Strain HD924 for producing dihydroxyacetone by microbial fermentation and method
A kind of technology of dihydroxyacetone and HD924, applied in the field of fermenting glycerol to produce dihydroxyacetone
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Embodiment 1
[0039] The method for producing dihydroxyacetone by fermenting glycerol with the bacterial strain HD924 is specifically as follows: the bacterial strain HD924 is first inoculated into a primary seed medium with a 10% inoculum size (the composition of the primary seed medium is: glycerol 30g / L, yeast powder 15g / L, KH 2 PO 4 0.3g / L, pH natural), cultured aerobically at 28°C for 24h; then the cultured primary seeds were inserted into the secondary seed medium at an inoculum size of 5% (the composition of the secondary seed medium was : Glycerin 30g / L, yeast powder 15g / L, CaCO 3 0.3g / L, pH 6.0), after 8 hours, put the cultured secondary seeds into the fermentation medium containing different glycerin concentrations (250mL triangular flask, liquid volume 50mL) at 200 rpm / min, fermented at 28°C for 48 h, and measured the content of dihydroxyacetone. The experimental results are shown in Table 4.
[0040] Wherein, the composition of the fermentation medium is: glycerol 50~350g...
Embodiment 2
[0043] Put the cultured secondary seeds into 5% inoculum of glycerol (glycerin comes from food grade glycerol, industrial grade glycerol and saponified crude glycerol respectively) into the fermentation medium with a concentration of 100g / L (250mL Erlenmeyer flask, filled with liquid volume 50mL) at 200 rpm, fermented at 28°C for 72 hours, and measured the content of dihydroxyacetone. The experimental results are shown in Table 5. Wherein, the fermentation medium consists of: glycerol 100g / L, yeast powder 10g / L, CaCO 3 3g / L, pH 6.0; the purity of food grade glycerin is 99.5%, the purity of industrial grade glycerin is 95%, and the saponified crude glycerin is waste glycerin from soap making industry (purity 60%). One, the cultivation of secondary seed is identical with embodiment 1.
[0044]
Embodiment 3
[0046] Utilize the method for producing dihydroxyacetone by fermenting glycerol with the bacterial strain HD924, specifically: the bacterial strain HD924 is directly inserted into the fermentation medium (250mL triangular flask, liquid capacity 50mL; the fermentation medium consists of: Food grade glycerol 100g / L, peptone 8g / L, calcium carbonate 5g / L, culture medium pH 7), rotating speed 200 rpm, fermented at 30°C for 72 h under aerobic conditions; The content of hydroxyacetone was 67.4 g / L.
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