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
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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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