重组大肠杆菌的高密度发酵和甘油生产条件的初步研究

在摇瓶中进行重组大肠杆菌菌株BL21高密度发酵条件的研究,考察了葡萄糖浓度、盐离子浓度、温度、接种量、发酵时间等对该菌株生产甘油的影响。初步确定底物浓度为2.5%,盐离子浓度0.2%,温度为37℃,接种量为2%,经24h的摇瓶发酵,甘油产量最高达6.8g/L。在30L发酵罐实验中、按初步确定的优化条件发酵26h,甘油产量可达46.67g/L,是LB/葡萄糖培养基中甘油产量的2.06倍。     

重组大肠杆菌高密度发酵生产RGD-TRAIL的条件优化

本文以一株产RGD-TRAIL的重组大肠杆菌为研究对象,在10L发酵罐中考查了诱导温度、pH值、溶氧、流加葡萄糖对重组大肠杆菌生长和RGD-TRAIL蛋白表达的影响。结果表明:诱导温度25℃,pH值控制7.0,溶氧控制30%,以5g·L~(-1)·h~(-1)流速流加葡萄糖最有利于菌体生长和蛋白表达,菌体收率和RGD-TRAIL产量分别达到45.99g·L~(-1)和160.2mg·L~(-1)。     

大肠杆菌发酵生产SOD最佳条件研究

通过对大肠杆菌进行液体发酵培养,用正交实验探索了四种微量元素（Cu^2 ,Zn^2 ,Mn^2 ,Fe^2 )加入量,培养时间,摇床转速和培养温度等对大肠杆菌细胞增养生产SOD的影响,最佳工艺条件为：CuSO450μmol/L,ZnSO430μmol/L,MnSO450μmol/L,FeSO430μmol/L,培养时间14h,摇床转速200r/min,培养温度38℃,产酶量7726IU/g湿菌体。     

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。     

基因重组大肠杆菌表达HrpNEcc蛋白的发酵条件及诱导条件优化

对已构建好的表达HrpNEcc蛋白的工程菌BL21(DE3)/pET30a(+)hrpN Ecc的摇瓶发酵条件及乳糖诱导进行优化, 通过在7L发酵罐中放大发酵实验,以期提高蛋白产量并降低生产成本。在摇瓶中优化的发酵及诱导条件是：5% 的接种量,TB培养基,菌体培养至对数生长前期,添加3g/L外源诱导剂乳糖时,HrpNEcc蛋白产量可达417.60mg/L,比不添加乳糖时提高了36.73%,比用IPTG诱导时提高了16.85%。7L发酵罐中发酵,获得菌体湿重达到57.24g/L（WCW）,可溶性HrpNEcc蛋白产量占细胞总蛋白的50.2%,为3.29 g/L。     

重组大肠杆菌高密度发酵研究进展

重组大肠杆菌的高密度发酵是提高基因工程产品产量的一个非常有铲的手段,是现代发酵工程研究的一个热点。本文就高密度发酵中影响重组大肠杆菌发酵产率的几个因素,包括宿主菌、培养基、培养条件、补料方法以及高密度发酵过程中存在的问题和对策加以讨论,着重探讨了高密度下大肠杆菌产生的有害代副产物－－乙酸的产生机制、抑制作用机理,以及控制乙酸机累的技术方法。     

分批培养时pH和温度对重组大肠杆菌生产谷胱甘肽合成酶系的影响

研究了2．5L罐分批培养时pH和温度对重组大肠杆菌生产谷胱甘肽合成酶系的影响,确定了分批培养时生产谷胱甘肽合成酶系的最佳pH和最佳温度。研究结果表明：在发酵液的pH为7．2和温度为37℃时,谷胱甘肽合成酶系产量和细胞干重达到最大,分别为690．6U／L和3．77g／L。采用变温控制对菌体的生长和谷胱甘肽合成酶系的合成并没有明显的优点。     

重组大肠杆菌高表达高密度发酵研究

大肠杆菌高密度高表达发酵技术是现代发酵工程的重要研究课题,此项技术可以有效地提高大肠杆菌的产量和外源重组蛋白的表达量,该文就影响大肠杆菌高密度发酵的主要因素如宿主菌类型、培养基组成、培养条件、生长抑制物质、补料调控等进行了阐述和讨论。     

用重组大肠杆菌发酵生产人生长激素研究

通过不同培养基、不同糖浓度对重组菌Ｅ．ｃｏｌｉＤＨ１０Ｂ／ｐＩＮⅢＡ３ＨＧＨ的菌体生长与外源蛋白表达量的影响的比较，确定较为合适的培养条件，并对发酵过程中调节ｐＨ的氨水用量与外源蛋白的表达量之间的相关性作探索，得到相关性曲线，从而根据氨水用量了解细菌的生长状况。     

用遗传算法进行重组大肠杆菌发酵动力学的分析

重组大肠杆菌在诱导表达人表皮生长因子的过程促使细菌的生长受到抑制,一部分重组菌丧失了分裂能力,但仍保持着一定的代谢活力,分离成为存活但不能培养的细菌,根据大肠杆菌在表达外源蛋白过程中细胞生理状态的不同将细菌分为三类,提出一个描述诱导表达过程中重组大肠杆菌分离、生长的动力学模型．应用遗传算法对不同底物浓度的细胞生长、分离和产物合成的动力学参数进行了有效地估计,避免了传统算法可能陷于局部最优的问题,模型计算结果与实验结果吻合良好．分离模型在初始糖浓为5-20g/L的范围内可以较好地描述发酵过程中细胞生长、分离和目标产物表达的过程并具有一定的预测能力．     

改造大肠杆菌合成海藻糖途径以高效合成海藻糖

海藻糖是相容性溶质的一种,因其具有多种生物学功能,在食品、化妆品、药品以及器官移植等方面均有很广泛应用。然而近几年生产海藻糖主要集中在使用酶催化的方法,虽然这种方法的转化效率高,但是却存在着副产物的问题,难以得到高纯度的海藻糖产品,严重制约了海藻糖的应用。本文通过基因工程技术在大肠杆菌Escherichia coli中构建了海藻糖高效合成新途径,通过全细胞催化合成海藻糖。利用PCR技术在哈氏噬纤维菌Cytophaga hutchinsonii中克隆获得海藻糖双功能合成酶基因(tpsp),采用E.coli pTac-HisA高效表达载体,实现海藻糖双功能合成酶基因(tpsp)高效表达,利用高效表达菌株进行全细胞催化,将葡萄糖高效转化为海藻糖。结果表明C.hutchinsonii海藻糖合成酶基因(tpsp)在E.coli中成功实现表达,该酶能够在胞内将葡萄糖高效转化为海藻糖,并将其转运到胞外,实现海藻糖的高效率合成,海藻糖的产量提高到1.2 g/L,相对转化率为21%。当将此高产菌株在发酵罐中进行转化时,海藻糖的产量达到13.3 g/L,葡萄糖的相对转化率达到48.6%。采用C.hutchinsonii海藻糖合成酶基因高效表达并且应用于海藻糖全细胞合成催化在国内外尚属首次报道,海藻糖的转化率及产率都已达到文献报道最高水平,本研究为开拓海藻糖生产新技术奠定了基础。     

重组大肠杆菌利用木糖发酵产高纯度L-乳酸

对重组大肠杆菌JH16利用木糖产高纯度的三一乳酸进行研究。通过无氧管驯化EscherwhiacdiJH12菌株得到E．coliJH16,驯化后的菌株茵体浓度提高了31％,乙酸积累减少了43％;在摇瓶中考察不同Mg2＋浓度对EcoliJHl6产三一乳酸的影响,确定最适Mg2＋质量浓度为0．25g/L;EcoEJH16以60g/L木糖为C源,在7L全自动发酵罐中添加0．25g／LMg2＋,乳酸积累量提高了18％,达38．18g/L,乳酸纯度高达95％;E．coliJH16在30g／L木糖和30g／L葡萄糖混合C源中,优先利用葡萄糖,当葡萄糖质量浓度低于1．56g/L后,菌体开始利用木糖进行乳酸发酵,最终得到39g／L乳酸。     

以甘油为底物利用重组大肠杆菌生产聚3-羟基丙酸

【目的】解决前期研究中所构建的以甘油为底物合成聚3-羟基丙酸(P3HP)的代谢途径中存在两个主要的问题——细胞内还原力不平衡和质粒丢失,以提高P3HP的产量。【方法】克隆来源于肺炎克雷伯氏菌的1,3-丙二醇(1,3-PDO)氧化还原酶基因,构建P3HP和1,3-PDO联产的菌株,解决细胞内还原力不平衡的问题。利用自杀性载体系统介导的同源重组技术,将甘油脱水酶及其激活因子的基因整合到大肠杆菌基因组中,提高质粒的稳定性。同时,对发酵条件进行优化。【结果】菌种改造和发酵条件优化显著提高了P3HP产量,在摇瓶条件下到达2.7 g/L,比以前的报道提高2倍,并可同时得到2.4 g/L 1,3-PDO。【结论】该重组大肠杆菌合成P3HP的产量得到提高,具有较好的工业化生产前景。     

利用大肠杆菌工程菌廉价高效生产聚羟基丁酸酯

利用大肠杆菌生产聚羟基脂肪酸酯是近来国际上生物可降解塑料的研究热点,本研究通过对适宜于聚羟基脂肪酸酯生产的大肠杆菌菌株的选择和碳源利用试验,初步确立了大肠杆菌代谢工程改造生产聚羟基脂肪酸酯的基础。并在此基础上,通过对大肠杆菌磷酸烯醇式丙酮酸葡萄糖转移酶系统的改造和工程菌环境诱导系统的应用,解决了大肠杆菌工程菌无法同时利用多种碳源合成聚羟基脂肪酸酯的难题。发酵试验证明,工程化改造的大肠杆菌利用廉价底物在5L发酵罐中分批培养32h后,菌体终浓度能够达到8.24g/L,聚羟基脂肪酸酯占细胞干重的84.6%。     

Improved glutathione production by gene expression in Escherichia coli

AIMS: To improve glutathione (GSH) production in Escherichia coli by different genetic constructions containing GSH genes. METHODS AND RESULTS: GSH production was very low in E. coli by the expression of gshI gene. An increase of GSH production was achieved by the expression of both gshI and gshII genes in E. coli. A higher GSH production, namely 34.8 mg g(-1) wet cell weight, was obtained by simultaneous expression of two copies of gshI gene and one copy of gshII gene. CONCLUSIONS: The simultaneous expression of two copies of gshI gene and one copy of gshII gene resulted in a significant increase in GSH production. SIGNIFICANCE AND IMPACT OF THE STUDY: The expression strategy for GSH production described here can be used to increase gene expression and obtain high production rates in other multienzyme reaction systems.     

Pseudomonas aeruginosa amidase: aggregation in recombinant Escherichia coli

The effect of cultivation parameters such as temperature incubation, IPTG induction and ethanol shock on the production of Pseudomonas aeruginosa amidase (E.C.3.5.1.4) in a recombinant Escherichia coli strain in LB ampicillin culture medium was investigated. The highest yield of soluble amidase, relatively to other proteins, was obtained in the condition at 37°C using 0.40 mM IPTG to induce growth, with ethanol. Our results demonstrate the formation of insoluble aggregates containing amidase, which was biologically active, in all the tested growth conditions. Addition of ethanol at 25°C in the culture medium improved amidase yield, which quantitatively aggregated in a biological active form and exhibited in all conditions an increased specific activity relatively to the soluble form of the enzyme. Non-denaturing solubilization of the aggregated amidase was successfully achieved using L-arginine. The aggregates obtained from conditions at 37°C by FTIR analysis demonstrated a lower content of intermolecular interactions which facilitated the solubilization step applying non-denaturing conditions. The higher interactions exhibited in aggregates obtained at suboptimal conditions compromised the solubilization yield. This work provides an approach for the characterization and solubilization of novel reported biologically active aggregates of this amidase.     

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.