FIELD: biotechnology.
SUBSTANCE: basic fermentation medium is prepared on the basis of fermentative lysate of starch in an amount of 8-15% for glucose, and additional fermentation medium containing the components of basic fermentation medium, 2-3.5 times concentrated. They are sterilised. Biosynthesis of L-lysine is carried out using strain-producer Corynebacterium glutamicum of All-Russia classification of microorganisms Ac-2577D (BIGOR 55). The fermentor is loaded with the basic nutrient medium in amount of 1/3 of its volume. Then inoculation of the basic fermentation nutrient medium is carried out with 10-20% inoculum grown in two stages. Biosynthesis process is carried out with continuous feeding starting from 8-16 hours of cultivation. At that the inhibitory concentration of reducing substances in the culture fluid of 4-8% is maintained. After filling the device to the maximum volume after 60-66 hours of cultivation and then every 6-12 hours for the rest part of biosynthesis process a part of the culture fluid in amount of 10-15% of the maximum volume is pumped into the device for final fermentation. In this device, the biosynthesis process is continued for 6-12 hours under the same conditions as in the main device but without feeding the additional nutrient medium. Then L-lysine is isolated.
EFFECT: invention enables to carry out the biosynthesis process for a long time without reducing the rate of synthesis of L-lysine, and provides obtaining of the culture fluid with high concentration of L-lysine prior to the isolation.
4 ex
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Authors
Dates
2013-06-27—Published
2011-06-29—Filed