大肠杆菌CMP-唾液酸合成酶最小活性域的研究

比较大肠杆菌与脑膜炎奈瑟氏球菌的CMP－唾液酸合成酶的氨基酸序列,发现大肠杆菌CMP－唾液酸合成酶的保守区域主要位于N－端,其C－末端似乎对其催化活性没有作用。通过PCR方法,对大肠杆菌CMP－唾液酸合成酶的C－末端进行了一系列截短,将得到的产物连接至表达载体pET-15b中,在大肠杆菌BL21（DE3）pLysS中表达。经IPTG诱导,发现从C－末端截去189个氨基酸酶仍有催化活性,说明大肠杆菌CMP－唾液酸合成酶的最小活性域主要集中在N－不端的229个氨基酸。在催化活性的C－端缺失突变合成酶的比活,最适pH及热稳定性发生变化,提示被截去的C－端氨基酸残基虽不直接参与构成酶的催化活性中心,但可影响催化活性域的构象,从而对酶的催化活性与稳定性产生影响。     

过量表达自身hemA基因的重组大肠杆菌发酵生产5-氨基乙酰丙酸的研究

研究了优化重组大肠杆菌产5-氨基乙酰丙酸（ALA）的条件,提高大肠杆菌发酵生产AL气的产量。在测定重组大肠杆菌GT48的生长曲线的基础上,确定诱导时间,优化摇瓶发酵条件。然后,进一步在5L发酵罐上进行间歇和流加发酵研究。摇瓶实验表明,细胞培养最佳初始pH为6．5,最佳诱导时间为稳定期前期,最佳接种量为2％,过高的葡萄糖浓度对细胞生长和产物合成均有一定的抑制作用。在5L发酵罐间歇发酵中,重组菌产ALA能力达到47．8mg／L。采用流加发酵可以进一步将产物产量提高到63．8mg／L。构建的过量表达自身的hemA基因的大肠杆菌具有较高的产ALA能力,通过发酵条件优化和采用流加发酵可以提高AL气产量。     

Glycine to glutamic acid misincorporation observed in a recombinant protein expressed by Escherichia coli cells

A novel amino acid misincorporation, in which the intended glycine (Gly) residues were replaced by a glutamic acid (Glu), was observed in a recombinant protein expressed by Escherichia coli. The misincorporation was identified by peptide mapping and liquid chromatography-tandem mass spectrometric analysis on proteolyzed peptides of the protein and verified using the corresponding synthetic peptides containing the misincorporated residues. Analysis of the distribution of the misincorporated residues and their codon usage shows strong correlation between this misincorporation and the use of rarely used codon within the E. coli expression system. Results in this study suggest that the usage of the rare codon GGA has resulted in a Glu for Gly misincorporation.     

Purification, properties, and genetic location of Escherichia coli cytidine 5'-monophosphate N-acetylneuraminic acid synthetase

N-Acetylneuraminic acid cytidylyltransferase (EC 2.7.7.43) (CMP-NeuAc synthetase) catalyzes the formation of cytidine monophosphate N-acetylneuraminic acid. We have purified CMP-NeuAc synthetase from an Escherichia coli O18:K1 cytoplasmic fraction to apparent homogeneity by ion exchange chromatography and affinity chromatography on CDP-ethanolamine linked to agarose. The enzyme has a specific activity of 2.1 mumol/mg/min and migrates as a single protein and activity band on nondenaturing polyacrylamide gel electrophoresis. The enzyme has a requirement for Mg2+ or Mn2+ and exhibits optimal activity between pH 9.0 and 10. The apparent Michaelis constants for the CTP and NeuAc are 0.31 and 4 mM, respectively. The CTP analogues 5-mercuri-CTP and CTP-2',3'-dialdehyde are inhibitors. The purified CMP-N-acetylneuraminic acid synthetase has a molecular weight of approximately 50,000 on sodium dodecyl sulfate-polyacrylamide gel electrophoresis. The gene encoding CMP-N-acetylneuraminic acid synthetase is located on a 3.3-kilobase HindIII fragment. The purified enzyme appears to be identical to the 50,000 Mr polypeptide encoded by this gene based on insertion mutations that result in the loss of detectable enzymatic activity. The amino-terminal sequence of the purified protein was used to locate the start codon for the CMP-NeuAc synthetase gene. Both the enzyme and the 50,000 Mr polypeptide have the same NH2-terminal amino acid sequence. Antibodies prepared to a peptide derived from the NH2-terminal amino acid sequence bind to purified CMP-NeuAc synthetase.     

重组大肠杆菌右旋糖酐蔗糖酶的纯化及其性质

[目的]研究工程菌E.coli BL21(DE3)/pET28-dexYG产右旋糖酐蔗糖酶的纯化和酶学性质.[方法]工程菌经过IPTG诱导后生产含His-tag融合蛋白的右旋糖酐蔗糖酶,通过硫酸铵沉淀、Ni-NTA亲和层析纯化,得到纯度较高的酶蛋白,并对纯酶进行了酶学性质及动力学研究.[结果]经过SDS-PAGE测得该酶的分子量约为170 kDa,与理论推测值基本相同.以蔗糖为底物,酶促反应的最适温度为25～30℃,最适pH值为5.4,动力学常数Km值为10.43 mmol/L;酶活在pH 5.0～8.0较为稳定,在室温(25 ℃)保藏4天仍有59%的酶活力,4℃保存7周酶活力仅下降一半,但在35℃以上失活很快;Ca2 对催化作用有较大的促进,Mg2 有微弱的促进作用,K 对催化反应无影响,Cu2 的抑制作用最强.其他试剂对重组酶的活性有不同程度的影响,其中SDS抑制作用很强.[结论]研究为重组右旋糖酐蔗糖酶纯酶的获取、得到稳定性好、活性高的酶反应体系及利用该酶进行催化反应和工业化应用提供了重要参数.     

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。     

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。     

Production of p-Aminobenzoic acid by metabolically engineered Escherichia coli

The production of chemical compounds from renewable resources is an important issue in building a sustainable society. In this study, Escherichia coli was metabolically engineered by introducing T7lac promoter-controlled aroF^fbr, pabA, pabB, and pabC genes into the chromosome to overproduce para-aminobenzoic acid (PABA) from glucose. Elevating the copy number of chromosomal P_T7lac-pabA-pabB distinctly increased the PABA titer, indicating that elevation of 4-amino-4-deoxychorismic acid synthesis is a significant factor in PABA production. The introduction of a counterpart derived from Corynebacterium efficiens, pabAB (ce), encoding a fused PabA and PabB protein, resulted in a considerable increase in the PABA titer. The introduction of more than two copies of P_T7lac-pabAB (ce-mod), a codon-optimized pabAB (ce), into the chromosome of a strain that simultaneously overexpressed aroF^fbr and pabC resulted in 5.1?mM PABA from 55.6?mM glucose (yield 9.2%). The generated strain produced 35?mM (4.8?g?L^?1) PABA from 167?mM glucose (yield 21.0%) in fed-batch culture.     

Self-cycling operation increases productivity of recombinant protein in Escherichia coli

Self-cycling fermentation (SCF), a cyclical, semi-continuous process that induces cell synchrony, was incorporated into a recombinant protein production scheme. Escherichia coli CY15050, a lac(-) mutant lysogenized with temperature-sensitive phage λ modified to over-express β-galactosidase, was used as a model system. The production scheme was divided into two de-coupled stages. The host cells were cultured under SCF operation in the first stage before being brought to a second stage where protein production was induced. In the first stage, the host strain demonstrated a stable cycling pattern immediately following the first cycle. This reproducible pattern was maintained over the course of the experiments and a significant degree of cell synchrony was obtained. By growing cells using SCF, productivity increased 50% and production time decreased by 40% compared to a batch culture under similar conditions. In addition, synchronized cultures induced from the end of a SCF cycle displayed shorter lysis times and a more complete culture-wide lysis than unsynchronized cultures. Finally, protein synthesis was influenced by the time at which the lytic phase was induced in the cell life cycle. For example, induction of a synchronized culture immediately prior to cell division resulted in the maximum protein productivity, suggesting protein production can be optimized with respect to the cell life cycle using SCF.     

循环利用重组大肠杆菌细胞转化合成丁二酸

研究了回收丁二酸发酵液中的大肠杆菌进行细胞转化的可行性,以转化率和生产效率为指标,考察了不同菌体浓度、底物浓度、pH调节剂对细胞转化的影响。发酵结果表明大肠杆菌可以在仅含有葡萄糖和pH调节剂的水环境中转化生产丁二酸,并确定了最佳的转化条件为:细胞浓度(OD600)50,底物浓度40g/L,缓冲盐为MgCO3。基于优化好的条件,在7L发酵罐中进行重复批次转化,第1次转化的转化率和生产效率分别达到91%和3.22g/(L·h),第2次转化的生产效率和转化率达到了86%和2.04g/(L·h),第3次转化的转化率和生产效率分别达到了83%和1.82g/(L·h)。     

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.     

Production of free fatty acids from switchgrass using recombinant Escherichia coli

Switchgrass is a promising feedstock to generate fermentable sugars required for the sustainable operation of biorefineries because of their abundant availability, easy cropping system, and high cellulosic content. The objective of this study was to investigate the potentiality of switchgrass as an alternative sugar supplier for free fatty acid (FFA) production using engineered Escherichia coli strains. Recombinant E. coli strains successfully produced FFAs using switchgrass hydrolysates. A total of about 3 g/L FFAs were attained from switchgrass hydrolysates by engineered E. coli strains. Furthermore, overall yield assessments of our bioconversion process showed that 88 and 46% of the theoretical maximal yields of glucose and xylose were attained from raw switchgrass during sugar generation. Additionally, 72% of the theoretical maximum yield of FFAs were achieved from switchgrass hydrolysates by recombinant E. coli during fermentation. These shake‐flask results were successfully scaled up to a laboratory scale bioreactor with a 4 L working volume. This study demonstrated an efficient bioconversion process of switchgrass‐based FFAs using an engineered microbial system for targeting fatty acid production that are secreted into the fermentation broth with associated lower downstream processing costs, which is pertinent to develop an integrated bioconversion process using lignocellulosic biomass. © 2017 American Institute of Chemical Engineers Biotechnol. Prog., 34:91–98, 2018     

Regulation of colominic acid biosynthesis by temperature: role of cytidine 5''-monophosphate N-acetylneuraminic acid synthetase

Synthesis of colominic acid in Escherichia coli K-235 is strictly regulated by temperature. Evidence for the role of cytidine 5′-monophospho-N-acetylneuraminic acid (CMP-Neu5Ac) synthetase in this regulation was obtained by measuring its level in E. coli grown at 20 and 37°C. No activity was found in E. coli grown at 20°C. CMP-Neu5Ac started to be quickly synthesized when bacteria grown at 20°C were transferred to 37°C and was halted when cells grown at 37°C were transferred to 20°C. These findings suggest that temperature regulates the synthesis of this enzyme and therefore the concentration of CMP-Neu5Ac necessary for the biosynthesis of colominic acid.     

重组蛋白在大肠杆菌周间腔的分泌表达

大肠杆菌是用于生产重组蛋白的重要工程宿主菌。但是,要获得足够的正确折叠的蛋白还存在一定的缺陷,其中一种解决此问题的方法就是使重组蛋白分泌到大肠杆菌的周间腔里。在这篇综述中,主要讨论了使重组蛋白分泌表达至大肠杆菌周间腔的近期的研究进展。     

Production of recombinant protein in Escherichia coli cultured in extract from waste product alga,Ulva lactuca

This study examined the potential for waste product alga, Ulva lactuca, to serve as a media component for recombinant protein production in Escherichia coli. To facilitate this investigation, U. lactuca harvested from Jamaica Bay was dried, and nutrients acid extracted for use as a growth media. The E. coli cell line BL21(DE3) was used to assess the effects on growth and production of recombinant green fluorescent protein (GFP). This study showed that media composed of acid extracts without further nutrient addition maintained E. coli growth and recombinant protein production. Extracts made from dried algae lots less than six‐months‐old were able to produce two‐fold more GFP protein than traditional Lysogeny Broth media. © 2014 American Institute of Chemical Engineers Biotechnol. Prog., 30:784–789, 2014     

A single-cell assay of beta-galactosidase in recombinant Escherichia coli using flow cytometry

A flow cytometric method was developed for the assay of beta-galactosidase in single Escherichia coli cells. A new fluorogenic substrate for beta-galactosidase, C(12)FDG, contains a lipophilic group that allows the substrate to penetrate through cell membranes under normal conditions. When the substrate is hydrolyzed by intracellular beta-galactosidase, a green fluorescent product is formed and retained inside the cell. Consequently, the stained beta-galactosidase-positive cells exhibit fluorescence, which is detected by flow cytometry. This new assay was used to analyze the segregational instability caused by a reduction in specific growth rate of the plasmid-bearing cells in the T7 expression system. Induction results in a substantial accumulation of intracellular beta-galactosidase along with a rapid increase in the fraction of plasmid-free cells. Once the cells lose the plasmid, they no longer produce beta-galactosidase, which is reduced by at least half every generation; thus, after staining, the fluorescent, plasmid-bearing cells can be distinguished from the nonfluorescent, plasmid-free cells using flow cytometry. This article describes the feasibility of the flow cytometric assay for single E. coli cells and reports the optimal assay conditions. A direct relationship between beta-galactosidase activity and green fluorescence intensity was found, and the fractions of recombinant cells in batch cultures were analyzed after various levels of induction.     

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。     

Characterization of a pH-inducible promoter system for high-level expression of recombinant proteins in Escherichia coli

A pH-inducible promoter system was characterized and its potential applicability in recombinant protein production was evaluated using a plasmid construct, pSM552-545C(-), in which the promoter and activator coding sequences of the cad operon were inserted into the upstream region of a lacZ' reporter gene. Graded gene expression levels with respect to culture pH between 8.0 and 5.5 were observed and the induction range can be as high as 200-fold. The effects of several cultivation parameters, including pH, temperature, induction cell density, and inoculum size, were systematically examined. The practical application of this expression system to high level production of recombinant proteins was successfully demonstrated using a rich medium, superbroth. An extremely high recombinant protein productivity at a value of approximately 1.4 g/L with a specific expression level as high as 35% of total cellular protein can be obtained in a simple batch cultivation. The behavior of this expression system was further investigated using chemostat cultures. An uncommon relationship between the volumetric or specific recombinant protein activity and the dilution rate, with a maximal activity at a dilution rate of approximately 0.4 h(-1)was observed. (c) 1995 John Wiley & Sons, Inc.     

Characterization of up-regulated proteases in an industrial recombinant Escherichia coli fermentation

Proteolytic degradation of recombinant proteins is an industry-wide challenge in host organisms such as Escherichia coli. These proteases have been linked to stresses, such as the stringent and heat-shock responses. This study reports the dramatic up-regulation of protease activity in an industrial recombinant E. coli fermentation upon induction. The objective of this project was to detect and characterize up-regulated proteases due to recombinant AXOKINE overexpression upon IPTG induction. AXOKINE is a 22-kDa protein currently in clinical trials as a therapeutic for obesity associated with diabetes. AXOKINE was expressed in both the soluble and inclusion body fractions in E. coli. Sodium dodecyl sulfate gelatin-polyacrylamide gel electrophoresis (SDS-GPAGE) was used to analyze the up-regulated protease activity. Western blot analysis showed degraded AXOKINE in both the soluble and insoluble fractions. Protease inhibitors were used to characterize the proteases. The proteases were ethylenediaminetetraacetic acid (EDTA) sensitive. The protease activity increased in the presence of phenyl-methyl sulfonyl-fluoride (PMSF), a serine protease inhibitor. The incubation buffer composition was varied with respect to Mg2+ and ATP, and the protease activity was ATP independent and Mg2+ dependent. A two-dimensional electrophoresis technique was used to estimate the pI of the proteases to be between 2.9 and 4.0.