A kind of fermentation and separation and purification method of L-leucine
A technology for separation and purification and leucine, which is applied in the field of fermentation and separation and purification of L-leucine, can solve the problems of long operation cycle, large salt consumption, long time consumption, etc., and can reduce the generation of by-products and improve the sugar content. Acid conversion rate, simple and easy-to-control process
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Embodiment 1
[0037] Embodiment 1: A kind of method of fermentation and separation and purification of L-leucine
[0038] The method for fermentation and separation and purification of L-leucine in the present invention comprises the following steps:
[0039] (1) Activation culture: Corynebacterium glutamicum and Brevibacterium ammoniagenes were respectively inoculated on the activation medium, activated and cultured in an incubator at 28°C for 12 hours to obtain activated bacteria;
[0040] The activation medium includes: anhydrous glucose 1g / L, peptone 10g / L, beef extract 10g / L, yeast extract 5g / L, NaCl 2.5g / L, agar powder 20g / L, pH=6.8-7.0.
[0041] (2) Seed culture: Take a ring of well-grown activated Corynebacterium corynebacterium ATCC21885 and Brevibacterium ammoniagenes BNCC183441, and inoculate them into shake flasks containing seed medium 1 and 2, respectively, with a liquid volume of 200mL / 500mL , the condition of seed culture is 28℃, 200r / min shaker culture for 20h, until the c...
Embodiment 2
[0050] Embodiment 2: A kind of method of fermentation and separation and purification of L-leucine
[0051] The only difference from Example 1 is that the ratio of the seed liquid of Corynebacterium glutamicum and Brevibacterium ammoniagenes inoculated in the fermentation culture in step (3) is 8:2.
Embodiment 3
[0052] Embodiment 3: A kind of method of fermentation and separation and purification of L-leucine
[0053] The only difference from Example 1 is that the ratio of the seed liquid of Corynebacterium glutamicum and Brevibacterium ammoniagenes inoculated in the fermentation culture in step (3) is 8:3.
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