrolysate observed against time of fermentation has the following profile:
high concentration in the propagation phase (C 1 );
low concentration in the production phase—low level A (C 2A );
low concentration in the production phase—low level B (C 2B );
low concentration in the production phase—low level A (C 2A );
low concentration in the production phase—low level B (C 2B );
where C 1 >>C 2B >C 2A and the concentrations C 2A and C 2B are within the concentration ranges specified for C 2 , and wherein a first switch from low level A (C 2A ) to low level B (C 2B ) is conducted when a decrease in the cell number is observed and a subsequent switch from low level B (C 2B ) to low level A (C 2A ) is conducted when the cell number has been restored to a level approximately corresponding to the level before the decrease.
15. The method according to claim 8 , wherein the concentration of the plant protein hydrolysate observed against time of fermentation has the following profile:
high concentration in the propagation phase (C 1 );
low concentration in the production phase—low level A (C 2A );
low concentration in the production phase—low level B (C 2B );
low concentration in the production phase—low level A (C 2A );
low concentration in the production phase—low level B (C 2B );
where C 1 >>C 2B >C 2A and the concentrations C 2A and C 2B are within the concentration ranges specified for C 2 , and wherein a first switch from low level A (C 2A ) to low level B (C 2B ) is conducted when a decrease in the cell number is observed and a subsequent switch from low level B (C 2B ) to low level A (C 2A ) is conducted when the cell number has been restored to a level approximately corresponding to the level before the decrease.
16. The method according to claim 1 , wherein the concentration C 2 is in the range of 0.2-3.5 g/L.
17. The method according to claim 1 , wherein the concentration C 1 is in the range of 4.0-10.0 g/L.
18. The method according to claim 1 , wherein the plant protein hydrolysate is soy protein hydrolysate.
19. The method according to claim 1 , wherein the polypeptide is a Factor VII polypeptide.
20. The method according to claim 8 , wherein each of the cell culture liquids comprise a plant protein hydrolysate, and wherein the ratio between the concentration of the plant protein hydrolysate (C 1 ) in the first cell culture liquid and the concentration of the plant protein hydrolysate (C 2 ) in the second cell culture liquid is at least 1.5:1.