High-yield AD/ADD strain and method for high-efficient production of AD/ADD
A technology of strains and microorganisms, applied in the direction of microorganism-based methods, biochemical equipment and methods, bacteria, etc., can solve the problem of low single substrate feeding amount of AD and/or ADD, and achieve the effect of increasing the quantity
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Embodiment 1
[0030] Embodiment 1 Activation and Proliferation Culture of Bacterial Strains
[0031] Prepare activated slant medium (g / L): glucose 20, peptone 10, yeast powder 5, beef extract 5, potassium dihydrogen phosphate 1, ammonium nitrate 1, magnesium sulfate 0.5, agar 20, control pH 7.0. And the culture medium was sterilized at 121°C, 0.1Mpa, and steam for 20min. After sterilization, the culture medium is divided into 250ml eggplant-shaped bottles, and the filling volume of each bottle is 50ml.
[0032] The preserved strain Mycobacterium.sp-BK-1 (preservation number CGMCC No.5707) was taken out from the -80°C refrigerator, inoculated aseptically on the above slant medium, and cultured at 30°C for 5 days.
[0033] Prepare the shake flask seed medium (g / L): glucose 20, peptone 5, yeast powder 2.5, magnesium sulfate 0.5, control pH 7.0, 121°C, 0.1Mpa, steam sterilization for 20min. The seed medium is divided into 500ml Erlenmeyer flasks, and the volume of each bottle is 100ml.
[00...
Embodiment 2
[0035] Example 2 Production of AD and / or ADD by fermentation
[0036] Preparation of fermenter medium (g / L): Potassium dihydrogen phosphate 1, disodium hydrogen phosphate 0.5, refined molasses 60, magnesium sulfate 0.3, ammonium nitrate 3, sterol 25, soybean oil 147 (the average density of soybean oil is 0.92g / ml , about 0.159L, accounting for about 16% of the volume ratio of the fermentation broth), control pH 6.8, prepare a fermenter with a volume of 7.5L, a liquid volume of 4L, sterilize at 121°C, 0.1Mpa, and steam for 20 minutes, and set aside.
[0037] According to the inoculum size of 10%, the culture obtained in the seed shake flask in Example 1 was transferred into a fermenter for biotransformation at 31° C., the stirring speed was 350 rpm, the ventilation flow rate was 1.0 L / L / min, and the fermentation time was cultivated for 168 hours.
[0038] When the fermentor was inoculated, the pH was controlled to be 6.5, and then the pH changed automatically. When the fermenta...
Embodiment 3
[0040] The fermentation medium and operation steps selected in this example are the same as in Example 2, the difference is that the pH is controlled at 7.0 during inoculation, adjusted to pH 7.5 in 24 hours, 8.0 in 48 hours, and above 8.5 after 72 hours. At the end of the fermentation, the pH of the fermentation broth was detected to be 9.1; the detected sterol residue was 7.2%, and the conversion rate was 68.0%; the total amount of AD and / or ADD was 10.41g / L, wherein AD:ADD=96:4.
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