High-cell density fed-batch fermentation process for producing recombinant protein
Methods for producing proteins, for example, recombinant meningococcal 2086 proteins, using fed-batch fermentation with continuous input of an inducer after achieving a threshold parameter, and optionally continuous input of a carbon source, for example, a constant rate input, to improve protein yields, as well as high density protein compositions and compositions for use in the methods of the present invention, are provided.
1. A method for producing a recombinant protein comprising:
culturing a recombinant bacterial cell to express a recombinant protein comprising continuously adding a carbon source to a culture comprising the recombinant bacterial cell and continuously adding an inducer to the culture after the culture achieves a threshold parameter, and isolating the recombinant protein from the culture, wherein the total amount of the inducer added to the culture during inducer feed is from 7 g/L to 15 g/L based on the total volume of the culture.
2. The method of claim 1 , wherein the threshold parameter is optical density (OD), dissolved oxygen (DO), concentration of nutrient in culture medium, total concentration of carbon source added to culture medium, or any combination thereof.
3. The method of claim 2 , wherein the threshold parameter is optical density (OD) of the culture.
4. The method of claim 3 , comprising continuously adding the inducer to the culture when the cell density of the culture achieves an OD 600 of about 70 to about 110.
5. The method of claim 4 , comprising continuously adding the inducer to the culture when the cell density of the culture achieves an OD 600 of about 70 to about 105.
6. The method of claim 5 , comprising continuously adding the inducer to the culture when the cell density of the culture achieves an OD 600 of about 75 to about 85.
7. The method of claim 6 , comprising continuously adding the inducer to the culture when cell density of the culture achieves an OD 600 of about 80.
8. The method of claim 1 , comprising adding the inducer to the culture at a constant rate, wherein the inducer is added to the culture by DO-stat feed or pH-stat feed.
9. The method of claim 1 , comprising adding the inducer to the culture at a constant rate of 3.35 g/L/h to 16 g/L/h, wherein the inducer is added to the culture by DO-stat feed or by pH-stat feed.
10. The method of claim 1 , wherein the total amount of the inducer added to the culture is from about 8 g/L to about 14 g/L.
11. The method of claim 10 , wherein the total amount of the inducer added to the culture during inducer feed is from about 9 g/L to about 11 g/L.
12. The method of claim 11 , wherein the total amount of the inducer added to the culture during inducer feed is about 10 g/L.
13. The method of claim 1 , comprising continuously adding the inducer to the culture for about 2 to about 8 hours after initiation of the method.
14. The method of claim 13 , comprising continuously adding the inducer to the culture for about 3 to about 6 hours after initiation.
15. The method of claim 1 , comprising isolating the recombinant protein about 2 to about 8 hours after starting to add the inducer to the culture.
16. The method of claim 15 , comprising isolating the recombinant protein about 3 to about 6 hours after starting to add the inducer to the culture.
17. The method of claim 1 , wherein the inducer is arabinose.
18. The method of claim 1 , comprising continuously adding the carbon source to the culture before induction.
19. The method of claim 1 , comprising continuously adding the carbon source to the culture before and during induction.
20. The method of claim 1 , comprising continuously adding the carbon source to the culture while the inducer is continuously added to the culture.
21. The method of claim 1 , comprising continuously adding the carbon source to the culture until the cell density of the culture achieves an OD 600 of about 70 to about 110.
22. The method of claim 1 , wherein the carbon source is a sugar-based carbon source.
23. The method of claim 22 , wherein the sugar-based carbon source is glucose.
24. The method of claim 1 , wherein the inducer is arabinose.
25. The method of claim 24 , comprising continuously adding the glucose to the culture medium while the arabinose is continuously added to the culture medium.
26. The method of claim 24 , comprising continuously adding the glucose until the cell density of the culture achieves an OD 600 of about 80.
27. A method for producing a recombinant protein comprising:
(a) introducing into a bacterial host cell an expression vector encoding a recombinant protein under the control of an inducible promoter to form a recombinant bacterial cell;
(b) introducing the recombinant bacterial cell into a culture medium to form a cell culture;
(c) adding a carbon source to the cell culture as a continuous feed;
(d) monitoring cell growth in the cell culture for achievement of a threshold optical density (OD 600 );
(e) adding an inducer of the inducible promoter to the cell culture as a continuous feed once the threshold optical density (OD 600 ) is achieved, wherein the total amount of inducer added to the culture is from 7 g/L to 15 g/L based on the total volume of the culture; and
(f) isolating the recombinant protein from the cell culture.
28. The method of claim 27 , comprising continuously adding the inducer to the culture when the cell density of the culture achieves an OD 600 of about 70 to about 110.
29. The method of claim 28 , comprising continuously adding the inducer to the culture when the cell density of the culture achieves an OD 600 of about 70 to about 105.
30. The method of claim 29 , comprising continuously adding the inducer to the culture when the cell density of the culture achieves an OD 600 of about 75 to about 85.
31. The method of claim 30 , comprising continuously adding the inducer to the culture when the cell density of the culture achieves an OD 600 of about 80.
32. The method of claim 27 , wherein the inducer is added to the culture at a constant rate, and wherein the inducer is added to the culture by DO-stat feed or pH-stat feed.
33. The method of claim 32 , wherein the inducer is added to the culture at a constant rate of from about 3.35 g/L/h to about 16 g/L/h.
34. The method of claim 27 , wherein the total amount of inducer added to the culture is about 10 g/L.
35. The method of claim 27 , comprising isolating the recombinant protein from the culture about 2 hours to about 8 hours after initiation of inducer feed.
36. The method of claim 35 , comprising isolating the recombinant protein from the culture about 3 hours to about 6 hours after initiation of inducer feed.
37. The method of claim 27 , wherein the carbon source is added to the cell culture during constant rate feed of both the carbon source and the inducer, during DO-stat feed of both the carbon source and the inducer or during pH-stat feed of both the carbon source and the inducer.
38. The method of claim 27 , wherein the inducer is arabinose.
39. The method of claim 27 , wherein the carbon source is a sugar-based carbon source.
40. The method of claim 39 , wherein the sugar-based carbon source is glucose.
41. The method of claim 27 , wherein the carbon source is glucose and the inducer is arabinose.
42. The method of claim 41 , comprising continuously adding glucose to the cell culture while the arabinose is continuously added to the cell culture.
43. The method of claim 41 , comprising continuously adding glucose to the cell culture until the cell density of the cell culture achieves an OD 600 of about 80.
44. A method for producing a recombinant protein comprising:
culturing a recombinant bacterial cell to express a recombinant protein by continuously adding an inducer to a culture comprising the bacterial cell after the culture achieves a threshold parameter, wherein the bacterial cell comprises a nucleic acid sequence for the gene of Neisseria meningitidis serogroup B, and wherein the total amount of inducer added to the culture is from 7 g/L to 15 g/L based on the total volume of the culture.
45. The method of claim 44 , wherein the threshold parameter is optical density (OD), dissolved oxygen (DO), pH, concentration of nutrient in culture medium, total concentration of carbon source added to culture medium, or any combination thereof.
46. The method of claim 45 , wherein the threshold parameter is optical density (OD) of the culture.
47. The method of claim 46 , wherein the continuous inducer feed is initiated when the cell density of the culture achieves an OD 600 of about 70 to about 110.
48. The method of claim 47 , wherein the continuous inducer feed is initiated when the cell density of the culture achieves an OD 600 of about 70 to about 105.
49. The method of claim 48 , wherein the continuous inducer feed is initiated when the cell density of the culture achieves an OD 600 of about 75 to about 85.
50. The method of claim 49 , wherein the continuous inducer feed is initiated when the cell density of the culture achieves an OD 600 of about 80.
51. The method of claim 44 , wherein the inducer is added to the culture at a constant rate of about 3.35 g/L/h to about 16 g/L/h, and wherein the inducer is added by DO-stat feed or pH-stat feed.
52. The method of claim 44 , wherein the total amount of inducer added to the culture during induction is about 10 g/L.
53. The method of claim 44 , wherein the inducer feed continues for about 2 hours to about 8 hours after initiation of the method.
54. The method of claim 53 , wherein the inducer feed continues for about 3 hours to about 6 hours after initiation of the method.
55. The method of claim 44 , wherein the recombinant protein is harvested from about 2 hours to about 8 hours after initiation of inducer feed.
56. The method of claim 55 , wherein the recombinant protein product is isolated from about 3 hours to about 6 hours after initiation of inducer feed.
57. The method of claim 44 , wherein the carbon source feed to the culture medium continues during inducer feed to the culture.
58. The method of claim 44 , wherein the inducer is arabinose.
59. The method of claim 44 , wherein the carbon source is a sugar-based carbon source.
60. The method of claim 59 , wherein the sugar-based carbon source is glucose.
61. The method of claim 60 , wherein the inducer is arabinose.
62. The method of claim 61 , wherein glucose is fed to the culture at a constant feed rate while adding the arabinose to the culture by DO-stat feed or by pH-stat feed of both the glucose and the inducer.
63. The method of claim 62 , wherein cell density in the culture achieves an OD 600 of about 80.
64. The method of claim 44 , wherein the recombinant protein is a meningococcal 2086 protein.
65. The method of claim 64 , wherein the meningococcal 2086 protein is non-lipidated.
66. The method of claim 64 , wherein the meningococcal 2086 protein is a subfamily A protein.
67. The method of claim 64 , wherein the meningococcal 2086 protein is a subfamily B protein.
68. A method for producing a recombinant meningococcal 2086 protein (P2086) comprising:
(a) introducing into a bacterial host cell an expression vector encoding a recombinant meningococcal 2086 protein under the control of an inducible promoter to form a recombinant bacterial cell;
(b) introducing the recombinant bacterial cell to a culture medium to form a culture;
(c) adding glucose to the culture;
(d) monitoring cell growth in the culture for achievement of a threshold optical density (OD);
(e) continuously adding an inducer of the inducible promoter to the culture once the cell density of the culture achieves an optical density of 70 to 110, wherein the total amount of inducer added to the culture is from 7 g/L to 15 g/L based on the total volume of the culture, and wherein the inducer is arabinose; and
(f) isolating the recombinant meningococcal 2086 protein from the culture after 3 to 6 hours after commencement of continuously adding the inducer.
69. The method of claim 1 , wherein the recombinant protein is a meningococcal 2086 protein.
70. The method of claim 69 , wherein the meningococcal 2086 protein is non-lipidated.
71. The method of claim 69 , wherein the meningococcal 2086 protein is lipidated.
72. The method of claim 69 , wherein the meningococcal 2086 protein is a subfamily A protein.
73. The method of claim 69 , wherein the meningococcal 2086 protein is a subfamily B protein.
74. The method of claim 27 , wherein the recombinant protein is a meningococcal 2086 protein.
75. The method of claim 74 , wherein the meningococcal 2086 protein is non-lipidated.
76. The method of claim 74 , wherein the meningococcal 2086 protein is lipidated.
77. The method of claim 74 , wherein the meningococcal 2086 protein is a subfamily A protein.
78. The method of claim 74 , wherein the meningococcal 2086 protein is a subfamily B protein.
79. The method of claim 64 , wherein the meningococcal 2086 protein is lipidated.