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2-keto-l-gulonic acid high concentration fermentation production technology

A production process, the technology of gulonic acid, applied in the direction of fermentation, microorganism-based methods, microorganisms, etc., can solve the problems of low product concentration, inability to give full play to the production capacity of strains and equipment, and achieve good stability and unchanged strains , Ease of wide application

Inactive Publication Date: 2009-03-25
DSM JIANGSHAN PHARMACEUTICAL (JIANGSU) CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The product concentration of this method is low, and the production capacity of the bacteria and equipment cannot be fully utilized.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0010] 300m 3 Fermentation tank with a fermentation volume of 263m 3 , the initial concentration of sorbose in the fermentation medium is 22mg / ml, ferment for 4 hours, start to add sorbose, and finish adding sorbose after 36 hours of fermentation, control the concentration of sorbose to 25mg / ml during the process of feeding, and adjust the pH to 7.1 after 26 hours of fermentation , ferment for 40 hours to adjust the pH to 7.4 until the end of the fermentation, and control the dissolved oxygen concentration to 35% during the fermentation process. The content of gulong acid at the end point of the fermentation broth was 109 mg / ml, and the conversion rate of alcohol and acid was 92.86%.

Embodiment 2

[0012] 180m 3 Fermentation tank with a fermentation volume of 150m 3 , the initial concentration of sorbose in the fermentation medium was 20mg / ml, after 7 hours of fermentation, the feeding of sorbose was started, and the feeding of sorbose was completed after 40 hours of fermentation. Ferment for 40 hours and adjust the pH to 7.4 until the end of the fermentation, and control the dissolved oxygen concentration to 40% during the fermentation. The content of gulonic acid at the end point of the fermentation broth was 105.64 mg / ml, and the conversion rate of alcohol and acid was 92.63%.

Embodiment 3

[0014] 180m 3 Fermentation tank with a fermentation volume of 155m 3 The fermentation medium initially contained 18mg / ml of sorbose, fermented for 6 hours, started feeding sorbose, and finished feeding sorbose after 40 hours of fermentation, controlled the concentration of sorbose in the feeding process to 18mg / ml, adjusted the pH to 7.2 after 32 hours of fermentation, Adjust the pH to 7.4 for 44 hours until the end of the fermentation, and control the dissolved oxygen concentration to 45% during the fermentation process. The content of gulong acid at the end point of the fermentation broth was 108 mg / ml, and the conversion rate of alcohol and acid was 92.69%.

[0015] Compared with the existing process, the fermentation output of the present invention is increased by 10%, the fermentation yield is increased by 3%, the equipment utilization rate is greatly improved, and the energy consumption and material consumption are also greatly reduced.

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PUM

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Abstract

The invention discloses a production technique of 2-keto-L-gulonic acid by high concentration fermentation. In a fermentation medium adopted by the production technique, the initial sorbin concentration is 15mg / ml to 25mg / ml; fermentation is carried out for 4 hours to 8 hours; continuous sorbin feeding is started; fermentation is carried out for 36 hours to 44 hours and then sorbin feeding is finished; during the feeding process, the content of sorbin is controlled to be 15 mg / ml to 30 mg / ml; when fermentation is carried out for 24 hours to 40 hours, pH value is adjusted to be 7.1 to 7.3; when fermentation is carried out for 40 hours to 44 hours, pH value is adjusted to be 7.4 to 7.6 until fermentation is finished; and dissolved oxygen during the whole fermentation process is controlled to be 30 percent to 50 percent. The technique adopted by the invention has total fed sorbin with a concentration of 10.5 percent to 11.5 percent (W / V) at the end of fermentation; the concentration of gulonic acid of fermentation solution is raised by 10 percent to 15 percent; the conversion rates of alcohol and acid are respectively promoted by 3 percentage points; and stability is good; besides, the technique process has simple and convenient operation and is easy for wide application.

Description

technical field [0001] The invention relates to a preparation method of vitamin C, in particular to a high-concentration fermentation production process of 2-keto-L-gulonic acid. Background technique [0002] At present, many domestic manufacturers mainly use two-step fermentation technology for vitamin C production. The main feature of this technology is that the fermentation process is completed in two steps. The first step is to use black vinegar bacteria to convert D-sorbitol into L-sorbose, and the second step is to convert sorbose from sorbose under the action of a mixed strain For 2-keto-L-gulonic acid (vitamin C precursor). This mixed strain is composed of two kinds of microorganisms, among which the microorganism responsible for sugar-acid conversion was originally named Gluconobacter oxidans, and its taxonomic position was re-determined after systematic identification recently, and the bacteria was renamed as common ketogenic group Guronic acid bacteria; the othe...

Claims

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Application Information

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IPC IPC(8): C12P7/60C12P39/00C12R1/01C12R1/11
Inventor 陈红黄建明袁训朱涛吴新莉
Owner DSM JIANGSHAN PHARMACEUTICAL (JIANGSU) CO LTD
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