Preparation technology for 2-keto -L-gulonic acid ferment strain
A technology of keto-based cologne and fermentation strains, applied in the direction of fermentation, microbial-based methods, bacteria, etc., can solve the problems of long fermentation period, low strain density, increased energy consumption and cost, etc., and shorten fermentation cycle, increase the activity of the strain, and increase the effect of the density of the strain
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Embodiment 1
[0007] First inoculate the small bacteria individually on the slant medium and cultivate them for 24 hours, then inoculate the large bacteria, and continue to cultivate for 28 hours. L fructose was used as the main carbon source, and the number of bacteria in the inoculum solution was 5.5×10 8 Individuals / ml, inoculated to 1m by expanding culture 3 In the fermenter, the fermentation ended for 46 hours, the 2-keto-L-gulonic acid content at the end point of the fermentation broth was 101.63mg / ml, and the fermentation conversion rate was 92.56%.
Embodiment 2
[0009] First inoculate the small bacteria separately on the slant medium and cultivate them for 20 hours, then inoculate the large bacteria, and continue to cultivate for 32 hours. L sucrose was used as the main carbon source, and the number of bacteria in the inoculum solution was 1.9×10 9 Individuals / ml, inoculated to 50m by expanding culture 3 In the fermenter, the fermentation ended for 45 hours, the 2-keto-L-gulonic acid content at the end point of the fermentation liquid was 104.86mg / ml, and the fermentation conversion rate was 92.91%.
Embodiment 3
[0011] First inoculate the small bacteria separately on the slant medium and cultivate them for 32 hours, then inoculate the large bacteria and continue to cultivate for 34 hours. L of sucrose was used as the main carbon source, and the number of bacteria in the inoculum solution was 8.3×10 9 Individuals / ml, inoculated to 100m by expanding culture 3 In the fermenter, the fermentation ended for 41 hours, the 2-keto-L-gulonic acid content at the end point of the fermentation broth was 104.81mg / ml, and the fermentation conversion rate was 92.81%.
[0012] The average fermentation period of this technology is shortened by 15%, the fermentation conversion rate is increased by 2 percentage points, the utilization rate of equipment is greatly improved, and the cost is also greatly reduced.
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