Adjusting ph to improve the fermentation process of recombinant human collagen production level
A human-derived collagen, production-level technology, applied in animal/human protein, fermentation, microorganism-based methods, etc., can solve the problems of low protein expression and fermentation level, low production efficiency, long fermentation cycle, etc. The effect of improving the level, saving production costs, and increasing the rate of biosynthesis
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Embodiment 1
[0016] Fermentation medium: 85% H 3 PO 4 26.7mL / L; CaSO 4 2H 2 O 1.175g / L; K 2 SO 4 18.2g / L; MgSO 4 ·7H 2 O 14.9g / L; KOH 4.13g / L; glycerol 40.0g / L; PTM1 4.35mL / L.
[0017] Add the seed liquid to the 1000L fermenter containing 500L fermentation medium according to the inoculation amount of 10%, the initial stirring speed is 200rpm, the tank pressure is 0.05MPa, the air flow and the speed are adjusted to make dissolved oxygen (DO) > 30%, and the initial stage control The pH is 5.2. When the carbon source was exhausted, the dissolved oxygen rose sharply, and 50% glycerin was added to supplement the carbon source until the wet weight of the bacteria was 214g / L, and the glycerin supplement was stopped. At this time, the fermentation and cultivation time was 18 hours. After the glycerol was exhausted, the pH was controlled to be 5.0, and methanol was started to flow into the stage of methanol induction culture. Adjust the rotation speed, air flow rate and feed methanol spe...
Embodiment 2
[0019] Fermentation medium: 85% H 3 PO 4 26.7mL / L; CaSO 4 2H 2 O 1.175g / L; K 2 SO 4 18.2g / L; MgSO 4 ·7H 2 O 14.9g / L; KOH 4.13g / L; glycerol 40.0g / L; PTM1 4.35mL / L.
[0020] Add the seed liquid to the 1000L fermenter containing 500L fermentation medium according to the inoculation amount of 10%, the initial stirring speed is 200rpm, the tank pressure is 0.05MPa, the air flow and the speed are adjusted to make dissolved oxygen (DO) > 30%, and the initial stage control The pH is 5.2. When the carbon source was exhausted, the dissolved oxygen rose sharply, and 50% glycerin was added to supplement the carbon source until the wet weight of the bacteria was 214g / L, and the glycerin supplement was stopped. At this time, the fermentation and cultivation time was 18 hours. After the glycerol was exhausted, the pH was controlled to 4.8, and methanol was started to be fed into the methanol-induced culture stage. Adjust the rotation speed, air flow rate and feed methanol speed to...
Embodiment 3
[0022] Fermentation medium: 85% H 3 PO 4 26.7mL / L; CaSO 4 2H 2 O 1.175g / L; K 2 SO 4 18.2g / L; MgSO 4 ·7H 2 O 14.9g / L; KOH 4.13g / L; glycerol 40.0g / L; PTM1 4.35mL / L.
[0023] Add the seed liquid to the 1000L fermenter containing 500L fermentation medium according to the inoculation amount of 10%, the initial stirring speed is 200rpm, the tank pressure is 0.05MPa, the air flow and the speed are adjusted to make dissolved oxygen (DO) > 30%, and the initial stage control The pH is 5.3. When the carbon source was exhausted, the dissolved oxygen rose sharply, and 50% glycerin was added to supplement the carbon source until the wet weight of the bacteria was 214g / L, and the glycerin supplement was stopped. At this time, the fermentation and cultivation time was 18 hours. After the glycerol was exhausted, the pH was controlled to 4.8, and methanol was started to be fed into the methanol-induced culture stage. Adjust the rotation speed, air flow rate and feed methanol speed to...
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