阅读说明：本技术 一种n-乙酰氨基葡萄糖的发酵生产方法 (Fermentation production method of N-acetylglucosamine ) 是由 卢健行 刘长峰 卢建智 张建华 吴祥舟 于 2019-12-09 设计创作，主要内容包括：本发明公开了一种N-乙酰氨基葡萄糖的发酵生产方法,将大肠杆菌、枯草芽孢杆菌、酿酒酵母菌制得混合发酵剂接种至发酵培养基中恒温摇床培养；发酵过程采用恒速补料方式进行,控制葡萄糖补料速度为3-5g/L·h,用氨水控制发酵过程pH不小于6.9,当发酵液OD600nm大于30时,加入诱导剂IPTG、甲醇溶液和半胱氨酸溶液,培养时间为35-72h。本发明通过混合发酵剂提高大肠杆菌活性,并通过多种手段降低谷氨酸的累积速度,有利于实现产品高产量生产。(The invention discloses a fermentation production method of N-acetylglucosamine, which comprises the steps of preparing a mixed leavening agent from escherichia coli, bacillus subtilis and saccharomyces cerevisiae, inoculating the mixed leavening agent into a fermentation medium, and carrying out constant-temperature shaking table cultivation; the fermentation process is carried out by adopting a constant-speed feeding mode, the feeding speed of glucose is controlled to be 3-5 g/L.h, the pH value of the fermentation process is controlled to be not less than 6.9 by using ammonia water, when the OD600nm of the fermentation liquor is more than 30, an inducer IPTG, a methanol solution and a cysteine solution are added, and the culture time is 35-72 h. The invention improves the activity of the escherichia coli by mixing the leavening agent, reduces the accumulation speed of the glutamic acid by various means, and is beneficial to realizing the high-yield production of products.)

1. A fermentation production method of N-acetylglucosamine is characterized in that: activating the seeds of escherichia coli, bacillus subtilis and saccharomyces cerevisiae to prepare a mixed starter; inoculating the mixed starter to a fermentation medium for constant-temperature shaking table culture; the fermentation process is carried out by adopting a constant-speed feeding mode, the feeding speed of glucose is controlled to be 3-5 g/L.h, the pH value of the fermentation process is controlled to be not less than 6.9 by using ammonia water, when the OD600nm of the fermentation liquor is more than 30, an inducer IPTG, a methanol solution and a cysteine solution are added, and the culture time is 35-72 h.

2. The method for the fermentative production of N-acetylglucosamine according to claim 1, wherein: the inducer IPTG, the methanol solution and the cysteine solution are added into a fermentation system in a feeding mode after being mixed.

3. The method for the fermentative production of N-acetylglucosamine according to claim 2, wherein: in the fermentation system, the final concentration of IPTG is 0.05-0.1mmol/L, the final concentration of cysteine is 1-5g/L, and the final concentration of methanol is 1-5 ml/L.

4. The process for the fermentative production of N-acetylglucosamine according to claim 1 or 2, wherein: the mixed leaven is prepared from the escherichia coli, the bacillus subtilis and the saccharomyces cerevisiae according to the volume ratio of (1-3) to 1: 1.

5. The process for the fermentative production of N-acetylglucosamine according to claim 1 or 2, wherein: the fermentation medium comprises: 35g/L glucose, 20g/L yeast extract powder, 10g/L alanine, 3g/L sodium lactate, 1.05g/L dipotassium hydrogen phosphate, 0.45g/L potassium dihydrogen phosphate, 0.1g/L sodium chloride, 0.3g/L zinc sulfate, 0.5g/L magnesium sulfate, 0.03g/L ferrous sulfate, 3.2g/L lactose and 5.5g/L glycerol.

6. The process for the fermentative production of N-acetylglucosamine according to claim 1 or 2, wherein: and performing activation culture on the escherichia coli and the saccharomyces cerevisiae on a plate culture medium for 6-8 hours before performing seed activation.

7. The method according to claim 4, wherein the fermentation production of N-acetylglucosamine comprises: the plate culture medium comprises 15g/L of peptone, 8g/L of yeast extract, 2g/L of galactose, 1g/L of sodium chloride, 1g/L of ammonium sulfate and 15g/L of agar.

8. The process for the fermentative production of N-acetylglucosamine according to claim 1 or 2, wherein: the seed activation of the escherichia coli and the saccharomyces cerevisiae is to inoculate the strain in a seed culture medium, the culture temperature is controlled to be 37 ℃, the shaking table speed is 220 and 270rpm, and the culture time is 12-14 h.

9. The method of claim 6, wherein the fermentation process of producing N-acetylglucosamine comprises: the seed culture medium comprises 11.5g/L of peptone, 20g/L of yeast extract powder, 2g/L of galactose, 5g/L of sodium chloride, 2g/L of ammonium sulfate and 5.5g/L of glycerol.

10. The process for the fermentative production of N-acetylglucosamine according to claim 1 or 2, wherein: the rotating speed of a shaking table is controlled to be 230-.

Technical Field

The invention belongs to the technical field of biological fermentation, and particularly relates to a fermentation production method of N-acetylglucosamine.

Background

Glucosamine (GleN) is an important hexosamine formed by substituting one hydroxyl group of glucose with an amino group, and there are two main types of glucosamine on the market today, one is glucosamine hydrochloride and the other is glucosamine sulfate. D-Glucosamine Hydrochloride (D-Glucosamine Hydrochloride), molecular formula C₆H₁₃NO₅HCl, a white crystal, odorless, slightly sweet, easily soluble in water, slightly soluble in methanol, insoluble in organic solvents such as ethanol, has important physiological functions for human body, participates in liver and kidney detoxification, plays a role in anti-inflammation and liver protection, has good curative effect on rheumatic arthritis and gastric ulcer, and is a main raw material for synthesizing antibiotics and anticancer drugs; can also be used in food, cosmetic and feed additive. Glucosamine hydrochloride is extracted from natural chitin, is a marine biological agent, and is the main component of chondroitin sulfate. It can promote the synthesis of mucopolysaccharide, raise the viscosity of joint synovial fluid, improve the metabolism of joint cartilage, promote the repair of joint cartilage and has obvious antiphlogistic and analgesic effects. It has the effect of promoting the injection efficiency of antibiotics, and can be used as nutritional supplement for diabetic patients.

N-acetylglucosamine is a white needle crystal, odorless, easily soluble in water, an important glucosamine derivative, is a basic composition unit of a plurality of important polysaccharides in biological cells, is a special monosaccharide with higher sweetness, has reducibility, is an important precursor for synthesizing bifidus factors, has important physiological functions in organisms, is clinically a medicament for treating rheumatic and rheumatoid arthritis, is also used as a food antioxidant and an infant food additive, is a sweetener for diabetics, is widely applied in the fields of food, medicine, chemical industry and the like, and has wide market prospect. At present, the domestic acquisition method of N-acetylglucosamine mainly comprises two methods, namely a chemical method and a biological method, wherein the biological method is used for synthesizing the N-acetylglucosamine by a microbial fermentation method, and has the advantages of short production time and high efficiency. However, glucosamine accumulated in the synthesis of N-acetylglucosamine by a fermentation method or N-acetylglucosamine can be transferred from the extracellular part into cells to be used as a carbon source, so that a large amount of N-acetylglucosamine cannot be accumulated in a fermentation liquid, and industrial production is difficult to realize.

Disclosure of Invention

In order to make up the defects of the prior art, the invention provides the fermentation production method of the N-acetylglucosamine, which has the advantages of high production efficiency, low cost and simple operation.

The invention is realized by the following technical scheme:

a fermentation production method of N-acetylglucosamine is characterized in that: activating the seeds of escherichia coli, bacillus subtilis and saccharomyces cerevisiae to prepare a mixed starter; inoculating the mixed starter to a fermentation medium for constant-temperature shaking table culture; the fermentation process is carried out by adopting a constant-speed feeding mode, the feeding speed of glucose is controlled to be 3-5 g/L.h, the pH value of the fermentation process is controlled to be not less than 6.9 by using ammonia water, when the OD600nm of the fermentation liquor is more than 30, an inducer IPTG, a methanol solution and a cysteine solution are added, and the culture time is 35-72 h.

Preferably, the inducer IPTG, the methanol solution and the cysteine solution are added into the fermentation system in a feeding mode after being mixed, so that the accumulation speed of the glutamic acid can be slowed down.

Further, in a fermentation system, the final concentration of IPTG is 0.05-0.1mmol/L, the final concentration of cysteine is 1-5g/L, and the final concentration of methanol is 1-5 ml/L; IPTG is used as inducer to induce the protein expression of colibacillus and bacillus subtilis, methanol solution induces the expression of saccharomyces cerevisiae, and cysteine is added to inhibit the accumulation of glutamic acid.

The mixed leaven is prepared from the escherichia coli, the bacillus subtilis and the saccharomyces cerevisiae according to the volume ratio of (1-3) to 1: 1.

The fermentation medium comprises: 35g/L glucose, 20g/L yeast extract powder, 10g/L alanine, 3g/L sodium lactate, 1.05g/L dipotassium hydrogen phosphate, 0.45g/L potassium dihydrogen phosphate, 0.1g/L sodium chloride, 0.3g/L zinc sulfate, 0.5g/L magnesium sulfate, 0.03g/L ferrous sulfate, 3.2g/L lactose and 5.5g/L glycerol.

And performing activation culture on the escherichia coli and the saccharomyces cerevisiae on a plate culture medium for 6-8 hours before performing seed activation.

The plate culture medium comprises 15g/L of peptone, 8g/L of yeast extract, 2g/L of galactose, 1g/L of sodium chloride, 1g/L of ammonium sulfate and 15g/L of agar.

The seed activation of the escherichia coli and the saccharomyces cerevisiae is to inoculate the strain in a seed culture medium, the culture temperature is controlled to be 37 ℃, the shaking table speed is 220 and 270rpm, and the culture time is 12-14 h.

The seed culture medium comprises 11.5g/L of peptone, 20g/L of yeast extract powder, 2g/L of galactose, 5g/L of sodium chloride, 2g/L of ammonium sulfate and 5.5g/L of glycerol.

The rotating speed of a shaking table is 230-.

The invention has the beneficial effects that: according to the invention, the fermentation activity is improved by mixing the leavening agent, and simultaneously, the saccharomyces cerevisiae is used as the leavening agent under the induction action of the methanol solution, so that the yield of the N-acetylglucosamine is increased, the glucosamine is finally produced by high-efficiency fermentation, the production speed of glutamic acid in the fermentation process can be reduced by adding cysteine, and the synthesis rate of the N-acetylglucosamine is improved.

Detailed Description

The present invention will be described in further detail with reference to specific embodiments thereof to assist those skilled in the art in providing a more complete, accurate and thorough understanding of the inventive concept and aspects thereof, and the scope of the present invention includes, but is not limited to, the following examples, and any modifications in the details and form of the technical aspects thereof that fall within the spirit and scope of the present application are intended to be included therein.

The raw materials used in the invention are all common raw materials sold in the market.

The following examples all follow the following medium composition:

the plate culture medium comprises: 15g/L of peptone, 8g/L of yeast extract powder, 2g/L of galactose, 1g/L of sodium chloride, 1g/L of ammonium sulfate and 15g/L of agar.

The seed culture medium comprises: the seed culture medium comprises 11.5g/L of peptone, 20g/L of yeast extract powder, 2g/L of galactose, 5g/L of sodium chloride, 2g/L of ammonium sulfate and 5.5g/L of glycerol.

The fermentation medium comprises: 35g/L glucose, 20g/L yeast extract powder, 10g/L alanine, 3g/L sodium lactate, 1.05g/L dipotassium hydrogen phosphate, 0.45g/L potassium dihydrogen phosphate, 0.1g/L sodium chloride, 0.3g/L zinc sulfate, 0.5g/L magnesium sulfate, 0.03g/L ferrous sulfate, 3.2g/L lactose and 5.5g/L glycerol.