Novel glutamic acid extracting process
An extraction process, glutamic acid technology, applied in the preparation of organic compounds, methods based on microorganisms, biochemical equipment and methods, etc., can solve the problems of low conversion rate, high consumption of sulfuric acid and liquid ammonia, high cost of culture medium, etc. Achieve the effects of improved strain utilization, low consumption of sulfuric acid, and low cost
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Embodiment 1
[0027] A new glutamic acid extraction process, which comprises the steps of:
[0028] 1) Weigh the raw materials of the fermentation medium: take each raw material according to the weight percentage for later use, including: 7% wheat bran hydrolyzate, 4% glucose, 3% straw treatment, 1% rice bran extract, 0.05% urea, and 0.02% shell powder , magnesium sulfate 0.01%, potassium dihydrogen phosphate 0.01%, and the rest is water;
[0029] 2) Preparation of fermentation medium: Add wheat bran hydrolyzate, glucose, straw treatment, rice bran extract, urea, shell powder, magnesium sulfate and potassium dihydrogen phosphate to water in sequence, stir evenly, and then maintain the Sterilize for 8 minutes, then cool down to 32°C to prepare a fermentation medium;
[0030] 3) Fermentation: Put the temperature-sensitive glutamic acid strain Brevibacterium flavum TMG0106 seed culture solution in the logarithmic growth phase into the fermentation medium at a volume ratio of 10% of the seed c...
Embodiment 2
[0042] Comparative test of process acid production rate and sugar-acid conversion rate of the present invention:
[0043] Control group: fermentation medium used: glucose 5%, yeast extract 6%, peptone 7%, corn steep liquor 1%, magnesium sulfate 1%, urea 0.05%, ferrous sulfate 0.03%, magnesium sulfate 0.02%, potassium dihydrogen phosphate 0.01%, VB1 0.01%, VH 0.01%, and the rest are water; the fermentation process is the same as in Example 1.
[0044] Embodiment 1 of the present invention and control group: the acid production rate and sugar-acid conversion rate of each group are shown in Table 1:
[0045] Table 1
[0046] group
[0047] Conclusion: The amount of acid production and the sugar-acid conversion rate of the Example 1 group of the present invention and the control group are not much different, and the Example group of the present invention is slightly higher; the cost of the culture medium of the Example 1 of the present invention only accounts for the cu...
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