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Culture mediums for producing doramectin through fermentation of mutant streptomyces avermitilis and material supplement method

A Streptomyces avermitilis, fermentation medium technology, applied in the field of fermentation, can solve the problems of affecting the quality of fermentation broth and fermentation effect, high production cost of doramectin, affecting the quality of fermentation broth, etc., to improve the quality and fermentation technology level , Improve the level of fermentation technology, the effect of low market price

Active Publication Date: 2015-04-29
宁夏泰瑞制药股份有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] 1 The fermentation production process has not changed much, and the fermentation technology level is maintained at 1000-1200u / ml, resulting in a low overall fermentation yield
[0005] 2 The quality of animal nitrogen source affects the quality and fermentation effect of fermentation broth
At present, peptone or yeast extract is added to the medium for domestic fermentation production of doramectin, or two or more nitrogen sources are selected to be added at the same time, resulting in more residual protein in the late stage of fermentation and higher viscosity of the fermentation broth, which reduces the extraction yield. Rate
[0006] 3 The available carbon source in the conventional medium is glucose, and part of the glucose is carbonized during the sterilization process of the medium, which affects the quality of the fermentation broth
[0007] 4. The production cost of doramectin is relatively high, and the cost of nitrogen source accounts for about 30% of the fermentation cost

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0055] 1m 3 seed pot culture

[0056]10L of maltose, 30kg of mixed starch, 5L of rapeseed oil, 20kg of low-temperature pressed soybean cake powder, 15kg of corn distiller's grains, 15kg of corn gluten powder, 1kg of light calcium carbonate, 1kg of ammonium sulfate, and 0.01kg of maltase.

[0057] During the seed cultivation process, the tank pressure is 0.02-0.04MPa; the tank temperature is 27-29°C; the air flow rate is 60m 3 / h; stirring speed 60~80r / min; pH6~8; culture time 40h. After the seed culture is over, the cell concentration is 25%, and there is no other miscellaneous bacteria pollution.

[0058] 10m 3 fermenter culture

[0059] 300L of maltose, 300kg of mixed starch, 100L of rapeseed oil, 300kg of low-temperature pressed soybean cake powder, 200kg of corn distiller's grains, 200kg of corn gluten powder, 8kg of potassium dihydrogen phosphate, 50kg of light calcium carbonate, 30kg of ammonium sulfate, 5kg of sodium cyclohexyl formate, Magnesium sulfate 2kg, zinc ...

Embodiment 2

[0063] 1m 3 seed pot culture

[0064] 12L of maltose, 32kg of mixed starch, 6L of rapeseed oil, 22kg of low-temperature pressed soybean cake powder, 18kg of corn distiller's grains, 17kg of corn gluten powder, 2kg of light calcium carbonate, 2kg of ammonium sulfate, and 0.02kg of maltase.

[0065] During the seed cultivation process, the tank pressure is 0.02-0.04MPa; the tank temperature is 27-29°C; the air flow rate is 60m 3 / h; stirring speed 60~80r / min; pH6~8; culture time 41h. After the seed culture is over, the cell concentration is 26%, and there is no other miscellaneous bacteria pollution.

[0066] 10m 3 fermenter culture

[0067] 320L of maltose, 350kg of mixed starch, 110L of rapeseed oil, 320kg of low-temperature pressed soybean cake powder, 220kg of corn distiller's grains, 230kg of corn gluten powder, 9kg of potassium dihydrogen phosphate, 60kg of light calcium carbonate, 40kg of ammonium sulfate, 8kg of sodium cyclohexyl formate, Magnesium sulfate 3kg, zinc...

Embodiment 3

[0071] 1m 3 seed pot culture

[0072] 15L of maltose, 35kg of mixed starch, 7L of rapeseed oil, 25kg of low-temperature pressed soybean cake powder, 20kg of corn distiller's grains, 18kg of corn gluten powder, 3kg of light calcium carbonate, 3kg of ammonium sulfate, and 0.03kg of maltase.

[0073] During the seed cultivation process, the tank pressure is 0.02-0.04MPa; the tank temperature is 27-29°C; the air flow rate is 60m 3 / h; stirring speed 60~80r / min; pH6~8; culture time 43h. After the seed culture is over, the cell concentration is 27%, and there is no other miscellaneous bacteria pollution.

[0074] 10m 3 fermenter culture

[0075] 350L of maltose, 400kg of mixed starch, 120L of rapeseed oil, 350kg of low-temperature pressed soybean cake powder, 250kg of corn distiller’s grains, 250kg of corn gluten powder, 10kg of potassium dihydrogen phosphate, 65kg of light calcium carbonate, 50kg of ammonium sulfate, 10kg of sodium cyclohexyl carboxylate, Magnesium sulfate 4kg...

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PUM

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Abstract

The invention relates to culture mediums for producing doramectin through fermentation of mutant streptomyces avermitilis and a material supplement method. The culture mediums comprise a seed culture medium and a fermentation culture medium, and are characterized in that the seed culture medium comprises corn lees and low-temperature pressing soya bean cake powder; the fermentation culture medium comprises corn lees, low-temperature pressing soya bean cake powder, polystyrene non-polar adsorbent resins and nonionic surfactants. The cost problem of raw materials and auxiliary materials are solved, the environment influence on sources of the raw materials and the auxiliary materials is reduced to the hilt, the supplying of the raw materials and the auxiliary materials is sufficient, the stable and efficient production of the doramectin is realized, and at the same time, the fermentation unit can be improved by using the culture mediums and the material supplement method.

Description

technical field [0001] The invention belongs to the field of fermentation technology, and in particular relates to a culture medium and feeding method for doramectin fermented by mutant Streptomyces avermitilis. Background technique [0002] Doramectin is a new type of macrolide antiparasitic drug, which is biosynthesized by mutant Streptomyces avermitilis in a fermentation mode. In comparison, its anti-parasitic range is wider, its insecticidal activity is higher, and its effective time for preventing parasitic re-infection is longer. It is considered to be the most promising new veterinary anti-parasitic drug. [0003] At present, the domestic use of mutant Streptomyces avermitilis to produce doramectin by fermentation, the main problems are: [0004] 1 The fermentation production process has not changed much, and the fermentation technology level is maintained at 1000-1200u / ml, resulting in a low overall fermentation yield. [0005] 2 The quality of animal nitrogen sour...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C12P17/18C12R1/465
Inventor 任勇
Owner 宁夏泰瑞制药股份有限公司
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