Method for producing 9-alpha-hydroxyandrostenedione by microbial fermentation
A technology for hydroxyandrostenedione and microbial fermentation, applied in the direction of microorganism-based methods, biochemical equipment and methods, microorganisms, etc., can solve problems such as pollution and unsuitability for industrial production of 9α-OHAD, and achieve simple extraction and high yield High, low environmental pressure effect
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Embodiment 1
[0037] Strain propagation: ZS3-9α was prepared into a bacterial concentration of 10 7 -10 9 Bacterial suspension of individual / ml, insert in the seed tank of seed culture medium with 5%-10% inoculum size afterwards and cultivate, and seed culture medium comprises: glucose 8g / L, MgSO 4 ·7H 2 O 0.8g / L, (NH 4 ) 2 Fe(SO 4 ) 2 ·6H 2 O 0.02g / L, CaCO 3 5.5g / L and citric acid 1.0g / L, the pH of the seed medium is 7.0;
[0038] Fermentation transformation: OD of seed liquid in the seed tank 600 When it is 15-20, insert it into the transformation medium with 20% inoculum size for cultivation, and the fermentation medium includes: glucose 30g / L, peptone 15g / L, bean cake powder 25g / L, MgSO 4 ·7H 2 O 0.5g / L, (NH 4 ) 2 Fe(SO 4 )2·6H 2 O 0.06g / L, CaCO 3 4.5g / L, 3.0g / L citric acid, pH of the fermentation medium is 7.0; wherein, the substrate phytosterol is added to the prepared basic fermentation medium with a mass fraction of 2.0%. The transformation culture conditions are as ...
Embodiment 2
[0042] In Example 1, the inoculum amount of strains during fermentation transformation was changed to 30%, and the transformation culture conditions were changed to: temperature 32°C, tank pressure 0.05MPa, stirring 150-200rpm, dissolved oxygen 30%, cycle 100h.
[0043] The test result is: the final conversion rate of 9α-OH AD is 93.2%.
Embodiment 3
[0045] Change the inoculum amount of the bacterial classification to 50% during fermentation transformation in Example 1, change the mass fraction of phytosterols to 3.0%, and change the transformation culture conditions to: temperature 32°C, tank pressure 0.05MPa, stirring 150-200rpm, cycle 120h .
[0046] The test result is: the final conversion rate of 9α-OH AD is 95.8%.
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