Enhancing method of production strength of 2-keto-L-gulonic acid
A technology for producing strength and gulonic acid, applied in the directions of microorganism-based methods, biochemical equipment and methods, microorganisms, etc., can solve problems such as inability to use L-sorbose, and achieve the effect of reducing costs
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Embodiment 1
[0048] at 1 m 3 Carried out in a fermenter, the initial concentration of L-sorbose in the fermentation medium was 16.15 g L -1 , fermented for 6 h, began to feed L-sorbose (i.e. sterile one-step fermentation broth), and controlled the L-sorbose concentration to 15~30 g L during the feeding process -1 After 39 hours of fermentation, the feeding of L-sorbose ended, the dissolved oxygen was controlled at 40% during the fermentation process, and the concentration of 2-KLG at the end of the fermentation was 77.09 g·L -1 , the fermentation period was 51 h, and the acid production rate was 1.51 g·(L·h) -1 ( figure 1 ).
Embodiment 2
[0050] at 1 m 3 Carried out in a fermenter, the initial concentration of L-sorbose in the fermentation medium was 10.15 g L -1 , add 0.21 g·L -1 L-glycine and 0.24 g L -1 L-proline, fermented for 4 h, began to feed L-sorbose (i.e. sterile one-step fermentation broth), and controlled the concentration of L-sorbose to 15-30 g L during the feeding process -1 After 29 hours of fermentation, the feeding of L-sorbose ended, the dissolved oxygen was controlled at 40% during the fermentation process, and the concentration of 2-KLG at the end of the fermentation was 80.29 g·L -1 , the fermentation period was 40 h, and the acid production rate was 2.00 g·(L·h) -1 ( figure 2 ).
Embodiment 3
[0052] at 1 m 3 Carried out in a fermenter, the initial concentration of L-sorbose in the fermentation medium was 10.15 g L -1 , add 0.1 g·L -1 L-glycine and 0.8 g L -1 L-proline, fermented for 4 h, began to feed L-sorbose (i.e. sterile one-step fermentation broth), and controlled the concentration of L-sorbose to 15-30 g L during the feeding process -1 After 29 hours of fermentation, the feeding of L-sorbose ended, the dissolved oxygen was controlled at 40% during the fermentation process, and the concentration of 2-KLG at the end of the fermentation was 78.34 g·L -1 , the fermentation period was 43 h, and the acid production rate was 1.88 g·(L·h) -1 .
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