聚γ-谷氨酸高产菌的选育与培养基优化

利用合成培养基为筛选培养基,以枯草芽孢杆菌(Bacillus subtilis)B6-1为出发菌株,经过三轮紫外线诱变和一轮硫酸二乙酯诱变得到了聚γ-谷氨酸高产突变株枯草芽孢杆菌W003,摇瓶液体发酵的聚γ-谷氨酸产量由出发菌株的10.9 g/L提高到20.5 g/L.单因素实验结果表明,该菌产聚γ-谷氨酸的合适碳源为葡萄糖,氮源为硫酸铵.通过正交实验得到了优化的培养基配方,经36h液体发酵,聚γ-谷氨酸产量可达到45.3 g/L.     

γ-聚谷氨酸高产菌株筛选及发酵条件优化

γ聚谷氨酸是一种生物可降解的高分子材料,可应用于多种领域,因此受到普遍重视。报道了以11株枯草芽孢杆菌菌株为培养菌株,用3种谷氨酸钠含量不同的培养基进行筛选获得1株γ聚谷氨酸高产菌株;再以该菌株为研究对象进行碳源、氮源、谷氨酸钠浓度、初始pH、接种量、通气量等发酵条件的优化实验,结果表明最佳发酵条件为:250ml三角烧瓶装液40ml,接种体积分数5%,麦芽糖50g/L,酵母膏10g/L,谷氨酸钠30g/L,NaCl10g/L,KH₂PO₄5g/L,MgSO₄·7H₂O0.5g/L,初始pH6.0,发酵60h,此时γ聚谷氨酸产量最高,达到30.26g/L,比国外报道的20g/L的产量有显著提高。纯化后产物经红外光谱及核磁共振检测,鉴定为γ聚谷氨酸。     

原生质体诱变选育ε-聚赖氨酸高产菌株

以白色链霉菌UN2-71为出发菌株,对其原生质体进行硫酸二乙酯(DES)诱变,选育ε-聚赖氨酸高产菌株。经过试管初筛和摇瓶复筛,得到1株稳定性好的菌株D3-32,摇瓶产量达到1.56g/L,比出发菌株提高49.43%。采用2.3L发酵罐进行发酵试验,控制pH分两阶段培养后,ε-聚赖氨酸最高产量达到4.59g/L,比出发菌株提高了2.65倍。     

谷氨酸棒杆菌一步法发酵糖质原料生产γ-聚谷氨酸

γ-聚谷氨酸在食品、化妆品、生物医药等领域具有广泛的应用,目前主要的生产菌株是谷氨酸依赖型菌株,在生产过程中需要添加谷氨酸作为前体,因而生产γ-聚谷氨酸的成本较高。文中主要研究从糖质原料一步法发酵合成γ-聚谷氨酸的生产工艺。首先,从产γ-聚谷氨酸的菌株枯草芽孢杆菌中克隆γ-聚谷氨酸合成酶的基因簇pgs BCA,在谷氨酸棒杆菌模式菌株ATCC13032中进行诱导型和组成型表达,结果显示,仅诱导型表达菌株可以积累γ-聚谷氨酸,产量为1.43 g/L。进一步对诱导条件进行优化,确定诱导时间为2 h,IPTG浓度为0.8 mmol/L,γ-聚谷氨酸产量为1.98g/L。在此基础上,在一株高产谷氨酸的谷氨酸棒杆菌F343中外源表达pgs BCA,对重组菌进行发酵,结果表明,在摇瓶发酵中γ-聚谷氨酸产量达到10.23g/L,在5L发酵罐中产量达到20.08g/L;继而对γ-聚谷氨酸进行分子量测定,结果显示,产自F343重组菌的γ-聚谷氨酸的重均分子量比产自枯草芽孢杆菌的提高34.77%。文中构建了一步法发酵糖质原料生产γ-聚谷氨酸的新途径,同时为开发其潜在应用奠定了基础。     

L-缬氨酸高产菌株的选育研究

以产L-缬氨酸的谷氨酸棒状杆菌(Corynebacterium glutamicum)为原始菌株,利用注入低能氮离子束进行一系列诱变,获得一株稳定的高产L-缬氨酸突变菌株。摇瓶培养96h后发酵能力可达38.0g·L-1,较出发菌株提高18.01%。通过对摇瓶中葡萄糖、玉米浆浓度及培养条件进行优化,发酵能力达到40.6g·L-1,50L发酵罐的发酵能力可达70g·L-1左右。     

产L-谷氨酸工程菌株的诱变选育及其发酵效率

以高产L-谷氨酸的谷氨酸棒杆菌GY1为研究对象,采用ARTP进行全局诱变,进一步提高L-谷氨酸的发酵水平。首先,对谷氨酸棒杆菌GY1原生质体的制备及再生条件进行优化,接着,根据致死率选择最佳的ARTP处理时间,然后,采用96微孔板及摇瓶发酵的方式对突变株进行筛选,最后,对获得的优良突变株进行50 L罐发酵验证。结果显示,溶菌酶浓度为10.0 mg/mL,酶解90 min,原生质体形成率和再生率达到最佳。ARTP最佳处理时间为40 s,致死率达到89.6%,经过初筛与摇瓶复筛,获得突变株YAG117,其摇瓶发酵L-谷氨酸含量达16.3 g/L,较出发菌株提高13.9%,且连续传代五代遗传稳定。50 L补料分批发酵条件下,L-谷氨酸产量在36 h最高,达到216.6 g/L,较出发菌株提高12.9%,糖酸转化率达68.87%,比出发菌株提高了10.2%。ARTP处理GY1菌株原生质体,能够有效积累有利突变,提高突变株发酵生产L-谷氨酸的能力,获得的突变株YAG117也显示了较好的工业化应用潜力。     

产赤藓糖醇菌种的诱变育种

以耐高渗酵母为出发菌株,采用紫外线诱变处理,得到了一株变异株C1。其摇瓶发酵产赤藓糖醇24．9g／L左右。通过摇瓶发酵试验,研究了菌株C1的遗传稳定性。研究结果表明,经多次传代实验,菌株C1的发酵产糖醇能力没有改变,表明其是稳定的变异株。赤藓糖醇的产量由诱变前的12、594g／L提高到24.943g／L,提高了98.1％。关键词：     

虾青素高产菌的选育

红发夫酵母（Phaffia rhodozyma)是微生物发酵法生产虾青素的优良菌株,作者采用Cs^137-γ射线重复辐照,并进行亚硝基胍（NTG）诱变处理,选育得到一株高产虾青素的红发夫酵母YB-20-28突变株,该菌株摇瓶发酵的生物量达老人家酵母YB-20-28突变株,该菌株摇瓶发酵的生物量达36.3g/L,总色素含量为1216.0μg/g,较出发菌株提高308%,虾青素产量达30.9μg/mL,是一株颇具开发潜力的虾青素高产菌株。     

γ-聚谷氨酸生产菌的选育及培养条件研究

从土壤中筛选分离到1株γ聚谷氨酸的生产菌株yt102,初步鉴定为枯草芽孢杆菌;以此为出发菌株采用紫外线(UV)、亚硝基胍(NTG)进行复合诱变,获得1株γ聚谷氨酸高产突变株,突变株连续传代10次,发酵性能稳定;通过单因素和正交试验确定培养基的最佳组成,在最优条件下,γ聚谷氨酸的平均产量可达28.5 g/L。     

聚-ε-赖氨酸高产菌株的筛选及其发酵工艺的初步研究

利用亚甲基蓝平板初筛、摇瓶复筛,从土壤中筛选了一株聚-ε-赖氨酸（ε-PL）高产菌株,ε-PL摇瓶产量大于2g/L,经初步鉴定该菌株为白色链霉菌（Streptomyces albulus）。对该菌株发酵生产ε-PL的培养基成分进行初步研究表明：葡萄糖是最好的碳源,酵母粉和硫酸铵是最佳的复合氮源,在优化培养基下,ε-PL摇瓶产量达到3.9 g/L。     

A newly isolated Bacillus siamensis SB1001 for mass production of poly-γ-glutamic acid

Poly-γ-glutamic acid (γ-PGA) is a retaining agent; it has applications in the food, medicine, agriculture, cosmetics and wastewater treatment industries. Most of the γ-PGA producing strains belong to the genus Bacillus. This study reports on a novel γ-PGA producing species. Bacillus siamensis SB1001 was screened and isolated from organically cultivated soybeans exhibiting a high γ-PGA producing ability. The fermentation medium and culture parameters for γ-PGA production by Bacillus siamensis SB1001 were optimized by statistical methods. The sucrose, l-glutamic acid and dipotassium phosphate in the medium were shown to be the significant factors of the γ-PGA production, and the optimum medium obtained consisted of the following: 106.86 g/L sucrose, 69.84 g/L l-glutamic acid and 2.39 g/L dipotassium phosphate. Using the optimized medium, 25.22 g/L γ-PGA were produced with a productivity of 1.05 g/L/h. The γ-PGA obtained had a molecular weight of 7.9 × 10⁵ Da and a polydispersity index of 2.34, and the ratio of d-/L-glutamic acid was 89.71%:10.29%. To the best of our knowledge, this is the first report of γ-PGA production by B. siamensis strain. B. siamensis SB1001 has great potential as an industrial γ-PGA producer.     

添加物对枯草芽胞杆菌γ-聚谷氨酸合成代谢的影响

在枯草芽孢杆菌HCUL-B115代谢网络和发酵特性研究的基础上,通过添加适量的氨基酸、有机酸和维生素对聚γ谷氨酸(γPGA)发酵进行合成代谢进行研究。结果发现,大部分添加物对聚γ谷氨酸的积累都有一定的影响,特别是L谷氨酸、L苯丙氨酸、L精氨酸、L天冬氨酸、L缬氨酸、延胡索酸、草酸、丙二酸、烟酸、维生素B6和抗坏血酸等添加物对菌株HCUL-B115合成聚γ谷氨酸有明显促进作用,添加后产率比不添加任何物质提高20%左右。从代谢层面上分析,这些添加物除了促进菌体自身生长之外,同时防止了菌体对各添加物的过量合成,强化了菌株HCUL-B115合成聚γ谷氨酸的代谢途径。     

Physiological and metabolic analysis of nitrate reduction on poly-gamma-glutamic acid synthesis in Bacillus licheniformis WX-02

Nitrate is an important nitrogen source for organism, but whether and how nitrate improves poly-γ-glutamic acid (γ-PGA) production of bacterial is not clear. The effect of nitrate on γ-PGA production of Bacillus licheniformis WX-02 was investigated. By addition of 50 mmol/L nitrate, the γ-PGA yield reached 12.3 ± 0.21 g/L, which increased 2.3-fold compared to the control. The mechanism of enhanced γ-PGA production was further investigated by analysis of nitrate reduction, physiology, pyruvate overflow metabolism and energy synthesis. Nitrate reduction was only carried out in the middle stage of γ-PGA fermentation. The result of consumption of nutrients showed that glucose uptake was not effected and the l-glutamic acid utilization efficiency increased from 48.3 to 77.0 %. The date of overflow metabolism obtained from high-performance liquid chromatography showed that the metabolism of pyruvate, formate, lactate and acetoin was both heightened by nitrate reduction, while the 2,3-butanediol biosynthesis was decreased. Meanwhile, the change of energy indicated that more ATP was synthesized during nitrate reduction. In summary, nitrate was a positive effector of γ-PGA biosynthesis in B. licheniformis WX-02 and nitrate reduction affected multi-metabolism pathways, including glycolysis, overflow metabolism and energy metabolism.     

Functions of poly-gamma-glutamic acid (γ-PGA) degradation genes in γ-PGA synthesis and cell morphology maintenance

Poly-γ-glutamic acid (γ-PGA) is an important biopolymer with greatly potential in industrial and medical applications. In the present study, we constructed a metabolically engineered glutamate-independent Bacillus amyloliquefaciens LL3 strain with considerable γ-PGA production, which was carried out by single, double, and triple markerless deletions of three degradation genes pgdS, ggt, and cwlO. The highest γ-PGA production (7.12 g/L) was obtained from the pgdS and cwlO double-deletion strain NK-pc, which was 93 % higher than that of wild-type LL3 strain (3.69 g/L). The triple-gene-deletion strain NK-pgc showed a 28 % decrease in γ-PGA production, leading to a yield of 2.69 g/L. Furthermore, the cell morphologies of the mutant strains were also characterized. The cell length of cwlO deletion strains NK-c and NK-pc was shorter than that of the wild-type strain, while the ggt deletion strains NK-g, NK-pg, NK-gc, and NK-pgc showed longer cell lengths. This is the first report concerning the markerless deletion of γ-PGA degradation genes to improve γ-PGA production in a glutamate-independent strain and the first observation that γ-glutamyltranspeptidase (encoded by ggt) could be involved in the inhibition of cell elongation.     

一株γ-聚谷氨酸合成菌的筛选与鉴定

从土壤中筛选分离获得一株γ-聚谷氨酸合成菌PGS-1,经鉴定为枯草芽孢杆菌(Bacillus subtilis),在富含谷氨酸和葡萄糖的培养基中可大量合成γ-聚谷氨酸,摇瓶发酵产量达26 g/L,不同于大多文献报道的微生物合成的γ-聚谷氨酸具有较高的分子量,该菌株合成的γ-聚谷氨酸分子量较低(3×105-4×105 kD),分子量分布较窄,可适用于低分子量要求的应用领域,如作为药物的控缓释载体,值得深入开发研究。     

高分子量聚谷氨酸的微生物合成及其发酵过程的研究

目的：以枯草芽孢杆菌纳豆亚种为出发菌株,考察不同碳氮源及NaCl浓度、谷氨酸、种龄、接种量对微生物发酵产1-聚谷氨酸的影响,以提高γ-聚谷氨酸的产量。方法：该菌菌种活化后,接入种子培养基,于37℃、200r／min震荡培养18h,然后按2％接种量接入不同发酵培养基进行发酵培养。γ-聚谷氨酸分离纯化后,根据其产量筛选最适发酵培养基组成及发酵条件,并对产物进行分析测定。结果：①最佳碳氮源分别为葡萄糖、蛋白胨,NaCl浓度为30g／L、种龄15h、接种量3％,且需在培养基中添加谷氨酸。②该菌株在最适条件下发酵56h时,γ-聚谷氨酸产量达32．7g／L,凝胶渗透色谱分析其相对分子质量为426kDa,呈多分子质量聚集体形式。③γ-聚谷氨酸的合成与菌体生长并非完全同步。结论：γ-聚谷氨酸作为一种天然的、可生物降解的、对环境和人体无害的多聚物,可由微生物发酵合成,且在此适宜条件下产量较高。     

Glutamic acid independent production of poly-γ-glutamic acid by Bacillus amyloliquefaciens LL3 and cloning of pgsBCA genes

A new glutamic acid independent poly-γ-glutamic acid (γ-PGA) producing strain, which was identified as Bacillusamyloliquefaciens LL3 by analysis of 16S rDNA and gyrase subunit A gene (gyrA), was isolated from fermented food. The product had a molecular weight of 470, 801 and l-glutamate monomer content of 98.47%. The pre-optimal medium, based on single-factor tests and orthogonal design, contained 50 g/L sucrose, 2 g/L (NH₄)₂SO₄, 0.6 g/L MgSO₄, and provided well-balanced changes in processing parameters and a γ-PGA yield of 4.36 g/L in 200 L system. The γ-PGA synthetase genes pgsBCA were cloned from LL3, and successfully expressed by pTrcLpgs vector in Escherichia coli JM109, resulting the synthesis of γ-PGA without glutamate. This study demonstrates the designedly improved yield of γ-PGA in 200 L system and the first report of pgsBCA from glutamic acid independent strain, which will benefit the metabolized mechanism investigation and the wide-ranging application of γ-PGA.     

Improvement of kojic acid production in Aspergillus oryzae B008 mutant strain and its uses in fermentation of concentrated corn stalk hydrolysate

A strain designated M866, producing kojic acid with a high yield, was obtained by combining induced mutation using ion beam implantation and ethyl methane sulfonate treatment of a wild type strain of Aspergillus oryzae B008. The amount of kojic acid produced by the strain M866 in a shaking flask was 40.2 g/L from 100 g/L of glucose, which was 1.7 times higher than that produced by wild strain (23.58 g/L). When the mixture of glucose and xylose was used as carbon source, the resulting kojic acid production was raised with the increasing of glucose ratios in the mixture. With concentrations of glucose at 75 g/L and xylose at 25 g/L mixed in the medium, the production of kojic acid reached 90.8 %, which was slightly lower than with glucose as the sole source of carbon. In addition, the kojic acid fermentation of the concentrated hydrolysate from corn stalk was also investigated in this study, the maximum concentration of kojic acid accumulated at the end of the fermentation was 33.1 g/L and this represents the yield based on reducing sugar consumed and the overall productivity of 0.36 g/g and 0.17 g/L/h, respectively.