表达酿酒酵母ALAS的重组大肠杆菌胞外5-氨基乙酰丙酸的产量和纯化

5-氨基乙酰丙酸(5-aminolevulinate,ALA)由5-氨基乙酰丙酸合酶(5-aminolevulinate synthase,ALAS)催化产生。利用重组细菌在大肠杆菌合成ALA已有不少研究。重组真核生物ALAS在大肠杆菌合成ALA的研究没有报道。酿酒酵母ALAS在大肠杆菌重组表达,在摇瓶培养条件下,分析了胞外ALA的产量,重组菌的生长状况和细胞中ALAS的活性,利用两种国产树脂纯化ALA,毛细管电泳分析确定ALA纯度在LB培养基中,初始pH6.5,含有20mmol/L的酮戊酸、20mmol/L琥珀酸和20mmol/L的甘氨酸,37℃下诱导培养12h,胞外ALA的产量为162mg/L培养基。纯化的ALA纯度达到90%。     

表达浑球红细菌hemA基因生产5-氨基乙酰丙酸的研究

5-氨基乙酰丙酸（5-aminolevulinate acid,ALA）在农业,工业,医药业具有广泛的应用。ALA由5-氨基乙酰丙酸合酶（5-aminolevulinate acid synthase, ALAS）催化产生,其生物合成受终产物血红素的反馈抑制。本研究克隆一种浑球红细菌的hemA基因,序列分析其与已报道的基因具有96％的同源性,蛋白质编码区域也发生改变,并利用生物信息学软件进行同源关系的分析。采用大肠杆菌重组技术,构建表达载体pET28a—hemA,表达了有活性的浑球红细菌（Rhodobacter sphaeroides）的ALAS,研究了IPTG诱导和PH对研究ALAS的影响,同时分析了重组菌株合成ALA的能力,测定胞外产量。结果表明,在PH6．5,30mmol／L琥珀酸和60mmol／L甘氨酸培养条件下,胞外ALA的最大合成量达到669mg／L。     

微生物发酵生产5-氨基乙酰丙酸研究进展

5-氨基乙酰丙酸是生物体内吡咯生物合成途径的关键中间产物,具有广泛的应用前景。文中从三方面归纳了国内外关于5-氨基乙酰丙酸的最新研究进展:生产5-氨基乙酰丙酸的微生物筛选分离与诱变;基于C4途径的微生物全细胞生物转化合成5-氨基乙酰丙酸;基于微生物代谢工程改造构建高产5-氨基乙酰丙酸的工程菌株。最后,预测了未来5-氨基乙酰丙酸的研究方向和焦点。     

表达酿酒酵母ALAS的重组大肠杆菌胞外5-氨基乙酰丙酸的产量和纯化

5-氨基乙酰丙酸（5-aminolevulinate,ALA）由5-氨基乙酰丙酸合酶（5-aminolevulinate synthase,ALAS）催化产生。利用重组细菌在大肠杆菌合成ALA已有不少研究。重组真核生物ALAS在大肠杆菌合成ALA的研究没有报道。酿酒酵母ALAS在大肠杆菌重组表达,在摇瓶培养条件下,分析了胞外ALA的产量,重组菌的生长状况和细胞中ALAS的活性,利用两种国产树脂纯化ALA,毛细管电泳分析确定ALA纯度在LB培养基中,初始pH 6.5,含有20mmol/L的酮戊酸、20mmol/L琥珀酸和20mmol/L的甘氨酸,37℃下诱导培养12h,胞外ALA的产量为162mg /L培养基。纯化的ALA纯度达到90%。     

重组球形红细菌5-氨基乙酰丙酸合酶同工酶hemA和hemT的特性

将编码光合细菌Rhodobactersphaeroides 5- 氨基乙酰丙酸合酶(ALAS)的同工酶基因hemA、hemT转入E .coli中进行高表达,并将高表达的同工酶进行分离、纯化.纯化的hemA是可溶的,并具有催化活性,而hemT大部分是不溶的,且在体外条件下无活性.与其它重组ALAS相比,R .sphaeroides的hemA活性表达需PLP作为催化因子,除去PLP或用硼酸钠破坏与PLP的连接,hemA活性下降90 % .hemA PLP的紫外 可见光谱分析表明hemA与PLP之间形成一个醛亚胺键,而hemT与PLP之间未形成该键.hemA对修饰组氨酸、精氨酸、胱氨酸残基的试剂很敏感,对可切割Arg15 1和Ser15 2的类胰蛋白酶也很敏感,PLP也不能阻止该酶的切割作用.抗血清试验表明,hemA、hemT的抗血清均可与小鼠的ALAS杂交,并都有一个抗原决定簇.     

琥珀酸脱氢酶或琥珀酰辅酶A合成酶缺失促进大肠杆菌积累5-氨基乙酰丙酸

5-氨基乙酰丙酸 (ALA) 是生物体内四吡咯类化合物的合成前体,在农业及医药领域应用广泛,是极具开发价值的高附加值生物基化学品。目前利用外源C4途径的重组大肠杆菌发酵生产ALA的研究主要利用LB培养基并添加葡萄糖和琥珀酸、甘氨酸等合成前体,成本较高。琥珀酸在C4途径中以琥珀酰辅酶A的形式直接参与ALA的合成。文中在以葡萄糖为主要碳源的无机盐培养基中研究了琥珀酰辅酶A下游代谢途径琥珀酸脱氢酶编码基因sdhAB和琥珀酰辅酶A合成酶编码基因sucCD缺失对ALA积累的影响。与仅表达异源ALA合成酶的对照菌株相比,sdhAB和sucCD缺失菌株ALA的产量分别提高了25.59%和12.40%,且ALA的积累不依赖于琥珀酸的添加和LB培养基的使用,从而大幅降低了生产成本,显示出良好的工业应用前景。     

提高类球红细菌5-氨基乙酰丙酸产率的措施

5-氨基乙酰丙酸是四吡咯化合物生物合成的必需前体物,它作为一种无公害的绿色除草剂、杀虫剂、植物生长促进剂以及治疗癌症的药物而受到广泛的关注。文章综述了类球红细菌5-氨基乙酰丙酸的发酵生产现状以及提高其发酵产率的策略与措施。     

不同流加发酵方式对重组大肠杆菌细胞外Hegf表达水平的影响

人表皮生长因子 (ｈＥＧＦ)是由 5 3个氨基酸组成的单链多肽 ,内有 3个二硫键。它具有多种重要的生物学功能 ,能够促进表皮细胞的生长繁殖 ,加速皮肤和角膜创伤的修复 ,加速胃溃疡的治疗和抑制胃酸的分泌 ,具有广阔的医疗应用前景[1 ] 。最近又发现ｈＥＧＦ在化妆品产业中有潜在的重大应用[2 ] 。这些都促进了人们试图采用基因工程技术大规模地生产ｈＥＧＦ。1982年Ｓｍｉｔｈ等人首先在Ｅ .ｃｏｌｉ中以融合蛋白形式实现了ｈＥＧＦ的表达[3 ] ,随后在枯草杆菌和酵母菌中亦相继实现了表达[4] 。由于ｈＥＧＦ在酵母菌中表达水平很低 ,大肠杆…     

光合细菌利用工业有机废水产生5-氨基乙酰丙酸

[目的]利用本实验室筛选的5-氨基乙酰丙酸(5-aminolevulinic acid,ALA)高产紫色非硫红假单胞菌株,以味精、柠檬酸、啤酒和豆制品生产废水作为底物,进行光合细菌利用废水产生ALA并去除化学需氧量(CODcr)的研究.[方法]光合细菌培养温度为30℃,光照强度为3000 Lux,进行乙酰丙酸、甘氨酸、琥珀酸的添加与否和废水灭菌与否的处理,用比色法测定菌液光密度,ALA检测采用Ehrlich'S试剂分光光度检测法.[结果]在不添加乙酰丙酸(levulinic acid,LA)、甘氨酸和琥珀酸的条件下,菌株99-28的菌体生长在72～96 h达到稳定期,ALA产量在96h最高,在4种废水中,味精废水的ALA产量最高,CODcr去除率也最高;添加LA、甘氨酸和琥珀酸显著提高ALA产量,但CODcr去除效果不好.废水不灭菌略微降低99-28菌株的生长和CODcr的去除能力,在添加LA、甘氨酸和琥珀酸的条件下的,ALA产量明显下降.ALA高产突变菌株L-1在有机废水中的生长状况、对有机废水的CODcr去除与菌株99-28表现一致,在不添加和添加LA、甘氨酸和琥珀酸的条件下,突变株L-1的ALA产量明显比菌株99-28高.[结论]本实验室筛选的紫色非硫红假单胞菌株能利用有机废水作为底物产生ALA并降解CODcr.     

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。     

大肠杆菌K5产肝素前体heparosan的研究进展

肝素是一种被广泛临床应用的抗凝血药物多糖。Heparosan是某些细菌荚膜中的GAG成分,其二糖骨架结构与脊椎动物中的肝素类似,可以作为肝素和硫酸乙酰肝素的生物合成前体。本文综述了肝素及肝素前体heparosan的功能与应用,heparosan在大肠杆菌K5中合成转运相关酶的研究,以及发酵法生产heparosan的研究进展,并对其应用前景进行了展望。     

Temperature gradient-based high-cell density fed-batch fermentation for the production of pyruvate oxidase by recombinant E. coli

Pyruvate oxidase (PyOD) is a very powerful enzyme for clinical diagnostic applications and environmental monitoring. Influences of temperature on cell growth, plasmid stability, and PyOD expression during the PyOD fermentation process by recombinant Escherichia coli were investigated. Based on the influences of temperature on the physiological metabolism, a novel high-cell density fed-batch cultivation with gradient temperature decrease strategy for effective PyOD production was achieved, under which the biomass (OD₆₀₀) of recombinant E. coli could reach to 71 and the highest PyOD activity in broth could reach to 3,307 U/L in 26?hr fermentation.     

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。     

Optimization of extracellular 5-aminolevulinic acid production from Escherichia coli transformed with ALA synthase gene of Bradyrhizobium japonicum

Extracellular accumulation of 5-aminolevulinic acid (ALA) by an E. coli overexpressing ALA synthase (ALAS) was achieved by inserting a hemA gene from Bradyrhizobium japonicum and expressed under the control of T7 promoter. At pH 7.0 extracellular ALA reached up to 15 mM in a jar fermenter with an addition of glycine (30 mM) and succinate (90 mM) in the medium. ALA accumulation was increased to 20 mM by adding levulinic acid (30 mM) to the cultures.     

重组大肠杆菌合成左旋多巴条件的优化

通过对合成体系各组分对产物形成的影响的研究。分别求得了底物邻苯二酚,丙酮酸及乙酸氨的表观米氏常数,表观底物抑制常数和最适底物浓度,并得出合成左旋多巴的最适反应体系为：1%丙酮酸,1.2%邻苯二酚,2%乙酸铵,0.1?TA,0.2%亚硫酸钠,用氨水调pH至8.0。加入从与合成体系等体积培养液中收获的重组大肠杆菌细胞,于15℃反应16h,L-DOPA的产量为15.36g/L。     

Metabolic oscillations in an E. coli fermentation

Recombinant E. coli fermentations were observed to undergo regular, reproducible oscillations in oxygen uptake for several hours during a controlled fermentation process. Culture growth slowed during the period of oscillations, delaying induction of recombinant protein production. The oscillations were similar in 10-L and 1,000-L fermentors and also occurred with different feed control algorithms. Both observations support the hypothesis that the oscillations are metabolic in nature. Analysis of amino acid, ATP, and GTP pools suggests that the oscillations result from aberrant regulation of isoleucine biosynthesis leading to repeated starvation events in which protein synthesis and growth are impaired. Both a nutritional solution, isoleucine feeding, and a genetic solution, repair of an ilvG frameshift mutation in E. coli K-12 strains, were found to eliminate the oscillations, further supporting the proposed mechanism for the behavior. These results illustrate the interesting and complicated physiological behavior which can be displayed in metabolic networks and provide another example of surprising problems that can arise in growing recombinant organisms in fermentors.     

Production of poly(4-hydroxybutyric acid) by fed-batch cultures of recombinant strains of Escherichia coli

A recombinant strain of Escherichia coli was used to produce poly(4-hydroxybutyric acid), P(4HB), homopolyester by fed-batch culture in M9 mineral salts medium containing glucose and 4-hydroxybutyric acid as carbon sources. The final cell dry weight, P(4HB) concentration and P(4HB) content were 12.6 g/l, 4.4 g/l, and 36% of cell dry weight, respectively, in a 27-l stirred and aerated fermenter after 60 h of fed-batch fermentation at constant pH.     

Fed-batch operation of recombinant Escherichia coli containing trp promoter with controlled specific growth rate

A feb-batch operation for the production of bovine somatotropin (bST) under the control of tryptophan promoter in Escherichia coli was investigated. The plasmid used contains a two-cistron system and altered codon usage for higher expression of bST. Specific growth rate is an important parameter in the fermentation, because it affects the production of growth-inhibitory organic acids and the expression of recombinant protein. The feeding rate was adjusted to keep the specific growth rate constant in this study. The variable growth yield expressed as a function of time was used for the calculation of the feeding rate. The growth yield decreases during the fermentation as product expression is induced. The specific growth rate was well controlled; however, intracellular bST concentration decreased at high cell concentrations. This is considered to be due to degradation by proteases. The decrease was prevented by an exponential feeding of the yeast extract as an organic nitrogen source. (c) 1994 John Wiley & Sons, Inc.