天蓝色链霉菌海藻糖合酶的异源表达、活性分析及重组菌全细胞转化合成海藻糖的条件优化

从天蓝色链霉菌Streptomyces coelicolor克隆得到海藻糖合酶基因 (ScTreS),在大肠杆菌Escherichia coli BL21(DE3) 中进行了异源表达,通过 Ni-NTA 亲和柱对表达产物进行分离纯化得到纯酶,经 SDS-PAGE 测定其分子量约为62.3 kDa。研究其酶学性质发现该酶最适温度35 ℃;最适pH 7.0,对酸性条件比较敏感。通过同源建模和序列比对分析,对该基因进行定点突变。突变酶K246A比酶活比野生酶提高了1.43倍,突变酶A165T相对提高了1.39倍,海藻糖转化率分别提高了14%和10%。利用突变体重组菌K246A进行全细胞转化优化海藻糖的合成条件并放大进行5 L罐发酵,结果表明：在麦芽糖浓度300 g/L、初始反应温度和pH分别为35 ℃和7.0的条件下,转化率最高达到71.3%,产量为213.93 g/L;当底物浓度增加到700 g/L时,海藻糖产量仍可达到465.98 g/L。     

昆虫海藻糖及其合成酶基因的特性与功能研究进展

海藻糖广泛存在于细菌、真菌、昆虫、无脊椎动物和植物等大量生物中。它不仅可以作为昆虫的能量来源,而且在抗逆等方面起着重要作用。海藻糖合成酶(Trehalose-6-phosphate synthase,TPS)是海藻糖合成过程中的一个关键酶。目前细菌、真菌和植物中都已经被发现和克隆,但其不存在于哺乳动物中。海藻糖是昆虫的"血糖",主要通过海藻糖合成酶和海藻糖-6-磷酸脂酶(Trehalose-6-phosphate phosphatase,TPP)在脂肪体中催化合成。TPS基因所编码的蛋白序列一般都包含两个保守的结构域:TPS和TPP,分别对应着酵母中的Ots A和Ots B基因。昆虫海藻糖合成酶的基因表达和酶活性的变化与昆虫的多项生理过程有着密切的关系,海藻糖合成酶有可能成为控制害虫的新靶标。     

灰树花海藻糖合成酶基因的克隆及其在大肠杆菌中的表达

海藻糖主要作用是作为生物体的结构组分、以及保护生物膜和保护蛋白质。在灰树花中 ,海藻糖在干重中所占比例最高可达到 1 5 %～ 1 7% ,说明灰树花合成海藻糖的能力很强。将灰树花海藻糖合成酶基因克隆 ,并在大肠杆菌表达系统里表达。表达量为 1 90mg L。通过活性测定 ,证明在大肠杆菌中表达的海藻糖合成酶具有酶活性 ,结合基因工程和酶工程方法 ,为合成海藻糖的研究提供了新的方向     

代谢工程改造大肠杆菌合成己二酸

己二酸是一种具有重要应用价值的二元羧酸,是合成尼龙-66的关键前体。目前,生物法生产己二酸存在生产周期长、生产效率低的问题。本研究选择一株野生型高产琥珀酸菌株大肠杆菌(Escherichia coli) FMME N-2为底盘细胞,首先通过引入逆己二酸降解途径的关键酶,成功构建了可合成0.34 g/L己二酸的E. coli JL00菌株;接着,对合成路径限速酶进行表达优化,使E. coli JL01菌株在摇瓶发酵条件下产量达到0.87 g/L;随后,通过敲除sucD基因、过表达acs基因和突变lpd基因的组合策略平衡己二酸合成前体的供应,优化菌株E. coli JL12己二酸产量进一步提升至1.51 g/L;最后,在5 L发酵罐上对己二酸发酵工艺进行优化。工程菌株经72 h分批补料发酵,己二酸的产量达到22.3 g/L,转化率为0.25 g/g,生产强度为0.31 g/(L·h),具备了一定的应用潜力。本研究可为包括己二酸在内的多种二元羧酸细胞工厂的构建提供理论依据和技术基础。     

大肠杆菌角鲨烯合成途径的构建与调控

角鲨烯因其具有良好的抗氧化功能而被广泛应用于食品、医药、化妆品、工业应用等领域。本实验在大肠杆菌中构建角鲨烯合成途径,通过对其合成途径中关键限速酶(1-脱氧-D-木酮糖-5-磷酸合酶和异戊烯基二磷酸异构酶)过表达的方法进行初步调控,使角鲨烯的产量提升了近三倍。之后采用单因素试验对其发酵培养基和培养条件进行优化,以此来提高角鲨烯的产量。优化发酵条件后,使用最优发酵培养基——TB培养基,在最佳发酵条件:37℃,220r/min培养至OD600约为1.2时加入终浓度为0.1mmol/L的IPTG诱导剂,25℃条件下诱导48h,角鲨烯产量可达73.88mg/L。     

Pseudomonas putida S1海藻糖合成酶基因在大肠杆菌中的克隆表达

利用PCR和TA克隆方法扩增和克隆得到了恶臭假单胞菌Pseudomonas putida S1的海藻糖合成酶基因treS.对其进行序列分析表明,其编码区含有2067bp,编码含688个氨基酸残基的蛋白质,其核苷酸序列和蛋白质序列与来源于其它假单胞菌属细菌的海藻糖合成酶的序列表现出了较高同源性.将该基因序列与表达载体pQE30T连接,构建重组质粒pQE30T-TS,并将其转化至E.coli M15菌株中.重组菌株经诱导表达后SDS-聚丙烯酰胺凝胶电泳结果显示有明显的分子量约77.5kD的特异蛋白条带出现.经测定酶活力达19U/mL,约是原始菌株P.putida S1的50倍.     

红色亚栖热菌TPS/TPP海藻糖合成途径中相关基因的克隆、表达及功能鉴定

通过构建红色亚栖热菌(Meiothermus ruberCBS-01)的基因组DNA文库,克隆得到该嗜热菌海藻糖合成途径中的磷酸海藻糖合成酶(TPS)和磷酸海藻糖磷酸酯酶(TPP)基因。以pET21a为表达载体,将磷酸海藻糖合成酶和磷酸海藻糖磷酸酯酶在大肠杆菌中进行表达并纯化,利用薄层层析的方法验证了这两个酶的活性。同时,本研究检测了红色亚栖热菌在各种环境压力下细胞内含物成分的变化情况,发现在高渗环境压力的诱导下,该菌会在胞内积累大量的6-磷酸海藻糖,而并非海藻糖,这为进一步研究TPS/TPP和TreS途径在细胞体内的作用奠定了基础。     

重组大肠杆菌全细胞催化合成莱鲍迪苷D

莱鲍迪苷D(Rebaudioside D,RD)是一种稀有具有高甜度的甜菊糖苷类化合物。本文实现了重组大肠杆菌全细胞催化莱鲍迪苷A(Rebaudioside A,RA)合成RD。以水稻c DNA为模板,扩增得到葡萄糖基转移酶基因eugt11,构建了重组菌株E.coli BL21(p ETDuet-eugt11),并成功表达了重组蛋白6His-EUGT11。通过Ni柱亲和层析纯化并在体外酶催化反应表征了其催化活性。将重组菌BL21(p ETDuet-eugt11)应用于催化合成RD研究。探讨了反应体系pH、温度、柠檬酸钠浓度、菌体密度、二价金属离子、二甲苯体积分数、UDPG添加浓度对反应效率的影响。单因素考察结果显示,在菌体密度0.16 g湿细胞/m L反应液,底物RA浓度为1.0 mmol/L,pH 8.0,60 mmol/L柠檬酸钠,1%二甲苯,0.1 mmol/L Zn Cl2,12.0 mmol/L UDPG,反应温度42℃,反应时间24 h的条件下,RD产量为123.6 mg/L(约0.1 mmol/L)。     

海藻糖合酶的分子生物学研究进展

海藻糖合酶能够将麦芽糖转化为海藻糖,在海藻糖的工业生产中具有十分重要的意义。本文从海藻糖合酶的基因克隆、基因工程应用、结构和催化机制的研究以及其在微生物体内的功能等方面讨论了海藻糖合酶的研究进展。     

重组大肠杆菌生产谷胱甘肽发酵条件的研究

研究了重组Ｅ．Ｃｏｌｉ产ＧＳＨ的发酵条件,重点考察了添加酵母膏、前体氨基酸和ＡＴＰ的影响。结果发现,前体氨基酸和ＡＴＰ均能促进胞内ＧＳＨ的积累,若在发酵０ｈ和１２ｈ分别加入２０ｇ／ＬＡＴＰ和９ｍｍｏｌ／Ｌ前体氨基酸,则细胞干重和胞内ＧＳＨ含量可分别比对照提高２４％和１４倍。应用正交试验得出的针对细胞干重和ＧＳＨ总量的最佳组合,最大细胞干重和ＧＳＨ总量比原试验中的最好结果分别提高了１０％和２６％。在分析了该菌对葡萄糖利用情况的基础上,对该菌进行了指数流加培养,２５ｈ细胞干重与发酵液内ＧＳＨ总量分别达到８０ｇ／Ｌ和８８０ｍｇ／Ｌ,比摇瓶最好结果分别提高了８３和４６倍。     

Defined media optimization for growth of recombinant Escherichia coli X90

An optimized, defined minimal medium was developed to support balanced growth of Escherichia coli X90 harboring a recombinant plasmid. Foreign protein expression was repressed in these studies. A pulse injection technique was used to identify the growth responses to nutrients in a chemostat. Once the nutrients essential for growth had been identified, the yield coefficients for individual medium components. These yield coefficients were used to develop an optimized, glucose-limited defined minimal medium that supports balanced cell growth in chemostat culture. The biomass and substrate concentrations follow the Monod chemostat model. The maximum specific growth rate determined in a washout experiment is 0.87 h(-1) for this strain in the optimized medium. the glucose yield factor is 0.42 g DCW/g glucose and the maintenance coefficient is zero in the glucose-limited chemostat culture. (c) 1993 John Wiley & Sons, Inc.     

响应面分析法优化重组大肠杆菌生物合成谷胱甘肽的条件

通过响应面分析法和典型性分析得出重组大肠杆菌酶法合成谷胱甘肽的最优条件:菌体量249 mg/mL,磷酸钾缓冲液145 mmol/L,MgCl243 mmol/L和ATP 34 mmol/L,预测谷胱甘肽最大量为16.50 mmol/L。验证性实验证明在优化条件下,重组大肠杆菌酶法合成谷胱甘肽达16.42 mmol/L。响应面分析还表明,在重组大肠杆菌酶法合成谷胱甘肽各因素中,MgCl2和ATP,以及菌体量与磷酸钾缓冲液之间的交互作用较显著。     

Escherichia coli yjjPB genes encode a succinate transporter important for succinate production

Under anaerobic conditions, Escherichia coli produces succinate from glucose via the reductive tricarboxylic acid cycle. To date, however, no genes encoding succinate exporters have been established in E. coli. Therefore, we attempted to identify genes encoding succinate exporters by screening an E. coli MG1655 genome library. We identified the yjjPB genes as candidates encoding a succinate transporter, which enhanced succinate production in Pantoea ananatis under aerobic conditions. A complementation assay conducted in Corynebacterium glutamicum strain AJ110655ΔsucE1 demonstrated that both YjjP and YjjB are required for the restoration of succinate production. Furthermore, deletion of yjjPB decreased succinate production in E. coli by 70% under anaerobic conditions. Taken together, these results suggest that YjjPB constitutes a succinate transporter in E. coli and that the products of both genes are required for succinate export.     

新型大肠杆菌高效表达载体pHsh的构建与应用

在现代生物学和生物技术研究中,通过基因的重组表达获得目标蛋白是一种应用最广泛的方法。因其培养简单、操作方便、遗传背景清楚、克隆表达系统成熟完善,大肠杆菌表达系统通常是人们表达重组蛋白的首选,而表达载体在重组蛋白的生产中起决定作用。pHsh及其衍生质粒是近年发展起来的新型大肠杆菌表达载体,其调控外源基因表达的原理不同于所有其他表达系统,并且具有表达水平高、成本低廉等特点。介绍大肠杆菌表达系统的组成和常用表达载体,并对由pHsh系列载体组成的Hsh表达体系的构建策略、表达调控机制及其使用方法进行综述。Hsh表达体系的建立和发展有望从一个不同的角度帮助解决基因的重组表达中常见的表达水平低、诱导剂成本高、包涵体形成等问题。     

Polyhydroxyalkanoate production in recombinant Escherichia coli

Abstract The bacterial species Escherichia coli has proven to be a powerful tool in the molecular analysis of polyhydroxyalkanoate (PHA) biosynthesis. In addition, E. coli holds promise as a source for economical PHA production. Using this microorganism, clones have been developed in our laboratory which direct the synthesis of poly-β-hydroxybutyrate (PHB) to levels as high as 95% of the cell dry weight. These clones have been further enhanced by the addition of a genetically mediated lysis system that allows the PHB granules to be released gently and efficiently. This paper describes these developments, as well as the use of an E. coli strain to produce the copolymer poly-(3-hydroxybutyrate- co -3-hydroxyvalerate (PHB- co -3-).     

Optimum melanin production using recombinant Escherichia coli

AIMS: A parametric study was conducted to define optimum conditions to achieve high yields in the conversion of tyrosine to eumelanin (EuMel) using recombinant Escherichia coli. METHODS AND RESULTS: Escherichia coli W3110 (pTrcMutmelA) expressing the tyrosinase coding gene from Rhizobium etli and glucose-mineral media were used to transform tyrosine into EuMel. Batch aerobic fermentor cultures were performed to study the effect of temperature, pH and inducer concentration (isopropyl-D-thio-galactopyranoside) on melanin production. Under optimum conditions, 0.1 mmol l(-1) of isopropyl-D-thio-galactopyranoside, temperature of 30 degrees C, and changing pH from 7.0 to 7.5 during the production phase, a 100% conversion of tyrosine into EuMel is obtained. Furthermore, tyrosine feeding allowed us to obtain the highest level (6 g l(-1)) of EuMel produced by recombinant E. coli reported until now. CONCLUSIONS: The most important factors affecting melanin formation and hence influencing the rate and efficiency in the conversion of tyrosine into EuMel in this system, are the temperature and pH. SIGNIFICANCE AND IMPACT OF THE STUDY: Maximum theoretical yield was obtained using a simple culture process and mineral media to convert tyrosine (a medium value compound) into melanin, a high value compound. The process reported here avoids the use of purified tyrosinase, expensive chemical methods or the cumbersome extraction of this polymer from animal or plant tissues.     

产1，3-丙二醇重组大肠杆菌JM109（pEtac—dhaB—tac—yqhD）的构建

在生物柴油的生产过程中,最高可得到约10％的副产物甘油,副产物甘油的去向将成为生物柴油大规模产业化发展所面临的严峻问题。以生物柴油副产物甘油为原料耦合生产1,3-丙二醇,不仅解决了生物柴油副产物甘油的出路问题,同时降低了1,3-丙二醇的生产成本。本研究在前期工作的基础上,分别获得了来源于肺炎克雷伯氏茵的甘油脱水酶编码基因dhaB和来源于大肠杆菌的1,3-PD氧化还原酶同工酶编码基因yqhD,利用表达载体pEtac串联构建了重组质粒pEtac—dhaB—tac—yqhD,将其转化大肠杆菌得到产1,3-丙二醇重组大肠杆菌JM109（pEtac—dhaB-tac—yqhD）,降低了代谢中间产物3-羟基丙醛的积累,提高了1,3-丙二醇的产量。     

Practical protocols for production of very high yields of recombinant proteins using Escherichia coli

The gram‐negative bacterium Escherichia coli offers a mean for rapid, high yield, and economical production of recombinant proteins. However, high‐level production of functional eukaryotic proteins in E. coli may not be a routine matter, sometimes it is quite challenging. Techniques to optimize heterologous protein overproduction in E. coli have been explored for host strain selection, plasmid copy numbers, promoter selection, mRNA stability, and codon usage, significantly enhancing the yields of the foreign eukaryotic proteins. We have been working on optimizations of bacterial expression conditions and media with a focus on achieving very high cell density for high‐level production of eukaryotic proteins. Two high‐cell‐density bacterial expression methods have been explored, including an autoinduction introduced by Studier (Protein Expr Purif 2005;41:207–234) recently and a high‐cell‐density IPTG‐induction method described in this study, to achieve a cell‐density OD₆₀₀ of 10–20 in the normal laboratory setting using a regular incubator shaker. Several practical protocols have been implemented with these high‐cell‐density expression methods to ensure a very high yield of recombinant protein production. With our methods and protocols, we routinely obtain 14–25 mg of NMR triple‐labeled proteins and 17–34 mg of unlabeled proteins from a 50‐mL cell culture for all seven proteins we tested. Such a high protein yield used the same DNA constructs, bacterial strains, and a regular incubator shaker and no fermentor is necessary. More importantly, these methods allow us to consistently obtain such a high yield of recombinant proteins using E. coli expression.