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D-ribose fermentation process regulating method

A fermentation process and ribose technology, which is applied in the field of regulation of D-ribose fermentation process, can solve problems such as optimized control methods that have not yet emerged, and achieve the effects of shortened fermentation cycle, easy control, and enhanced repeatability

Inactive Publication Date: 2005-12-14
CHENGZHI LIFE SCI CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, there is no mature method for the optimal control of the D-ribose fermentation process of these strains.

Method used

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  • D-ribose fermentation process regulating method

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Experimental program
Comparison scheme
Effect test

Embodiment 1

[0067] Bacillus pumilus (B. pumilus) CGMCC 0845 was used. In 350L seed medium (pH 7.0) consisting of 2.0% sorbitol (w / w), 2.0% corn steep liquor, 0.1% yeast extract, 0.3% dipotassium hydrogen phosphate, 0.1% potassium dihydrogen phosphate, and 0.05% magnesium sulfate Medium, control the pressure of the seed tank to 1.0kg / cm 2 , Rotation speed 200 rpm, culture temperature 36 ℃, after 16 hours of culture, access is made of glucose 16.0% (w / w), corn steep liquor 2.6%, yeast extract 0.1%, ammonium sulfate 0.7%, manganese sulfate 0.005%, calcium carbonate In a 2.2% fermentation medium (pH 7.0) of 3200L, the stirring speed was controlled to be 180 rpm and the culture temperature was 36°C. In the early period of fermentation, it is controlled at pH 6.5-7.0 and dissolved oxygen 20-25% for 0-18 hours; in the middle and late fermentation period, it is controlled at pH 6.3-6.5 and dissolved oxygen 25-30%. 18 hours before fermentation, glucose consumption is slow, mainly in the growth stage o...

Embodiment 2

[0073] B. subtilis (B. subtilis) CGMCC 0846 was used. In 350L seed culture medium composed of glucose 2.0% (w / w), yeast extract 0.3%, corn steep liquor 0.05%, dipotassium hydrogen phosphate 0.3%, potassium dihydrogen phosphate 0.1%, magnesium sulfate 0.05% (pH 7.0) , Control the pressure of seed tank 1.0kg / cm 2 , Rotation speed 200 rpm, culture temperature 36 ℃, after 18 hours of culture, connect with glucose 16.0% (w / w), corn steep liquor 2.6%, ammonium sulfate 0.7%, manganese sulfate 0.005%, calcium carbonate 2.2% 3200L fermentation medium (pH 7.0). Control the stirring speed at 180 rpm, and the culture temperature at 36°C. In the early period of fermentation, 0-18 hours, control at pH 6.5-7.0, dissolved oxygen 18-22%; in the middle and late fermentation period, control at pH 6.0-6.2, dissolved oxygen 20-25%; at 36℃, 0.60kg / m 2Cultivation under aeration and stirring. 18 hours before fermentation, glucose consumption is slow, mainly in the growth stage of bacteria. After 18 hours...

Embodiment 3

[0079] Bacillus pumilus ATCC 31093 was used. In 350L seed culture medium composed of sorbitol 2.0%, corn steep liquor 2.0%, dipotassium hydrogen phosphate 0.3%, potassium dihydrogen phosphate 0.1%, tyrosine and phenylalanine each 100μg / ml (pH 7.0), Control seed tank pressure 1.0kg / cm 2 , Rotation speed 200 rpm, culture temperature 36 ℃, after 16 hours of culture, access is made of glucose 16.0% (w / w), dry yeast 1.2%, ammonium sulfate 0.6%, manganese sulfate 0.005%, calcium carbonate 2.2%, tryptophan Acid, tyrosine and phenylalanine prepared 50μg / ml 3200L fermentation medium (pH 7.0), using the same fermentation control conditions as in Example 1, after 33 hours of fermentation culture, the glucose in the fermentation broth decreased 2.5-3.0%, control the sugar concentration in the fermentation broth to be within the range of 2.5-3.0%, and start to feed sugar at a flow rate of 120 liters / hour, the sugar concentration of the feed is 40%, and the volume is 550L. After 48 hours of fer...

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Abstract

The invention relates to a method for regulating and optimizing the D-ribose fermentation process. This method is a fermentation control method that focuses on controlling dissolved oxygen and pH value, controlling key variables such as bacterial growth, substrate consumption rate, and product production rate, and adding sugar in a timely manner. In 5000L The results of the fermentation tank fermentation show that by applying this method, the sugar production level of D-ribose can be increased by 20 to 34%, the fermentation cycle is shortened to 42 to 50 hours, the filling coefficient of the fermentation tank is increased from 70% to more than 80%, and the fermentation process is easy to Control and repeatability are enhanced.

Description

(1) Technical field [0001] The invention relates to a method for regulating the D-ribose fermentation process. (2) Background technology [0002] The preparation methods of D-ribose include extraction and separation from natural substances, chemical synthesis, and microbial fermentation. To extract and isolate D-ribose from natural products, the extraction process is complicated and the manufacturing cost is high, so it is not suitable for large-scale production. As far as synthetic methods are concerned, people have tried to synthesize D-arabinose (Gehrke and Aichner, 1927), D-gluconic acid (Steiger, 1936), D-glucose (Korczynski A et al. 1979), L-glutamic acid and D-xylose (Lacourt Gadras, et al. 1992) to synthesize D-ribose. Before the 1980s, the industrial production of D-ribose was mainly carried out by chemical synthesis of glucose at home and abroad, that is, oxidation and replacement of glucose D-ribose is prepared through a seven-step reaction of conversion, replac...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C12P19/02
Inventor 高润香李文濂梁是森王威
Owner CHENGZHI LIFE SCI CO LTD