A method for preparing ansamitocin p-3 by using actinomycetes precious orange fasciculatus
A technology of ansamectin and actinomycetes, applied in the field of biological fermentation, can solve the problems of low proportion of ansamectin P-3, inability to synthesize maytansinol, low output of ansamectin, etc. Low cost, saving production cost, high purity effect
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Embodiment 1
[0058] Example 1: 50L tank fed-batch fermentation (the hot-squeezed soybean meal powder was not added during the fermentation culture, and the supplementary method of isobutanol was flow-feeding)
[0059] (1) Spore culture: Streak culture of spores of the precious orange fascicle actinomycete frozen in a 20% glycerol tube in a solid medium petri dish, and inverted culture at 28°C for 6 days;
[0060] Solid medium formula: yeast extract 0.3%, soy peptone 0.5%, malt extract 0.3%, glycerol 1%, agar powder 2%, natural pH;
[0061] (2) Seed culture: Add 6L of liquid seed culture medium to a 10L fermentor, sterilize at 121°C for 30 minutes, scrape the spores from the petri dish and inoculate the liquid seed culture medium; culture at 28°C, with a ventilation volume of 0.4vvm, Stirring at 80 rpm; during the cultivation process, the dissolved oxygen is maintained above 30% by adjusting the aeration rate and enhanced stirring, the maximum aeration rate is 1 vvm, the maximum rotation speed is ...
Embodiment 2
[0067] Example 2: 50L tank fed-batch fermentation (add hot-squeezed soybean meal powder during fermentation culture, and the supplementary method of isobutanol is fed-batch)
[0068] (1) Spore culture: as in Example 1;
[0069] (2) Seed cultivation: as in Example 1;
[0070] (3) Fermentation culture: as in Example 1, the difference is that the liquid fermentation medium is: corn starch 5%, corn syrup dry powder 2%, hot pressed soybean meal 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] Fermentation culture 0-60h, supplemented with 22.5% glucose solution at a flow rate of 0.5mL / L / h, after 60h fermentation, supplemented with 25% glucose, 10% hot-pressed soybean meal and 10% glucose at a rate of 1mL / L / h % Isobutanol feed liquid, fermented for 412 hours, until the expression level of ansamcin P-3 no longer increased, the fermentation has ended, the expressi...
Embodiment 3
[0073] Example 3: 50L tank fed-batch fermentation
[0074] (1) Spore culture: as in Example 1;
[0075] (2) Seed cultivation: as in Example 1;
[0076] (3) Fermentation culture: as in Example 2, the difference is the feeding process. Fermentation culture is 0-60h, and 22.5% glucose solution is added at a flow rate of 0.5mL / L / h. After 60h of fermentation, 1mL / L Supplement with a feed liquid containing 25% glucose and 10% hot-pressed soybean meal at a rate of 1 / h. Isobutanol supplementation adopts a one-time addition of 55mL every 24h; fermentation culture is to 408h, to ansamicin P-3 The expression level no longer increases, the fermentation has ended, the expression level reached 1211mg / L (such as figure 1 Shown);
[0077] (4) The sample processing and detection methods are as in Example 1.
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