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Fermentation production method for xylitol

A production method and technology of xylitol, which is applied in the field of xylitol fermentation and production, can solve the problems of interfering with the separation and purification of xylitol, difficulty in fine-tuning dissolved oxygen, and low industrial value, so as to increase the reproduction speed, shorten the fermentation time, The effect of reducing the fermentation time

Inactive Publication Date: 2013-07-03
HEFEI UNIV OF TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The dissolved oxygen level in the fermentation process directly regulates the production rate of xylitol. Since microbial aerobic fermentation technology must be adopted, it is difficult to meet the requirements of this process in industrial production. In actual industrial production, it affects the dissolved oxygen in the fermentation broth. There are many factors, especially under low dissolved oxygen conditions, it is difficult to fine-tune dissolved oxygen through aeration, and the oxygen level in the fermentation liquid cannot be accurately controlled; Xylitol dehydrogenase gene, thereby inhibiting the conversion of xylitol to xylulose, but in the reaction process, a large amount of relatively expensive glycerol needs to be added as a substrate to maintain the normal growth and metabolic activities of cells, and the residual glycerol is serious Interfering with the subsequent separation and purification of xylitol, the industrial value is not high
At present, the highest yield of xylose into xylitol is 70%~80%, and there is no economical and mature method for the optimal control of strains, which affects the economical and large-scale production of xylitol

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0021] Pachysomyces tannophilus ( Pachysolen tannophilus ) into the fermentation medium, the amount of access was 8%, the fermentation time was 36 hours, the culture temperature was 29°C, and the tank pressure was 0.6 kg / cm 2 , the stirring speed is 300 rpm, and the pH is pH5;

[0022] The early stage of fermentation is the natural redox potential, the ventilation rate in the early stage of fermentation is 3 liters per minute, and the fermentation time in the early stage of fermentation is 24 hours; Milliliters / minute feed glucose solution to realize, the concentration of the solution that feeds glucose is 40%, and the aeration rate in the middle and late period of fermentation is 0.1 liter / minute;

[0023] The raw materials and weight of the fermentation medium: glucose 50 g / liter, xylose 100 g / liter, yeast extract 15 g / liter, potassium dihydrogen phosphate 4 g / liter, magnesium sulfate 0.1 g / liter.

Embodiment 2

[0025] Pachysomyces tannophilus ( Pachysolen tannophilus ) into the fermentation medium, the amount of access is 6%, the fermentation time is 36 hours, the culture temperature is 30°C, and the tank pressure is 0.6 kg / cm 2 , the stirring speed is 280 rpm, and the pH is pH5;

[0026] The early stage of fermentation is a natural oxidation-reduction potential, the ventilation rate in the early stage of fermentation is 3~3.5 liters per minute, and the fermentation time in the early stage of fermentation is 24 hours; Realized by feeding glucose solution at 4 ml / min, the solution concentration of feeding glucose is 50%, and the aeration rate in the middle and late stage of fermentation is 0.15 liter / min;

[0027] The raw materials and weight of the fermentation medium: 40 g / liter of glucose, 120 g / liter of xylose, 20 g / liter of yeast extract, 5 g / liter of potassium dihydrogen phosphate, and 0.3 g / liter of magnesium sulfate.

Embodiment 3

[0029] Pachysomyces tannophilus ( Pachysolen tannophilus ) into the fermentation medium, the amount of access is 8%, the fermentation time is 36 hours, the culture temperature is 30°C, and the tank pressure is 0.8 kg / cm 2 , the stirring speed is 300 rpm, and the pH is pH5;

[0030] The early stage of fermentation is the natural redox potential, the ventilation rate in the early stage of fermentation is 3.5 liters per minute, and the fermentation time in the early stage of fermentation is 24 hours; Milliliters / minute feed glucose solution to realize, the solution concentration of feed glucose is 50%, the ventilation rate in the middle and late stage of fermentation is 0.3 liters / minute;

[0031] The raw materials and weight of the fermentation medium: 45 g / liter of glucose, 110 g / liter of xylose, 18 g / liter of yeast extract, 4.5 g / liter of potassium dihydrogen phosphate, and 0.15 g / liter of magnesium sulfate.

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Abstract

The invention relates to a fermentation production method for xylitol, which is based on the mastery of principle of preparing the xylitol through fermentation of Pachysolen tannophilus. According to the method, the fermentation process comprises two stages of Pachysolen tannophilus proliferation and xylitol fermentation, at the first stage, fermentation liquor dissolved oxygen is improved through filling large amounts of oxygen so as to increase the proliferation speed of the Pachysolen tannophilus and shorten the fermentation time; and at the second stage, the oxidation-reduction potential of fermentation liquor can be adjusted through controlling feeding glucose amount, so as to improve the conversion efficiency of the xylitol. According to the invention, the production is carried out in a fermentation tank of 5000 L, the fermentation time is shortened to 36 hours, the xylose consumption rate is 95 percent, the xylitol conversion rate is 99 percent, and the production speed rate of the xylitol is 7.23 g / liter per hour. Compared with a conventional fermentation, the xylitol conversion rate is improved by 10 percent; the production speed rate is improved by 7 percent. The method integrates fermentation and regulation and control, has the advantages of being controllable, accurate and economical, and has a wide market prospect.

Description

technical field [0001] The invention belongs to the technical field of xylitol production, in particular to a method for producing xylitol by fermentation. Background technique [0002] Xylitol is a five-carbon polyol, an intermediate product of xylose metabolism, and is mainly used as a sweetener and food additive. In recent years, the market demand for xylitol has continued to expand, and the annual output value of xylitol in China has reached 1.2 billion yuan. At present, the industrial production of xylitol is mainly the chemical hydrogenation method, and the yield from xylose to xylitol is only about 50-60%. The bioconversion method is to use the hemicellulose hydrolyzate rich in xylose to convert xylose into xylitol through a biological method. The process does not need to purify xylose, nor does it need high-pressure equipment. It is easy to separate and purify, and reduces production costs. Produce good social and economic benefits. [0003] At present, there are ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C12P7/18C12R1/645
Inventor 杨培周姜绍通郑志罗水忠潘丽军陈淼林齐蕴艺
Owner HEFEI UNIV OF TECH
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