Method for preparing ansamitocin P-3 from precious orange actinosynnema pretiosum
A technology of ansesomycin and actinomycetes, which is applied in the field of biological fermentation, can solve the problems of low proportion of anseomycin P-3, difficulty in large-scale production, inability to synthesize maytansinol and the like, and achieves low cost, The effect of increasing output and saving production costs
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Embodiment 1
[0058] Embodiment 1: 50L tank fed-batch fermentation (during fermentation and cultivation, no hot-pressed bean cake powder was added, and the addition method of isobutanol was fed-batch)
[0059] (1) Spore culture: the spores of Actinomyces fasciculatus orientalis spores frozen in 20% glycerol tubes were cultured by streaking on a solid medium culture dish, and cultured upside down at 28°C for 6 days;
[0060] Solid medium formula: yeast extract 0.3%, soybean peptone 0.5%, malt extract 0.3%, glycerin 1%, agar powder 2%, natural pH;
[0061] (2) Seed culture: Add 6L liquid seed medium to a 10L fermenter, and after sterilizing at 121°C for 30 minutes, scrape the spores from the culture dish and inoculate them into the liquid seed medium; Stir at a speed of 80rpm; during the cultivation process, the dissolved oxygen is kept above 30% by adjusting the ventilation and strengthening the stirring, the maximum ventilation is 1vvm, the maximum rotation speed is 350rpm, and the seed liq...
Embodiment 2
[0067] Embodiment 2: 50L tank fed-batch fermentation (add hot-pressed bean cake powder during fermentation and cultivation, and the supplementary mode of isobutanol is fed-batch)
[0068] (1) Spore culture: as in Example 1;
[0069] (2) seed culture: as embodiment 1;
[0070] (3) Fermentation culture: as in Example 1, the difference is that the liquid fermentation medium is: cornstarch 5%, corn steep liquor dry powder 2%, hot-pressed bean cake powder 2%, glucose 0.5%, K 2 HPO 4 ·3H 2 O 0.025%, MgSO 4 ·7H 2 O 0.3%, CaCO 3 0.4%, CaCl 2 0.1%, isobutanol 0.3%, CoCl 2 ·6H 2 O 0.0005%, FeSO 4 ·7H 2 O 0.0002%, initial pH 7.2;
[0071] For 0-60 hours of fermentation culture, 22.5% glucose solution was added at a flow rate of 0.5mL / L / h. After 60 hours of fermentation, 25% glucose, 10% hot-pressed bean cake powder and 10% glucose solution were added at a rate of 1mL / L / h. % isobutanol feed solution, fermented and cultivated for 412 hours, until the expression of ansamitocin P-3...
Embodiment 3
[0073] Example 3: 50L tank fed-batch fermentation
[0074] (1) Spore culture: as in Example 1;
[0075] (2) seed culture: as embodiment 1;
[0076] (3) Fermentation culture: as in Example 2, the difference is the feeding process, fermentation culture 0-60h, add 22.5% glucose solution with a flow rate of 0.5mL / L / h, after fermentation 60h, add 22.5% glucose solution with 1mL / L Feed solution containing 25% glucose and 10% hot-pressed bean cake powder was added at a rate of / h, and 55mL of isobutanol was added once every 24h; The expression level of is no longer increasing, the fermentation has ended, and the expression level reaches 1211mg / L (such as figure 1 shown);
[0077] (4) Sample processing and detection methods are as in Example 1.
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