CN1276087C - Process for biologically synthesizing gamma-amino butyric acid - Google Patents
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Abstract
Description
技术领域technical field
本发明涉及一种生物合成γ-氨基丁酸的方法。The invention relates to a method for biosynthesizing γ-aminobutyric acid.
背景技术Background technique
γ-氨基丁酸(简称GABA)是一种具有重要生理活性的非蛋白质氨基酸,是中枢神经系统重要的神经递质。大量文献报道,GABA具有降血压和胆固醇、降低神经元活性,防止神经细胞过热,不仅具有安神和抗除抑郁作用,而且还能增强脑功能和长期记忆、增加生长激素分泌、防止肥胖、健肝利肾、改善更年期综合症等功能。随着对GABA生理活性的不断深入研究,最新研究发现的γ-氨基丁酸的生理功能越来越多。GABA也越来越多地受到了更多的关注,GABA在生物体内虽然广泛存在,但无论动、植物中,含量却都很低,分离很困难,需要对其进行合成制备。对于它的合成制备方法主要有化学合成法和生物合成方法。与化学合成方法相比,生物法合成GABA是利用生物体内的谷氨酸脱羧酶作为催化剂,以L-谷氨酸钠(L-MSG)为底物,将L-谷氨酸钠(L-MSG)α-脱羧,产生γ-氨基丁酸和CO2,主要优点在于合成条件温和,不需要昂贵的原材料,环境污染小,能耗小。采用生物法合成GABA的关键之一就是筛选出具有高谷氨酸脱羧酶活力的优良菌株。有文献报道,GABA的生物合成通常采用大肠杆菌作为生产菌株,但是用大肠杆菌作为生产菌株存在食品安全卫生方面的隐患,本实验室筛选到一株具有高效生物合成GABA能力的乳酸菌株。本文报道了一种生物合成GABA的方法。γ-Aminobutyric acid (GABA for short) is a non-protein amino acid with important physiological activity and an important neurotransmitter in the central nervous system. A large number of literature reports that GABA can lower blood pressure and cholesterol, reduce neuron activity, and prevent nerve cell overheating. It not only has the effect of calming the nerves and anti-depression, but also enhances brain function and long-term memory, increases growth hormone secretion, prevents obesity, and strengthens the liver. Kidney benefit, improve menopausal syndrome and other functions. With the continuous in-depth research on the physiological activity of GABA, more and more physiological functions of γ-aminobutyric acid have been discovered in the latest research. GABA has also received more and more attention. Although GABA exists widely in organisms, its content is very low in animals and plants, and its separation is very difficult. It needs to be synthesized. There are mainly chemical synthesis method and biosynthesis method for its synthetic preparation method. Compared with the chemical synthesis method, the biosynthesis of GABA utilizes the glutamic acid decarboxylase in the organism as a catalyst, and L-sodium glutamate (L-MSG) is used as a substrate to convert L-sodium glutamate (L- MSG) α-decarboxylation to produce γ-aminobutyric acid and CO 2 , the main advantages are mild synthesis conditions, no need for expensive raw materials, less environmental pollution, and less energy consumption. One of the keys to biosynthesize GABA is to screen out excellent strains with high glutamic acid decarboxylase activity. It has been reported in the literature that Escherichia coli is usually used as the production strain for the biosynthesis of GABA, but there are hidden dangers in food safety and hygiene when using Escherichia coli as the production strain. Our laboratory screened out a lactic acid strain with high-efficiency biosynthesis of GABA. This paper reports a method for the biosynthesis of GABA.
发明内容Contents of the invention
本发明的目的是提供一种生物合成γ-氨基丁酸的方法。The purpose of the present invention is to provide a method for biosynthesizing γ-aminobutyric acid.
保藏编号为:CGMCC NO.1306的短乳杆菌(Lactobacillus brevis),经琼脂斜面培养基活化后,转接于GYP种子培养基或MRS种子培养基,培养10~30小时后,以0.5%~5%的接种量接种于GYP或MRS发酵培养基中,在25℃~35℃下静置培养48h~120h,即得含菌体的发酵液,菌体离心分离收集;离心后的菌体再以灭过菌的去离子水洗涤,取0.25~2g湿菌体,悬浮于15~50mL的柠檬酸-磷酸氢二钠缓冲体系中,L-谷氨酸钠含量为5mM~60mM,反应1~10小时,反应液离心即得含γ-氨基丁酸的溶液。The preservation number is: Lactobacillus brevis (Lactobacillus brevis) of CGMCC NO.1306, after being activated by agar slant medium, transferred to GYP seed medium or MRS seed medium, after culturing for 10-30 hours, with 0.5%-5 % of the inoculum was inoculated in GYP or MRS fermentation medium, and cultured at 25°C-35°C for 48h-120h to obtain the fermentation liquid containing bacteria, and the bacteria were collected by centrifugation; the centrifuged bacteria were then Wash with sterilized deionized water, take 0.25-2g of wet bacteria, suspend in 15-50mL citric acid-disodium hydrogen phosphate buffer system, the content of L-sodium glutamate is 5mM-60mM, and react for 1-10 hours, the reaction solution was centrifuged to obtain a solution containing γ-aminobutyric acid.
保藏编号为:CGMCC NO.1306的短乳杆菌(Lactobacillus brevis),在发酵时产乳酸,显微镜观察成对或成链状出现,不运动,无孢子,菌落小,表面光滑;属于革兰氏阳性菌株,兼性厌氧。The preservation number is: Lactobacillus brevis (Lactobacillus brevis) of CGMCC NO.1306, which produces lactic acid during fermentation, appears in pairs or chains under the microscope, does not move, has no spores, small colonies, smooth surface; belongs to Gram-positive strain, facultatively anaerobic.
本发明采用短乳杆菌作为菌种,菌体生长达到稳定期,收集菌体,采用全细胞催化,以L-谷氨酸钠(L-MSG)为底物,以柠檬酸-磷酸氢二钠为缓冲体系,无其它碳氮源等其它培养基成分,利用乳酸菌体内含有高活性谷氨酸脱羧酶,将L-谷氨酸钠(L-MSG)α-脱羧,产生γ-氨基丁酸,GABA产量达到1~6g/L。本方法的优点在于生产成本低、反应条件温和、环境污染小、方法简单、易于操作,周期短、生产效率高,并且产品纯度较高,减轻了后续分离纯化工艺。In the present invention, Lactobacillus brevis is used as the strain, and the growth of the thallus reaches a stable period, and the thallus is collected, catalyzed by whole cells, with L-sodium glutamate (L-MSG) as the substrate, and citric acid-disodium hydrogen phosphate As a buffer system, there is no other medium components such as other carbon and nitrogen sources, and the highly active glutamic acid decarboxylase in lactic acid bacteria is used to decarboxylate L-sodium glutamate (L-MSG) to produce γ-aminobutyric acid. GABA production reached 1 ~ 6g / L. The method has the advantages of low production cost, mild reaction conditions, little environmental pollution, simple method, easy operation, short period, high production efficiency, and high product purity, which reduces the subsequent separation and purification process.
具体实施方式Detailed ways
A.菌株A. strain
本实验室筛选。Screened by this laboratory.
B.培养基B. Medium
1000mL琼脂斜面保藏培养基:葡萄糖10g,酵母膏10g,蛋白胨5g,乙酸钠2g,MgSO4·7H2O 20mg,MnSO4·4H2O 1mg,NaCl 1mg,FeSO4·7H2O 1mg,琼脂15g,pH 6.8。1000mL agar slant preservation medium: glucose 10g, yeast extract 10g, peptone 5g, sodium acetate 2g, MgSO 4 7H 2 O 20mg, MnSO 4 4H 2 O 1mg, NaCl 1mg, FeSO 4 7H 2 O 1mg, agar 15g , pH 6.8.
1000mL GYP种子培养基:葡萄糖10g,酵母膏10g,蛋白胨5g,乙酸钠2g,MgSO4·7H2O 20mg,MnSO4·4H2O 1mg,NaCl 1mg,FeSO4·7H2O 1mg,pH 6.6-7.0。1000mL GYP seed medium: glucose 10g, yeast extract 10g, peptone 5g, sodium acetate 2g, MgSO 4 7H 2 O 20mg, MnSO 4 4H 2 O 1mg, NaCl 1mg, FeSO 4 7H 2 O 1mg, pH 6.6- 7.0.
1000mL GYP发酵培养基:葡萄糖10g,酵母膏10g,蛋白胨5g,乙酸钠2g,MgSO4·7H2O 20mg,MnSO4·4H2O 1mg,NaCl 1mg,FeSO4·7H2O 1mg,一水合L-谷氨酸钠10g,pH 6.6-7.0。1000mL GYP fermentation medium: glucose 10g, yeast extract 10g, peptone 5g, sodium acetate 2g, MgSO 4 7H 2 O 20mg, MnSO 4 4H 2 O 1mg, NaCl 1mg, FeSO 4 7H 2 O 1mg, monohydrate L - Sodium Glutamate 10g, pH 6.6-7.0.
1000mL MRS种子培养基:牛肉膏10g,酵母膏5g,蛋白胨10g,K2HpO42g,柠檬酸铵2g,葡萄糖20g,吐温-801mL,醋酸钠5g,无机盐溶液5mL(MgSO4·7H2O,11.5%;MnSO4·2H2O,2.4%),pH 6.6。1000mL MRS seed medium: beef extract 10g, yeast extract 5g, peptone 10g, K 2 HpO 4 2g, ammonium citrate 2g, glucose 20g, Tween-801mL, sodium acetate 5g, inorganic salt solution 5mL (MgSO 4 7H 2 O, 11.5%; MnSO4-2H2O , 2.4% ) , pH 6.6.
1000mL MRS发酵培养基:牛肉膏10g,酵母膏5g,蛋白胨10g,K2HPO42g,柠檬酸铵2g,葡萄糖20g,吐温-801mL,醋酸钠5g,无机盐溶液5mL(MgSO4·7H2O,11.5%;MnSO4·2H2O,2.4%),一水合L-谷氨酸钠10g,pH 6.6。1000mL MRS fermentation medium: beef extract 10g, yeast extract 5g, peptone 10g, K 2 HPO 4 2g, ammonium citrate 2g, glucose 20g, Tween-801mL, sodium acetate 5g, inorganic salt solution 5mL (MgSO 4 7H 2 O, 11.5%; MnSO 4 ·2H 2 O, 2.4%), 10 g of sodium L-glutamate monohydrate, pH 6.6.
C.制备工艺C. Preparation process
此菌株经琼脂斜面培养基活化后,转接于GYP种子培养基或MRS种子培养基,培养10~30小时后,以0.5%~5%的接种量接种GYP或MRS发酵培养基,在30℃下静置培养48h~120h,即得含菌体的发酵液,菌体通过离心(8000r/min,5min)收集。离心后的菌体再以灭过菌的去离子水洗涤,取0.25~2g湿菌体,悬浮于25mL的柠檬酸-磷酸氢二钠缓冲体系中,L-谷氨酸钠含量为5mM-100mM,反应1~10小时,反应液离心即得含γ-氨基丁酸的溶液。After the strain was activated on agar slant medium, it was transferred to GYP seed medium or MRS seed medium. After culturing for 10-30 hours, inoculate GYP or MRS fermentation medium with an inoculation amount of 0.5%-5%. Under static culture for 48h ~ 120h, the fermentation liquid containing bacteria is obtained, and the bacteria are collected by centrifugation (8000r/min, 5min). After centrifugation, the cells were washed with sterilized deionized water, and 0.25-2 g of wet cells were taken, suspended in 25 mL of citric acid-disodium hydrogen phosphate buffer system, and the content of L-sodium glutamate was 5 mM-100 mM , react for 1 to 10 hours, and centrifuge the reaction solution to obtain a solution containing γ-aminobutyric acid.
该菌株经琼脂斜面培养基活化后,转接于GYP种子培养基或MRS种子培养基,培养10~30小时后,以0.5%~5%的接种量接种GYP或MRS发酵培养基,在30℃下静置培养48h~120h,即得含菌体的发酵液,菌体通过离心(8000r/min,5min)收集。离心后的菌体再以灭过菌的去离子水洗涤,取0.25~2g湿菌体,悬浮于25mL的柠檬酸-磷酸氢二钠缓冲体系中,L-谷氨酸钠含量为5mM-100mM,反应1~10小时,反应液离心即得含γ-氨基丁酸的溶液。After the strain was activated on the agar slant medium, it was transferred to GYP seed medium or MRS seed medium. After culturing for 10-30 hours, it was inoculated with GYP or MRS fermentation medium with an inoculation amount of 0.5%-5%. Under static culture for 48h ~ 120h, the fermentation liquid containing bacteria is obtained, and the bacteria are collected by centrifugation (8000r/min, 5min). After centrifugation, the cells were washed with sterilized deionized water, and 0.25-2 g of wet cells were taken, suspended in 25 mL of citric acid-disodium hydrogen phosphate buffer system, and the content of L-sodium glutamate was 5 mM-100 mM , react for 1 to 10 hours, and centrifuge the reaction solution to obtain a solution containing γ-aminobutyric acid.
实施例1Example 1
此菌株经琼脂斜面培养基活化后,转接于GYP种子培养基,培养时间为24小时,将种子培养液以1%的接种量接种于GYP发酵培养基中,发酵培养基内加1%的一水合L-谷氨酸钠,发酵培养基的装液量为200mL/500mL,静置培养60小时,即得含菌体的发酵液,菌体通过离心(8000r/min,5min)收集。离心后的菌体再以灭过菌的去离子水洗涤,取0.5g湿菌体,悬浮于25mL的柠檬酸-磷酸氢二钠缓冲体系中,L-谷氨酸钠含量为10mM,反应1小时,反应液离心经高效液相色谱分析得,γ-氨基丁酸含量约1g/L。After the strain was activated on the agar slant medium, it was transferred to the GYP seed medium for 24 hours. The seed culture liquid was inoculated in the GYP fermentation medium with 1% inoculation amount, and 1% of Sodium L-glutamate monohydrate, the liquid volume of the fermentation medium is 200mL/500mL, and it is left to culture for 60 hours to obtain the fermentation liquid containing bacteria, and the bacteria are collected by centrifugation (8000r/min, 5min). After centrifugation, the cells were washed with sterilized deionized water, and 0.5 g of wet cells were taken, suspended in 25 mL of citric acid-disodium hydrogen phosphate buffer system, and the content of L-sodium glutamate was 10 mM. Reaction 1 hours, the reaction solution was centrifuged and analyzed by high-performance liquid chromatography, and the content of γ-aminobutyric acid was about 1g/L.
实施例2Example 2
此菌株经琼脂斜面培养基活化后,转接于GYP种子培养基,培养时间为24小时,将种子培养液以1%的接种量接种子GYP发酵培养基中,发酵培养基内加1%的一水合L-谷氨酸钠,发酵培养基的装液量为200mL/500mL,静置培养60小时,即得含菌体的发酵液,菌体通过离心(8000r/min,5min)收集。离心后的菌体再以灭过菌的去离子水洗涤,取0.5g湿菌体,悬浮于25mL的柠檬酸-磷酸氢二钠缓冲体系中,L-谷氨酸钠含量为20mM,反应2小时,反应液离心经高效液相色谱分析得,γ-氨基丁酸含量约2g/L。After the strain was activated on the agar slant medium, it was transferred to the GYP seed medium for 24 hours. The seed culture solution was inoculated into the GYP fermentation medium with 1% inoculation amount, and 1% of the fermented medium was added to the fermentation medium. Sodium L-glutamate monohydrate, the liquid volume of the fermentation medium is 200mL/500mL, and it is left to culture for 60 hours to obtain the fermentation liquid containing bacteria, and the bacteria are collected by centrifugation (8000r/min, 5min). After centrifugation, the cells were washed with sterilized deionized water, and 0.5 g of wet cells were taken, suspended in 25 mL of citric acid-disodium hydrogen phosphate buffer system, and the content of L-sodium glutamate was 20 mM. Reaction 2 hours, the reaction solution was centrifuged and analyzed by high performance liquid chromatography, and the content of γ-aminobutyric acid was about 2g/L.
实施例3Example 3
此菌株经琼脂斜面培养基活化后,转接于GYP种子培养基,培养时间为24小时,将种子培养液以1%的接种量接种于GYP发酵培养基中,发酵培养基内加1%的一水合L-谷氨酸钠,发酵培养基的装液量为200mL/500mL,静置培养60小时,即得含菌体的发酵液,菌体通过离心(8000r/min,5min)收集。离心后的菌体再以灭过菌的去离子水洗涤,取0.5g湿菌体,悬浮于25mL的柠檬酸-磷酸氢二钠缓冲体系中,L-谷氨酸钠含量为40mM,反应3小时,反应液离心经高效液相色谱分析得,γ-氨基丁酸含量约4g/L。After the strain was activated on the agar slant medium, it was transferred to the GYP seed medium for 24 hours. The seed culture liquid was inoculated in the GYP fermentation medium with 1% inoculation amount, and 1% of Sodium L-glutamate monohydrate, the liquid volume of the fermentation medium is 200mL/500mL, and it is left to culture for 60 hours to obtain the fermentation liquid containing bacteria, and the bacteria are collected by centrifugation (8000r/min, 5min). After centrifugation, the cells were washed with sterilized deionized water, and 0.5 g of wet cells were taken, suspended in 25 mL of citric acid-disodium hydrogen phosphate buffer system, and the content of L-sodium glutamate was 40 mM. Reaction 3 hours, the reaction solution was centrifuged and analyzed by high performance liquid chromatography, and the content of γ-aminobutyric acid was about 4g/L.
实施例4Example 4
此菌株经琼脂斜面培养基活化后,转接于GYP种子培养基,培养时间为24小时,将种子培养液以1%的接种量接种于GYP发酵培养基中,发酵培养基内加1%的一水合L-谷氨酸钠,发酵培养基的装液量为200mL/500mL,静置培养60小时,即得含菌体的发酵液,菌体通过离心(8000r/min,5min)收集。离心后的菌体再以灭过菌的去离子水洗涤,取0.5g湿菌体,悬浮于25mL的柠檬酸-磷酸氢二钠缓冲体系中,L-谷氨酸钠含量为60mM,反应5小时,反应液离心经高效液相色谱分析得,γ-氨基丁酸含量约6g/L。After the strain was activated on the agar slant medium, it was transferred to the GYP seed medium for 24 hours. The seed culture liquid was inoculated in the GYP fermentation medium with 1% inoculation amount, and 1% of Sodium L-glutamate monohydrate, the liquid volume of the fermentation medium is 200mL/500mL, and it is left to culture for 60 hours to obtain the fermentation liquid containing bacteria, and the bacteria are collected by centrifugation (8000r/min, 5min). After centrifugation, the bacteria were washed with sterilized deionized water, and 0.5 g of wet bacteria was taken, suspended in 25 mL of citric acid-disodium hydrogen phosphate buffer system, and the content of L-sodium glutamate was 60 mM. hours, the reaction solution was centrifuged and analyzed by high performance liquid chromatography, and the content of γ-aminobutyric acid was about 6g/L.
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| WO2009103547A1 (en) * | 2008-02-21 | 2009-08-27 | Basf Se | Process for the production of gamma-aminobutyric acid |
| CN101724587B (en) * | 2009-09-10 | 2011-10-12 | 浙江师范大学 | Lactobacillus brevis L2 bacterial strain of high yield gamma-aminobutyrique and screening method and applications thereof |
| CN102174449B (en) * | 2011-03-04 | 2012-08-22 | 天津科技大学 | Method for producing high-yield gamma-propalanine and application thereof |
| CN102260720A (en) * | 2011-07-20 | 2011-11-30 | 贵州大学 | Method for producing gamma-aminobutyric acid by using Lactobacillus fructivorans |
| CN102559552B (en) * | 2012-01-09 | 2014-06-11 | 天津科技大学 | Production method and application of high-yield gamma-aminobutyric acid |
| CN102796779B (en) * | 2012-08-24 | 2013-11-20 | 南通励成生物工程有限公司 | Biological method for preparing gamma-aminobutyric acid |
| CN103966274B (en) * | 2013-02-05 | 2017-03-15 | 中国科学院海洋研究所 | A kind of method that gamma aminobutyric acid is produced as raw materials through biotransformation with aquatic products and its processing fent |
| CN108300742A (en) * | 2017-07-26 | 2018-07-20 | 南通励成生物工程有限公司 | A kind of method that current adding substrate enzyme prepares γ-aminobutyric acid |
| CN113061061A (en) * | 2021-02-19 | 2021-07-02 | 安徽丰乐农化有限责任公司 | Preparation method of chemical fertilizer rich in gamma-aminobutyric acid |
| CN114058653B (en) * | 2021-12-29 | 2024-02-09 | 南通励成生物工程有限公司 | Method for preparing gamma-aminobutyric acid by biological synthesis method |
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