Characteristics of batch culture of a recombinant bacillus brevis excreting a foreign esterase

The productivity of extracellular enzyme was evaluated in batch culture using a protein hyperexcreting host, Bacillus brevis HPD31(5) harboring pHSC131, which carried a gene (est) encoding esterase activity from Bacillus stearother mophilus. Optimum temperature and pH for the bacterial growth and the production of extracellular esterase were found to be 35 degrees C and pH 6.5, by using the standard medium (GPY) containing neomycin as a selective pressure, Under the cultivation condition employed, cell growth reached 5 g dry cell weight/L, while the extracellular esterase activity amounted to 4.5 U/mL. Most (79%-92%) of the esterase produced was excreted into the medium. pHSC131 was stably retained in the host cell during cultivation in the presence of neomycin. However, in the absence of neomycin, the plasmid was completely lost from the host after 12-h cultivation accompanied by decreases in both esterase activity and production of total extracellular protein. The copy number of the plasmid was estimated to be approximately 7 throughout the cultivation. Sodium dodecyl sulfate-polyacrylamide gel electrophoresis of the excreted proteins showed the presence of a protein having an apparent molecular weight of 32,000, which equals to the value predicted from the DNA sequence of the est gene.     

枯草芽胞杆菌乙酰木聚糖酯酶的鉴定及诱导剂对酯酶活力的影响

以枯草芽胞杆菌CICC 20034为研究对象,对其分泌的高相对分子质量酯酶进行鉴定,并考察诱导剂对其活力的影响。结果表明:枯草芽胞杆菌CICC 20034可分泌一种相对分子质量为1.07×105的酯酶,经蛋白质质谱鉴定为乙酰木聚糖酯酶,单体分相对子质量为3.56×104。在发酵培养基中添加乙酸乙酯和木糖可以显著的促进乙酰木聚糖酯酶的活力,而三丁酸甘油酯和大分子诱导剂——木聚糖、玉米芯粉和壳聚糖对酯酶的活力几乎无促进作用。枯草芽胞杆菌CICC 20034以乙酸乙酯为诱导剂时最高比酶活为0.62 U/mL,为已知报道的野生细菌乙酰木聚糖酯酶的最高酯酶活力。     

Effect of culture conditions on growth and esterase production by the moderate thermophile Bacillus circulans MAS2

Growth and esterase production (activity on p-nitrophenyl caprylate) by the newly isolated Bacillus circulans MAS2 bacterial strain were studied. The growth rate at 50°C was high (0.9 h^-1) on LB medium with glucose added. Esterase production followed growth with the majority of activity being intracellular during exponential growth phase. During stationary phase, the esterase activity was released in the culture medium. The strain was able to grow at 35– 55°C with maximum growth rate at 50°C, showing a pattern typical of a moderate thermophile. Growth occurred at pH 6–9 with a maximum at 8, with a similar pattern for the esterase production. Addition of glucose, fructose, sucrose or sodium acetate greatly promoted both growth and esterase production while starch, inulin, tributyrin or glycerol showed no effect. Complex nitrogen sources such as tryptone or yeast extract increased growth and esterase production while mineral sources (ammonium chloride or sulfate), glycine or glutamate showed no effect. An increase of tryptone plus yeast extract and glucose concentrations stimulated growth and esterase production which reached 160 U L⁻¹. Received 17 March 1999/ Accepted in revised form 25 June 1999     

Study and improvement of the conditions for production of a novel alkali stable catalase

Catalase (CAT) is an enzyme capable of catalyzing the conversion of H(2)O(2) to O(2) and H(2)O. It has recently acquired interest due to its attractive potential application in the textile industries. In a previous study, a bacterium with slight halophilic and alkaliphilic characteristics, Bacillus sp. F26, was isolated and found to produce high-level alkaline CAT. In the present study, the effects of culture conditions on the CAT production were investigated. The results showed that the highest activity of CAT (13.9 U/mg protein) was obtained when glucose (15 g/L) was used as carbon source. The utilization of the mixture of corn steep liquid and beef extract stimulated both bacterial growth and CAT synthesis. The highest biomass (4.5 g/L) and activity of CAT (16.5 U/mg protein) were found synchronously when 10 g/L corn steep liquid and 10 g/L beef extract were used as nitrogen source. The addition of H(2)O(2) as an oxidative stress was used to enhance CAT production in the flasks. It was found that the activity of CAT was increased by 51.3-22.8 U/mg protein compared with the control when 2 mmol/L H(2)O(2) was added at later exponential phases (16 h), although the cell growth was significantly inhibited. Based on the above, an exponential H(2)O(2) feed strategy was developed, in which the feed rate of H(2)O(2) was controlled according to specific cell growth rate (mu). In this way, the maximum CAT production (29.9 U/mL) was obtained, which was 92.8 and 20.7% higher than that in batch and constant rate fed-batch fermentation, respectively.     

Production of recombinant beta-amylase of Bacillus aryabhattai

In this study, the effects of carbon source, nitrogen source, and metal ions on cell growth and Bacillus aryabhattai β-amylase production in recombinant Brevibacillus choshinensis were investigated. The optimal medium for β-amylase production, containing glucose (7.5?g·L^?1), pig bone peptone (40.0?g·L^?1), Mg²⁺ (0.05?mol·L^?1), and trace metal elements, was determined through single-factor experiments in shake flasks. When cultured in the optimized medium, the β-amylase yield reached 925.4?U mL^?1, which was 7.2-fold higher than that obtained in the initial medium. Besides, a modified feeding strategy was proposed and applied in a 3-L fermentor fed with glucose, which achieved a dry cell weight of 15.4?g L^?1. Through this cultivation approached 30?°C with 0?g·L^?1 initial glucose concentration, the maximum β-amylase activity reached 5371.8?U mL^?1, which was 41.7-fold higher than that obtained with the initial medium in shake flask.     

产碱性蛋白酶嗜碱芽孢杆菌的筛选及其研究

利用造纸黑液对土样进行富集,筛选出3株碱性蛋白酶酶活力较高的嗜碱芽孢杆菌X1、X2、X3。对它们的生长曲线,产酶曲线,在不同C、N源、pH值、盐浓度下的产酶活力进行的研究表明:3株嗜碱芽孢杆菌(Bacillussp.JBX1、X2、X5)酶活力较高(达到100U/mL),X2最高酶活可达140U/mL。最适pH值为9.5,碳源中的蔗糖,氮源中的酵母浸提物和硝酸钠均利于产酶。X1、X5两株嗜碱芽孢杆菌均表现出较强的耐盐耐高渗透压的能力。X1在11%的NaCl浓度下生长良好,酶活仍然达到80U/mL以上。而X2和X5对温度的耐受性比较强,在经70℃处理15min后依然保持了80%以上的酶活力,所产蛋白酶为高温碱性蛋白酶,从而为进一步的应用和研究奠定了基础。     

Production of nattokinase by high cell density fed-batch culture of Bacillus subtilis

Bacillus subtilis was cultivated to high cell density for nattokinase production by pH-stat fed-batch culture. A concentrated mixture solution of glucose and peptone was automatically added by acid-supplying pump when culture pH rose above high limit. Effect of the ratio of glucose to peptone in feeding solution was investigated on cell growth and nattokinase production by changing the ratio from 0.2 to 5 g glucose/g peptone. The highest cell concentration was 77 g/L when the ratio was 0.2 g glucose/g peptone. Cell concentration decreased with increasing the ratio of glucose to peptone in feeding solution, while the optimum condition existed for nattokinase production. The highest nattokinase activity was 14,500 unit/mL at a ratio of 0.33 g glucose/g peptone, which was 4.3 times higher than that in batch culture.     

Enhanced beta-galactosidase production by high cell-density culture of recombinant Bacillus subtilis with glucose concentration control

Cell concentration, recombinant protein (beta-galactosidase) level, and the specific enzyme expression level were increased from 19 to 184 g/L, 18.3 to 129 U/mL, and 3.2 to 5.7 U/mg protein, respectively, in fed-batch culture of recombinant Bacillus subtilis when glucose concentration was controlled at 1 g/L as compared with those of conventional fed-batch culture. Glucose concentration of the culture broth was monitored by an automatic on-line glucose analyzer and controlled with a moving identification combined with optimal control (MICOC) strategy. When glucose concentrations were controlled at 10, 1, and 0.2 g/L, accumulated propionic acid concentrations and specific enzyme activities were 18.5, 4.4, and 0.6 g/L and 2.9, 5.7, and 7.1 U/mg protein, respectively. The addition of various concentrations of sodium propionate to the growth medium in batch cultures resulted in a drastic decrease in the growth rate with respect to propionate concentration. The propionic acid was shown to be responsible for cell growth inhibition and enzyme activity reduction in fed-batch culture. (c) 1992 John Wiley & Sons, Inc.     

Phytase production by high cell density culture of recombinant Bacillus subtilis

Bacillus subtilis BD170, harboring a plasmid pGT44[phyC] carrying the phytase gene (phyC) and a phosphate-depletion inducible pst-promoter, was grown in a 2 l bioreactor. Using a controlled feeding of glucose, high cell densities of 32 and 56 g dry cell weight l^–1 were achieved with peptone and yeast extract, respectively, as the complex nitrogen sources in a semi-defined growth medium. The fed-batch protocol was applied to production of recombinant phytase and a high extracellular phytase activity (48 U ml^–1) was reached with peptone. Although the yeast extract feeding resulted in a higher cell density, it was unsuitable as a medium component for phytase expression due to its relatively high phosphate content.     

侧孢短芽胞杆菌产生线虫侵染性蛋白酶的优化

采用单因素试验确定侧孢短芽胞杆菌G4产线虫侵染性蛋白酶的最佳碳氮源,通过Placket-Burman设计筛选影响蛋白酶活力的主效因子,最陡坡试验和Box-Behnken设计获得主效因子的最佳水平,建立线虫侵染性蛋白酶的最佳生产体系:葡萄糖9.78 g/L、牛肉膏16.65 g/L、磷酸氢二钾0.75 g/L、可溶性淀粉12.5 g/L、氯化钠0.75 g/L、硫酸镁0.5 g/L、初始pH值自然、装液量50 mL,37℃摇瓶培养32 h,蛋白酶活力可达12 379.41 U/mL,较优化前的2 476.3 U/mL提高了4倍。     

A procedure for high-yield spore production by Bacillus subtilis

Bacillus subtilis spores have a number of potential applications, which include their use as probiotics and competitive exclusion agents to control zoonotic pathogens in animal production. The effect of cultivation conditions on Bacillus subtilis growth and sporulation was investigated in batch bioreactions performed at a 2-L scale. Studies of the cultivation conditions (pH, dissolved oxygen concentration, and media composition) led to an increase of the maximum concentration of vegetative cell from 2.6 x 10(9) to 2.2 x 10(10) cells mL(-)(1) and the spore concentration from 4.2 x 10(8) to 5.6 x 10(9) spores mL(-)(1). A fed-batch bioprocess was developed with the addition of a nutrient feeding solution using an exponential feeding profile obtained from the mass balance equations. Using the developed feeding profile, starting at the middle of the exponential growth phase and finishing in the late exponential phase, an increase of the maximum vegetative cell concentration and spore concentration up to 3.6 x 10(10) cells mL(-)(1) and 7.4 x 10(9) spores mL(-)(1), respectively, was obtained. Using the developed fed-batch bioreaction a 14-fold increase in the concentration of the vegetative cells was achieved. Moreover, the efficiency of sporulation under fed-batch bioreaction was 21%, which permitted a 19-fold increase in the final spore concentration, to a final value of 7.4 x 10(9) spores mL(-)(1). This represents a 3-fold increase relative to the highest reported value for Bacillus subtilis spore production.     

Enhanced amylase production by Bacillus subtilis using a dual exponential feeding strategy

A recombinant Bacillus subtilis strain (ATCC 31784) haboring the plasmid pC194 with a thermostable -amylase gene was cultured in a 22-l B. Braun Biostat C fermenter. Traditional batch operations suffer from low cell mass and protein productions because a high initial glucose concentration causes substrate inhibition and also product inhibition due to acetate accumulation. An exponential fed-batch strategy to prevent these inhibitions was developed in this work. The host strain is auxotrophic for phenylalanine, tyrosine and tryptophan. Due to low solubilities of tyrosine and tryptophan in the feed stream, tyrosine and tryptophan were dissolved separately in ammonia water to form a second feed stream. By dual feeding both streams at different exponential feed rates, a high cell density of 17.6 g/l and a final -amylase activity of 41.4 U/ml and the overall biomass yield of 0.39 g cell/g glucose were achieved.     

强化底物利用酶系表达,提升地衣芽孢杆菌生产碱性蛋白酶性能

地衣芽孢杆菌2709由于易于培养、GRAS状态和完善的蛋白质分泌能力,是已经投入工业生产碱性蛋白酶的菌株.为改善该菌株的发酵生产性能,提高菌体对培养基成分的利用和碱性蛋白酶产量,对菌株的胞外分泌酶系进行完善.利用同源重组机制,在基因组复制起始位点附近引入了来源于短小芽孢杆菌的木聚糖酶基因xynA和在复制起始位点中心对称...     

流加发酵对重组Bacillus subtilis发酵生产角质酶的影响

为实现基因工程菌Bacillus subtilis WSHB06-07生产角质酶的高产,在3L发酵罐中考察了不同初糖浓度对菌体生长和产酶的影响,并在选择38 g/L初始蔗糖浓度的基础上,进行碳源的分批流加和恒速流加,结果表明发酵16 h开始流加碳源,采用总补糖量60g/L,蔗糖平均流速为4g/(L·h)的恒速补料方式,角质酶酶活在31h可达到最大545.87U/ml,比分批发酵酶活提高67.8%,并获得较高的角质酶生产强度,满足工业化生产要求。     

Protease production by Bacillus subtilis in oxygen-controlled,glucose fed-batch fermentations

Summary An open-loop, on-off control system using the dissolved oxygen level to control a glucose feed was used in a study of growth and production of protease by Bacillus subtilis CNIB 8054. With this system, both glucose and oxygen were controlled at low concentrations. In batch fermentations, protease activity in the fermentation broth was maximum when growth had stopped. During oxygen-controlled, glucose fed-batch fermentations, growth and the production of protease activity continued during glucose feeding. Oxygen-controlled, glucose fed-batch fermentations produced more protease activity than batch fermentations, depending upon the set point for dissolved oxygen. These results indicate that control of glucose and oxygen concentrations can result in improvements in protease production.     

Use of fed-batch cultivation for achieving high cell densities for the pilot-scale production of a recombinant protein (phenylalanine dehydrogenase) in Escherichia coli

A fed-batch process for the high cell density cultivation of E. coli TG1 and the production of the recombinant protein phenylalanine dehydrogenase (PheDH) was developed. A model based on Monod kinetics with overflow metabolism and incorporating acetate utilization kinetics was used to generate simulations that describe cell growth, acetate production and reconsumption, and glucose consumption during fed-batch cultivation. Using these simulations a predetermined feeding profile was elaborated that would maintain carbon-limited growth at a growth rate below the critical growth rate for acetate formation (mu < mu(crit)). Two starvation periods are incorporated into the feed profile in order to induce acetate utilization. Cell concentrations of 53 g dry cell weight (DCW)/L were obtained with a final intracellular product concentration of recombinant protein corresponding to approximately 38% of the total cell protein. The yield of PheDH was 129 U/mL with a specific activity of 1.2 U/mg DCW and a maximum product formation rate of 0.41 U/mg DCW x h. The concentration of aectate was maintained below growth inhibitory levels until 3 h before the end of the fermentation when the concentration reached a maximum of 10.7 g/L due to IPTG induction of the recombinant protein.     

Characterization of Proteinases Excreted by Bacillus subtilis Marburg Strain during Sporulation

S ummary . This study has characterized 3 proteolytic enzymes during sporulation by Bacillus subtilis Marburg strain when grown in nutrient broth. A method of purification is described which permits the separation of 2 different proteinases: one belonging to the metal enzyme group and the other to the serine enzyme group. The third enzyme, probably an esterase, showed a high esterolytic activity, but only low proteolytic activity. Determination of the 3 enzymes in a mixture was accomplished by using specific substrates and inhibitors. They were excreted simultaneously between the end of the growth phase until the appearance of the prespores. During this entire period, 20% of the total proteolytic activity was due to the metal proteinase; 80% of the proteolytic activity and 15% of the esterolytic activity was due to the serine proteinase; 85% of the esterolytic activity was the result of the esterase. These findings will contribute to a more complete phenotypic characterization of those mutants of sporulation that appear to be involved in the production of extracellular hydrolytic enzymes.     

Degradation of African locust bean oil by Bacillus subtilis and Bacillus pumilus isolated from soumbala,a fermented African locust bean condiment

AIMS: To investigate predominant isolates of Bacillus subtilis and B. pumilus in soumbala, a fermented African locust bean condiment, for their ability to degrade African locust bean oil (ALBO). METHODS AND RESULTS: Agar diffusion test in tributyrin and ALBO agar was used for screening of the isolates for esterase and lipase activity, respectively. The quantity and the profile of free fatty acids (FFA) during 72 h of degradation of ALBO by the Bacillus isolates were studied by titration and gas chromatography. The degradation of tributyrin and ALBO was variable among the isolates. Two strains of B. subtilis and two strains of B. pumilus showed significantly higher esterase and lipolytic activities than the others. The degradation ALBO was most pronounced in enriched nutrient agar except for one isolate of B. pumilus degrading ALBO to the same extent regardless of the enrichment. The quantity of FFA released from ALBO by the most lipolytic strains of Bacillus increased mainly between 0 and 24 h and differed among the isolates. The profile of FFA was similar for the Bacillus isolates with oleic acid (C18:2) occurring as the major FFA in all the samples except in samples incubated with B. subtilis B9 where stearic acid (C18) was dominant. CONCLUSION: Bacillus isolates from soumbala showed high strain dependent lipolytic activity against ALBO. SIGNIFICANCE AND IMPACT OF THE STUDY: This study contributes to the selection of Bacillus strains to be used as starter cultures for controlled production of soumbala.     

Kinetics of alpha-amylase synthesis from Bacillus amyloliquefaciens

The microbial production of alpha-amylase from Bacillus amyloliquefaciens was investigated. The microorganism was grown using media containing glucose or maltose at 37 degrees C and under aerobic conditions in a 16-L fermentor. The alpha-amylase synthesis from maltose was not found to be inducible but was found to be subject to catabolite repression. The maltose uptake rate was observed to be the rate-limiting step compared to the conversion rate of maltose to glucose by intracellular alpha-glucosidase. The alpha-amylase activity achieved with maltose as a substrate was higher than that achieved with glucose. A slower growth rate and a higher cell density were obtained with maltose. The enzyme production pattern depended upon the nutrient composition of the medium.     

普鲁兰酶基因在解淀粉芽孢杆菌BF7658菌株中的分泌表达

根据文献报道的核苷酸序列合成Bacillus deramificans普鲁兰酶成熟肽编码基因BdP。将BdP基因插入芽孢杆菌分泌表达载体pUC980信号肽编码区下游,获得重组质粒pUC980-BdP,重组质粒转化中温α-淀粉酶生产菌解淀粉芽孢杆菌BF7658菌株。摇瓶发酵实验表明,重组转化子发酵液有明显普鲁兰酶酶活,约48h酶活达到最高水平,为2．8ASPU／mL。酶学性质分析表明,重组酶最适作用温度约为60℃,最适反应pH为5．0,60℃保温3h仍保存50％的活性。重组酶性质适合淀粉糖化工艺的要求。