Microorganism producing L-lysine and processes for producing L-lysine usi ng the same
A technology of lysine and Corynebacterium glutamicum, which is applied in the field of L-lysine-producing microorganisms and its production of L-lysine, and can solve the problems of no reported resistance to the antibiotic monensin
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Embodiment 1
[0019] Corynebacterium glutamicum CH77 and CJM107 were inoculated in a 250 ml elbow baffled bottle containing 25 ml of the following seed medium, and cultured at 30° C. for 20 hours with shaking (220 rpm). Inoculate 1 ml of seed medium into a 250 ml elbowed bottle with baffles containing less than 25 ml of production medium, and culture at 32° C. with shaking (220 rpm) for 96 hours. After the cultivation was completed, the amount of L-lysine was measured by HPLC. The L-lysine present as L-lysine hydrochloride in the culture solutions of Corynebacterium glutamicum CH77 and CJM107 were 47 g / l and 51 g / l, respectively. Seed medium (pH7.0)
[0020] Raw sugar 50g, peptone 10g, yeast extract 10g, urea 5g, KH 2 PO 4 4g, K 2 HPO 4 8g, MgSO 4 ·7H 2 O0.5g, biotin 100 μ g and thiamine hydrochloride 1000 μ g (per 1 liter of industrial water) production medium (pH7.0)
[0021] Molasses or pre-treated molasses (with reducing sugar) 50g, raw sugar 50g, yeast extract 4g, (NH 4 ) 2 S...
Embodiment 2
[0023] The CJM107 strain was grown in a medium containing molasses and raw sugar. After culturing, sulfuric acid or hydrochloric acid was added to 1 liter of L-lysine fermentation broth to adjust the pH to 2.0, thereby reducing the Ca 2+ converted to CaSO 4 or CaCl 2 . Next, the broth was applied to allow countercurrent adsorption to cation exchange resins (Dianion SK-1B, SK-1BL), which were regenerated in the form of ammonium ions. Subsequently, it was washed with desalted water to remove cell aggregates remaining in the resin layer, and then a concentrated fraction of L-lysine was recovered therefrom by elution with 2N ammonium hydroxide. After concentrating the recovered fraction, the concentrate was adjusted to pH 5.0 and cooled to 20° C., thereby forming L-lysine crystals.
[0024] The slurry obtained after complete crystallization was centrifuged to obtain a first wet product. The mother liquor was again concentrated and crystallized by batch method to obtain a seco...
Embodiment 3
[0025] The CJM107 strain was grown in a medium containing pretreated molasses and raw sugar. After cultivation, sulfuric acid was added to 1 liter of L-lysine fermentation broth to adjust the pH to 2.0, thereby reducing the Ca 2+ converted to CaSO 4 . Next, the broth was applied to allow countercurrent adsorption to cation exchange resins (Dianion SK-1B, SK-1BL), which were regenerated in the form of ammonium ions. Subsequently, it was washed with desalted water to remove cell aggregates remaining in the resin layer, and then a concentrated fraction of L-lysine was recovered therefrom by elution with 2 N ammonium hydroxide. After concentrating the recovered fraction, the concentrate was adjusted to pH 5.0 and cooled to 20° C., thereby forming L-lysine crystals.
[0026] The slurry obtained after complete crystallization was centrifuged to obtain a first wet product. The mother liquor was again concentrated and crystallized by batch method to obtain a second wet product. T...
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