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Method for producing β-carotene by fermentation of B. trispora and β-carotene

A technology of B. trispora and carotene, which is applied in the field of fermentation engineering, can solve the problems of reducing the metabolic flux of carotenoids, reducing the unit production efficiency, and slowing down the product accumulation rate, so as to reduce energy consumption costs and simplify operations , the effect of easy process

Active Publication Date: 2021-09-21
HEFEI INSTITUTES OF PHYSICAL SCIENCE - CHINESE ACAD OF SCI +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Use KH 2 PO 4 or K 2 HPO 4 Contain PO 4 3+ If the amount of salt is too small, the phosphorylation level will be insufficient, which will greatly reduce the metabolic flux of carotenoids, and if it is too much, it will bring a large amount of K + , so that the cell membrane permeability of the bacteria becomes too strong, and the β-carotene is easily transported from the intracellular to the extracellular, so that the accumulation rate of the product is correspondingly slowed down, and the unit production efficiency is reduced.
[0003] At the same time, the existing B. trispora fermentation of β-carotene is mainly based on single-tank fermentation. In view of its limited natural output and long fermentation cycle, it is necessary to develop a semi-continuous or continuous culture process to further reduce production. cost

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0046] B. trispora positive bacteria and B. trispora negative bacteria were respectively inoculated on the slant surface containing PDA medium, cultured at 28°C for 6 days, then transferred to seed medium, at 28°C, Cultivate for 48 hours under the condition of 220rpm, and feed air at a flow rate of 1.5vvm during the cultivation process.

[0047] The cultured B. trispora positive bacteria and B. trispora negative bacteria were inoculated in the fermenter containing the fermentation medium in a ratio of 1:5 by weight. The biomass dry weight of B. trispora positive bacteria and B. trispora negative bacteria were both 15g / L at the time of inoculation.

[0048] Simultaneously after the inoculation, feed dry compressed air into the fermenter at a flow rate of 1.5vvm, and then ferment at a stirring speed of 200rpm. During the fermentation process, the biomass dry weight of the fermentation system can reach about 45g / L. During the fermentation process, phytic acid was added to contr...

Embodiment 2

[0053] B. trispora positive bacteria and B. trispora negative bacteria were respectively inoculated on the slope containing PDA medium, cultured at 26°C for 8 days, then transferred to seed medium, and grown at 26°C, Cultivate for 52 hours under the condition of 200rpm, and feed air at a flow rate of 1vvm during the cultivation process.

[0054] The cultured B. trispora positive bacteria and B. trispora negative bacteria were inoculated in the fermenter containing the fermentation medium in a weight ratio of 1:3. The biomass dry weight of B. trispora positive bacteria and B. trispora negative bacteria was 12g / L at the time of inoculation.

[0055] Simultaneously after the inoculation, feed dry compressed air into the fermenter at a flow rate of 1vvm, and then ferment at a stirring speed of 180rpm. During the fermentation process, the biomass dry weight of the fermentation system was 40g / L. During the fermentation process, phytic acid was added to control the pH value of the ...

Embodiment 3

[0060] B. trispora positive bacteria and B. trispora negative bacteria were respectively inoculated on the slant surface containing PDA medium, cultured at 30°C for 4 days, then transferred to seed medium, at 30°C, Cultivate for 44 hours under the condition of 240rpm, and feed air at a flow rate of 2vvm during the cultivation process.

[0061] Inoculate the cultured B. trispora positive bacteria and B. trispora negative bacteria into the fermenter containing the fermentation medium at a weight ratio of 1:7. The dry weight of the biomass of the pulley mold negative bacteria was 10g / L.

[0062] Simultaneously after the inoculation, feed dry compressed air into the fermenter at a flow rate of 2vvm, and then ferment at a stirring speed of 220rpm. During the fermentation process, the biomass dry weight of the fermentation system was 50g / L. During the fermentation process, phytic acid was added to control the pH value of the fermentation system to be 6.0.

[0063] When fermenting...

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Abstract

The invention relates to a method for producing β-carotene by B. trispora fermentation and β-carotene, belonging to the field of fermentation engineering. The above method comprises: respectively cultivating B. trispora positive bacteria and B. trispora negative bacteria, simultaneously inoculating, fermenting, and using a regulator to control the pH value of the fermentation system to 5.8-6.2 during the fermentation process, semi-continuous culture, starting at the beginning of fermentation At 60h, feed and feed. Regulator is containing PO 4 3+ And does not contain acidic substances of metal ions and salts. The fermentation medium adopted in the fermentation process contains starch phosphate ester substances. This method is simple and low cost, by using PO 4 3+ And acidic substances without metal ions and salts control the fermentation pH and provide PO 4 3+ , to avoid bringing in excess K + , together with the use of starch phosphates to increase the production of β-carotene. The resulting β-carotene has a relatively high yield and is suitable for industrial production.

Description

technical field [0001] The invention relates to the field of fermentation engineering, and in particular to a method for producing β-carotene by B. trispora fermentation and β-carotene. Background technique [0002] Existing fermentation methods usually use KH 2 PO 4 or K 2 HPO 4 Contain PO 4 3+ salt to increase phosphorylation levels and provide K + , enhance the permeability of cell membrane, and benefit the entry of nutrients into cells. Use KH 2 PO 4 or K 2 HPO 4 Contain PO 4 3+ If the amount of salt is too small, the phosphorylation level will be insufficient, which will greatly reduce the metabolic flux of carotenoids, and if it is too much, it will bring a large amount of K + , so that the cell membrane permeability of the bacteria becomes too strong, and β-carotene is easily transported from the intracellular to the extracellular, so that the accumulation rate of the product is correspondingly slowed down, and the unit production efficiency is reduced. ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C12P23/00C12R1/645
CPCC12P23/00
Inventor 李翔宇汪志明陆姝欢余超刘洋姚建铭
Owner HEFEI INSTITUTES OF PHYSICAL SCIENCE - CHINESE ACAD OF SCI
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