Fermentation process capable of improving production level of recombinant human collagen

一种人源胶原蛋白、发酵工艺的技术,应用在提高重组人源胶原蛋白生产水平的发酵工艺领域,能够解决蛋白表达量和发酵水平低、发酵周期长、发酵水平低等问题,达到发酵水平提高、发酵时间缩短、表达量增加的效果

Active Publication Date: 2016-11-16
ZHEJIANG ZHUJI JUYUAN BIOTECHNOLOGY CO LTD
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  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Compared with the traditional process, the fermentation process of genetically engineered bacteria of collagen has the advantages of easy availability of raw materials, environmental protection, and stable product quality, but there are also problems such as longer fermentation cycle and lower production efficiency.
Chinese patent 201010602214.8 discloses a production method for expressing recombinant human-like collagen in Pichia pastoris. Pichia pastoris C13 is used as the strain, the expression level of recombinant collagen is 5g / L, the fermentation period is 99 hours, and the fermentation level 0.051g / L·h, although the fermentation cycle is short, the protein expression and fermentation level are too low
Chinese patent 201110327865.5 constructed a Pichia pastoris genetically engineered strain of recombinant human collagen. The genetically engineered strain was fermented to obtain recombinant human collagen. The fermentation period was 136 hours, and the protein expression was 16g / L. The level is 0.118g / L·h, although the protein expression has increased, but the fermentation period is too long and the fermentation level is low

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0017] 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.

[0018] The seed liquid is added in the 1000L fermenter that contains 500L fermentation medium according to the inoculation amount of 10%, the initial stirring speed is 200rpm, the tank pressure is 0.05MPa, and the air flow and speed are adjusted to make dissolved oxygen (DO) > 30%. 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 212g / L, and the glycerin supplement was stopped. At this time, the fermentation and cultivation time was 16 hours. After the glycerin was exhausted, methanol was added to enter the methanol induction culture stage, and sodium pyruvate was added at one time at the same time, and the addition amount was 0.01g / L fermentation medium. Adjust the rotation speed, ai...

Embodiment 2

[0020] 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; glycerin 40.0g / L; PTM1 4.35mL / L.

[0021] The seed liquid is added in the 1000L fermenter that contains 500L fermentation medium according to the inoculation amount of 10%, the initial stirring speed is 200rpm, the tank pressure is 0.05MPa, and the air flow and speed are adjusted to make dissolved oxygen (DO) > 30%. 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 210g / L, and the glycerin supplement was stopped. At this time, the fermentation and cultivation time was 16 hours. After the glycerol was exhausted, methanol was added to enter the stage of methanol induction culture, and sodium pyruvate was added at one time at a rate of 10 g / L. Adjust the rotation speed, air flow rate and feed methanol speed to make dissol...

Embodiment 3

[0023] 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.

[0024] The seed liquid is added in the 1000L fermenter that contains 500L fermentation medium according to the inoculation amount of 10%, the initial stirring speed is 200rpm, the tank pressure is 0.05MPa, and the air flow and speed are adjusted to make dissolved oxygen (DO) > 30%. 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 216g / L, and the glycerin supplement was stopped. At this time, the fermentation and cultivation time was 17 hours. After the glycerol was exhausted, methanol was added to enter the stage of methanol induction culture, and sodium pyruvate was added at one time at a rate of 0.1 g / L. Adjust the rotation speed, air flow rate and feed methanol speed to make disso...

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Abstract

The invention discloses a fermentation process capable of improving the production level of recombinant human collagen. The fermentation process comprises the following steps: firstly inoculating a Pichia pastoris strain liquid into a sterilized fermentation culture medium, fermentatively culturing for 14 to 18 hours, refilling methanol to carry out induction expression, simultaneously adding sodium pyruvate to the fermentation culture medium, wherein the sodium pyruvate is added in an amount of 0.01 to 10 g / L. In the fermentation process, the sodium pyruvate is added in the methanol-induced expression stage, so that the biosynthesis rate of the recombinant human collagen is improved; a continuous feed-batch way is adopted, so that the biosynthesis rate of the recombinant human collagen is further improved, and the fermentation time is shortened; meanwhile, the expression quantity of the recombinant human collagen is increased, the fermentation level is increased by more than 20%, and the production cost is reduced; the fermentation process is especially suitable for industrialized mass production of recombinant human collagen, and can bring huge practical application value for industrial production.

Description

technical field [0001] The invention belongs to the technical field of biological fermentation and relates to a fermentation process for improving the production level of recombinant human collagen. Background technique [0002] Collagen is an important protein in animals. It is widely distributed in tissues such as skin, cartilage, and blood vessels. It participates in cell migration, differentiation, and reproduction, and plays an important role in maintaining the normal physiological functions of cells, tissues, and organs. It is used in food , Feed, beauty, cosmetics, medicine and other fields are widely used. At present, collagen raw materials are mainly obtained by separation and purification after treating animal skin, bone and other tissues such as pigs and cattle with physical and chemical methods such as acid, alkali and heating. However, the collagen obtained by the above method has complex components and poor water solubility, and because it comes from animal ti...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C12P21/02C12R1/84
CPCC07K14/78C12P21/02C12R2001/84C12N1/16C12N1/38C12N1/165
Inventor 杜尔凤黄建民高力虎赵健烽陶海冯丽萍周爱梅季乐
Owner ZHEJIANG ZHUJI JUYUAN BIOTECHNOLOGY CO LTD
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