Production of Penicillin G acylase from Bacillus sp.: Effect of medium components

A Bacillus sp. producing a high level of intracellular penicillin G acylase (PAC) was isolated. The PAC production in this strain was induced by phenylacetic acid. Various carbon and nitrogen sources were evaluated for their effect on growth and PAC production at 28 °C and pH 7.0. Cells grown in medium supplemented with sucrose as carbon source and tryptone as nitrogen source produced maximum activity of 6.45 and 8.92 U mg^–1, respectively. Maximum concentration of PAC (10.1 Umg^–1) was produced by the cells grown in the medium containing sucrose and tryptone, which was twofold higher than the production in basal medium.     

Optimization of a culture medium for xylanase production by Bacillus sp. using statistical experimental designs

The concentrations of oat spelt xylan, casein hydrolysate and NH4Cl in the culture medium for production of xylanase from Bacillus sp. I-1018 were optimized by means of response surface methods. The path of steepest ascent was used to approach the optimal region of the medium composition. The optimum composition of the nutrient medium was then easily determined by using a central composite design and was found to be 3.16g/l of xylan, 1.94g/l casein hydrolysate, 0.8g/l of NH4Cl. The xylanase production was increased by 135% when the strain was grown in the optimized medium compared to initial medium.     

Optimization of a culture medium for xylanase production by Bacillus sp. using statistical experimental designs

The concentrations of oat spelt xylan, casein hydrolysate and NH4Cl in the culture medium for production of xylanase from Bacillus sp. I-1018 were optimized by means of response surface methods. The path of steepest ascent was used to approach the optimal region of the medium composition. The optimum composition of the nutrient medium was then easily determined by using a central composite design and was found to be 3.16g/l of xylan, 1.94g/l casein hydrolysate, 0.8g/l of NH4Cl. The xylanase production was increased by 135% when the strain was grown in the optimized medium compared to initial medium.     

解淀粉芽胞杆菌PC2产抑菌物质培养基及发酵条件优化

【目的】优化解淀粉芽胞杆菌PC2产抑菌活性物质发酵培养基及发酵条件。【方法】以马铃薯葡萄糖液体培养基为基础,依据发酵液对金黄色葡萄球菌抑菌圈的单因素试验结果,采用Box-Behnken响应面法优化发酵培养基,二次通用旋转组合设计,频率分析法优化发酵条件。【结果】影响发酵液抑菌活性的培养基主要组分为马铃薯、蔗糖和L-谷氨酸钠,最优发酵培养基配方为:马铃薯188.0 g/L,蔗糖22.0 g/L,L-谷氨酸钠1.80 g/L,培养基成本为0.81元/L;最佳发酵条件为:接种量6%、发酵温度30°C、装液量40 mL/250 mL、摇床转速185 r/min、发酵时间24 h、初始pH 7.0。优化后发酵液对金黄色葡萄球菌抑菌圈直径为30.82 mm,较优化前的18.22 mm增加了12.60 mm。【结论】优化后的培养基和发酵条件提高了解淀粉芽胞杆菌PC2发酵液的抑菌活性,为该菌株的工业化生产应用提供了依据。     

高产青霉素酰化酶巨大芽胞杆菌的诱变选育及产酶条件优化

【目的】选育高产青霉素G酰化酶(PGA)工业菌株。【方法】采用LiCl-紫外线复合诱变以及常压室温等离子体(ARTP)诱变技术对巨大芽胞杆菌(Bacillus megaterium) ATCC 14945进行处理。处理菌体涂平板后,将长出的菌落接种到液体培养基中,向培养6 h后的二代菌液中添加终浓度为0.1%的苯乙酸,28 °C、250 r/min条件下诱导培养40 h。对离心后获得的上清(粗酶液)采用NIPAB法测定PGA酶活力。以PGA酶活力最高的菌株为材料,对苯乙酸最佳添加量和最佳诱导时间进行优化,采用NIPAB法测定PGA酶活力。采用SDS-PAGE检测诱变前后巨大芽胞杆菌粗酶液中PGA的蛋白特性。【结果】从诱变菌落中筛选到PGA酶活力为39.60 U/mL的菌株12-4,酶活力比出发菌株提高了8.5倍。该菌株在液体培养6 h后添加终浓度为0.2%的苯乙酸,继续培养50 h后,PGA酶活力可达78.45 U/mL,比出发菌株提高了16.8倍。诱变前后菌株培养液中的PGA蛋白均具α、β亚基;诱变后菌株PGA α亚基的量没有明显变化,β亚基的量明显增多;α、β亚基之间的蛋白条带明显增多。【结论】采用诱变技术可提高巨大芽胞杆菌PGA活性,获得的诱变菌株12-4及培养条件对PGA工业化生产具有重要价值。     

重组青霉素G酰化酶在枯草芽孢杆菌中的表达条件优化

 为获得巨大芽孢杆菌青霉素 G酰化酶 (PGA)的高产菌株和条件 ,构建了分泌表达 PGA的基因工程枯草杆菌菌株 ,对表达条件进行了优化 .以 LB作为初始培养基 ,考察了温度、苯乙酸、装液量、碳源对于工程菌 PGA产量的影响 .实验发现重组细胞产酶不再需要变温和苯乙酸诱导 .充足的通气量和适当浓度的淀粉可使细胞密度及 PGA表达量大为提高 .表达条件优化后 ,菌体 A60 0由 3提高到 2 0 ,PGA的表达量由 3～ 6U/ml提高到 35～ 40 U/ml,为目前生产用巨大芽孢杆菌表达量的 6倍 .     

Enhanced production of penicillin G acylase from a recombinant Escherichia coli

Penicillin G acylase (pac) gene was cloned into a stable asd ⁺ vector (pYA292) and expressed in Escherichia coli. This recombinant strain produced 1000 units penicillin G acylase g^–1 cell dry wt, which is 23-fold more than that produced by parental Escherichia coli ATCC11105. This enzyme was purified to 16 units mg^–1 protein by a novel two-step process.     

Optimization of fermentation conditions for production of exopolysaccharide by Bacillus polymyxa

Production of exopolysaccharide (EPS) from a strain of Bacillus polymyxa was studied. Sucrose and potassium nitrate were found to be efficient carbon and nitrogen sources, respectively, for the production of the EPS. EPS production increased with the increase of sucrose concentration, probably due to the facilitated carbon uptake. Optimal pH was 7–8, and a sufficient supply of oxygen was needed for the EPS production. It was noted that the EPS synthesis by this B. polymyxa was growth-associated, indicating that a sufficient supply of nutrients was required for a high production of the EPS. As high as 54?g/l of EPS with a yield of 63% (g EPS/g sucrose) was obtained in 48?h of fed-batch cultivation with intermittent feeding of sucrose and potassium nitrate.     

重组毕赤酵母产青霉素G酰化酶的分批发酵动力学研究

构建了重组毕赤酵母产青霉素G酰化酶的分批发酵动力学模型。实验考察了分批发酵过程中甘油消耗、甲醇浓度、菌体浓度、溶氧、补料时间对青霉素G酰化酶活力的影响。应用Matlab软件,对菌体生长、基质消耗和产物生成方程进行最优参数估算和非线性拟合,得到相应的动力学模型。模型的计算值与实验值能较好地拟合,表明所建模型能较好反映重组毕赤酵母产青霉素G酰化酶的分批发酵过程。     

Development of a low-cost fermentation medium for ethanol production from biomass

Nutrient cost is an important aspect in the fermentation of biomass to ethanol. With a goal of developing a cost-effective fermentation medium, several industrially available nutrient sources were evaluated for their effectiveness in the simultaneous saccharification and fermentation of pretreated poplar with Saccharomyces cerevisiae D₅A. These studies showed that a low-cost medium containing 0.3% corn steep liquor and 2.5 mM MgSO₄ · 7H₂O was similar in performance to a nutrient-rich medium. Besides its low cost, this alternative medium consists of components that are available on a commercial scale, thereby making it industrially relevant. Received: 14 August 1996 / Received revision: 7 January 1997 / Accepted: 24 January 1997     

琥珀酸放线杆菌发酵培养基的优化

对琥珀酸放线杆菌(Actinobacillus succinogenes)CGMCC1593发酵产生琥珀酸培养基的主要成分,及其含量进行优化。通过单因素试验,得出发酵培养基中葡萄糖、酵母膏和玉米浆的含量对产生琥珀酸有显著影响;采用响应面法(RSM),得出多元二次回归方程拟合的三种因素与琥珀酸含量间的函数关系,并根据优化结果与实验,CGMCC1593产琥珀酸达到41.69g/L。     

Optimization of submerged fermentation medium for citrinin-free monascin production by Monascus

Microbial fermentation of citrinin-free Monascus pigments is in favor in the development of food industry. This study investigated the influences of carbon source, nitrogen source, and mineral salts on the cell growth, monascin (MS), and citrinin (CT) production in Monascus M9. A culture medium composition was established for maximizing the production of citrinin-free MS in submerged culture, as follows: 50?g/L Japonica rice powder, 20?g/L NH₄NO₃, 3?g/L NaNO₃, 1.5?g/L KH₂PO₄, 1?g/L MgSO₄?·?7H₂O, 0.2?g/L MnSO₄. Under these conditions, no CT was detectable by high performance liquid chromatography. The yield of MS reached 14.11?mg/g, improving approximately 30% compared with before optimization.     

Biotechnological advances on Penicillin G acylase: Pharmaceutical implications,unique expression mechanism and production strategies

In light of unrestricted use of first-generation penicillins, these antibiotics are now superseded by their semisynthetic counterparts for augmented antibiosis. Traditional penicillin chemistry involves the use of hazardous chemicals and harsh reaction conditions for the production of semisynthetic derivatives and, therefore, is being displaced by the biosynthetic platform using enzymatic transformations. Penicillin G acylase (PGA) is one of the most relevant and widely used biocatalysts for the industrial production of β-lactam semisynthetic antibiotics. Accordingly, considerable genetic and biochemical engineering strategies have been devoted towards PGA applications. This article provides a state-of-the-art review in recent biotechnological advances associated with PGA, particularly in the production technologies with an emphasis on using the Escherichia coli expression platform.     

响应面法优化产酰胺酶发酵培养基

采用响应面分析方法,对阿萨希丝孢酵母（Trichosporon asahii）ZZB-1产酰胺酶的发酵培养基进行了优化。运用单N子试验筛选出麦芽糖和酵母浸膏为最适碳源、氮源,金属离子Ca^2＋、Mn^2＋可提高发酵酰胺酶产量;通过最陡爬坡实验逼近以上4个因子的最大响应区域后,采用Box—Behnken响应面分析法,确定产酰胺酶最佳发酵培养基为麦芽糖18．84g／L、酵母浸膏9．55g／L、NaC15g／L、KH2PO41g／L、MgSO4·7H2O0．2g／L、FeS040．001g／L、CaC0370．84μmol／L、MnS0465．39肚mo[／L（1％丙烯酸诱导）,NH4·H2O调节pH至7．0。培养基优化后酰胺酶产量由初始2554U／L提高到4156U／L,为原始发酵培养基配方酶活产量的1．63倍。     

粘质沙雷氏菌产2,3-丁二醇培养基的优化

研究了各种碳源、氮源、柠檬酸及无机盐对细胞生长与产物形成的影响,通过单因子、正交及中心组合设计响应面分析优化发酵培养基。结果表明在培养基中添加柠檬酸不但可以促进细胞生长与糖耗速度,还可以缩短发酵周期,提高2,3-丁二醇的产量。采用优化后的培养基,2,3-丁二醇的产量由14.03g/L增加到39.27g/L,提高了近3倍。     

Optimization of fermentation medium for amidase production by response surface methodology

采用响应面分析方法,对阿萨希丝孢酵母(Trichosporon asahii)ZZB-1产酰胺酶的发酵培养基进行了优化.运用单因子试验筛选出麦芽糖和酵母浸膏为最适碳源、氮源,金属离子Ca2+、Mn2+可提高发酵酰胺酶产量;通过最陡爬坡实验逼近以上4个因子的最大响应区域后,采用Box-Behnken响应面分析法,确定产酰胺酶最佳发酵培养基为麦芽糖18.84 g/L、酵母浸膏9.55 g/L、NaCl 5g/L、KH2 PO41g/L、MgSO4·7H2O 0.2 g/L、FeSO40.001g/L、CaCO370.84 μmol/L、MnSO4 65.39 μmol/L(1％丙烯酸诱导),NH4·H2O调节pH至7.0.培养基优化后酰胺酶产量由初始2554U/L提高到4156 U/L,为原始发酵培养基配方酶活产量的1.63倍.     

巨大芽孢杆菌青霉素G酰化酶基因在枯草杆菌中的高表达

用ＰＣＲ方法从巨大芽孢杆菌的基因组ＤＮＡ中扩增到青霉素Ｇ酰化酶基因,并装载到枯草杆菌质粒ｐＰＺＷ１０３中,将其转化到枯草杆菌ＤＢ１０４中进行了分泌表达,重组菌株产酶无需苯乙酸诱导。在３７℃培养２４ｈ,菌液酶活力可达６ｕ／ｍｌ。１０天的连续传代实验表明重组菌株的稳定性很高。     

Application of cross-linked enzyme aggregates of Bacillus badius penicillin G acylase for the production of 6-aminopenicillanic acid

AIMS: Optimization of 6-aminopenicillanic acid (6-APA) production using cross-linked enzyme aggregates (CLEA) of Bacillus badius penicillin G acylase (PAC). METHODS AND RESULTS: CLEA-PAC was prepared using purified/partially purified PAC with phenylacetic acid as active-site blocking agent and glutaraldehyde as cross-linker. Conversion of penicillin G to 6-APA by CLEA-PAC was optimized using response surface methodology (RSM) (central composite rotatable design) consisting of a three-factor-two-level pattern with 20 experimental runs. CONCLUSION: Nearly, 80% of immobilization yield was obtained when partially purified enzyme was used for the preparation of CLEA-PAC. Quantitative conversion of penicillin G to 6-APA was observed within 60 min and the CLEA-PAC was reusable for 20 repeated cycles with 100% retention of enzyme activity. SIGNIFICANCE AND IMPACT OF THE STUDY: The faster conversion of penicillin G to 6-APA by CLEA-PAC and efficient reusability holds a strong potential for the industrial application.