大肠杆菌生产异戊二烯的代谢工程研究进展

异戊二烯作为一种重要的化工原料,主要用于合成橡胶。此外,还广泛应用于医药或化工中间体、食品、粘合剂及航空燃料等领域。利用微生物法生产异戊二烯因具有环境友好、利用廉价的可再生原料、可持续发展等优势而成为当今研究的热点。这里介绍了大肠杆菌生产异戊二烯的代谢途径及关键酶,从代谢工程的角度出发综述了目前为提高大肠杆菌异戊二烯产量所应用到的方法和策略,并对今后的发展方向进行了展望。     

LC-MS/MS-based metabolic profiling of Escherichia coli under heterologous gene expression stress

Escherichia coli is frequently exploited for genetic manipulations and heterologous gene expression studies. We have evaluated the metabolic profile of E. coli strain BL21 (DE3) RIL CodonPlus after genetic modifications and subjecting to the production of recombinant protein. Three genetically variable E. coli cell types were studied, normal cells (susceptible to antibiotics) cultured in simple LB medium, cells harboring ampicillin-resistant plasmid pET21a (+), grown under antibiotic stress, and cells having recombinant plasmid pET21a (+) ligated with bacterial lactate dehydrogenase gene grown under ampicillin and standard isopropyl thiogalactoside (IPTG)-induced gene expression conditions. A total of 592 metabolites were identified through liquid chromatography-mass spectrometry/mass spectrometry analysis, feature and peak detection using XCMS and CAMERA followed by precursor identification by METLIN-based procedures. Overall, 107 metabolites were found differentially regulated among genetically modified cells. Quantitative analysis has shown a significant modulation in DHNA-CoA, p-aminobenzoic acid, and citrulline levels, indicating an alteration in vitamin K, folic acid biosynthesis, and urea cycle of E. coli cells during heterologous gene expression. Modulations in energy metabolites including NADH, AMP, ADP, ATP, carbohydrate, terpenoids, fatty acid metabolites, diadenosine tetraphosphate (Ap4A), and l -carnitine advocate major metabolic rearrangements. Our study provides a broader insight into the metabolic adaptations of bacterial cells during gene manipulation experiments that can be prolonged to improve the yield of heterologous gene products and concomitant production of valuable biomolecules.     

重组基因表达对大肠杆菌生理的影响

重组基因在表达外源蛋白质时常常会耗用大量的宿主细胞资源,从而对宿主造成代谢负荷,代谢负荷使得宿主的生化和生理产生很大的变化,甚至损害宿主正常的代谢功能。而过重的代谢负荷会影响目标蛋白的表达量和表达质量。综述了产生代谢负荷的原因,宿主细胞对代谢负荷的应激反应、以及减轻代谢负荷的策略。     

理性设计和构建过量合成莽草酸的大肠杆菌代谢工程菌

利用代谢工程手段理性改造野生大肠杆菌的莽草酸(Shikimic acid,SA)合成途径及相关代谢节点,以构建高产莽草酸的工程菌株.根据细胞代谢网络分析,利用Red-Xer重组系统连续删除了野生型大肠杆菌CICIMB0013的莽草酸激酶基因(aroL、aroK),葡萄糖磷酸转移酶系统(PTS)的关键组分EIICBglc的编码基因(ptsG)以及奎宁酸/莽草酸脱氢酶基因(ydiB)并系统评价了基因删除对细胞的生长、葡萄糖代谢和莽草酸积累的影响.aroL、aroK的删除阻断了莽草酸进一步转化成为莽草酸-3-磷酸,初步提高莽草酸的累积.删除ptsG基因使大肠杆菌PTS系统部分缺失,细胞通过GalP-glk(半乳糖透性酶-葡萄糖激酶)途径,利用ATP将葡萄糖磷酸化后进入细胞.利用该途径运输葡萄糖能够减少PEP的消耗,使得更多的碳代谢流进入莽草酸合成途径,从而显著提高了莽草酸的产量.在此基础上删除ydiB基因,阻止了莽草酸合成的前体物质3-脱氢奎宁酸转化为副产物奎宁酸(Quinic acid,QA),进一步提高了莽草酸的累积.初步发酵显示4个基因缺失的大肠杆菌代谢工程菌生产莽草酸的能力比原始菌提高了90多倍.     

代谢相关酶过表达对CHO细胞瞬时表达anti-hLAG3的影响

为提高CHO细胞重组蛋白表达量,对比研究了过表达代谢相关酶丙酮酸羧化酶(PYC2)、苹果酸酶Ⅱ(MDH2)、丙氨酸转氨酶1(ALT1)、鸟氨酸转氨甲酰酶(OTC)、氨基甲酰磷酸合成酶Ⅰ(CPS Ⅰ)和代谢相关蛋白牛磺酸转运蛋白(TAUT)及透明颤菌血红蛋白(VHb)对ExpiCHO-S瞬时表达anti-hLAG3的影响...     

应用DNA芯片技术对禽致病性大肠杆菌可能致病基因体外表达水平的研究

应用DNA芯片研究禽致病性大肠杆菌可能致病基因的表达.构建禽致病性大肠杆菌毒力基因、潜在毒力基因的DNA芯片,应用基因芯片技术对同属O2血清型的禽高致病性大肠杆菌E058株和低致病性大肠杆菌E526株在体外LB培养基和鸡血清培养状态下进行差异表达分析.结果:在体外LB静置培养状态下,低致病株E526与高致病株E058相比共有16个差异基因,均为下调基因.在鸡血清静置培养中,E526与E058相比共有15个差异基因,均为下调基因.应用基因芯片成功筛选了禽致病性大肠杆菌在体外不同条件下的毒力基因及可能毒力基因中差异表达基因,表明一些铁摄取系统相关基因对APEC的毒力较重要,同时也筛选出了一些新的可能致病基因aes-1,aes-2,aes-3,aes-4,aes-6,aes-8,aes-10,aes-13,aes-15,aes-31等.     

Engineering HlyA hypersecretion in Escherichia coli based on proteomic and microarray analyses

Escherichia coli is a common host for recombinant protein production for biotechnology applications. Secretion to the extracellular media has the potential to reduce protein aggregation and to simplify downstream purification. However, the complexity of the mechanisms of protein secretion has confounded prior attempts to engineer enhanced secretion phenotypes. Here, mutagenesis was used to perturb E. coli W3110 cells secreting HlyA via a Type I pathway. An activity assay identified a mutant secreting fourfold more active alpha-hemolysin than the parent strain. The mutant was characterized using both high-density microarrays for mRNA profiling and a proteomics strategy for protein expression. The relative mRNA and protein expression levels of tRNA-synthetases were decreased in the mutant compared to the parent. A mathematical model of prokaryotic translation was used to design a variant of the hlyA gene that encodes the same amino acid sequence but uses rare codons to slow the rate of translation by altering five bases. Analysis of the parent strain transformed with a plasmid containing this variant gene resulted in the recovery of, and further improvement upon, the selected hypersecretion phenotype. These results present one of the first successful metabolic engineering attempts based on molecular information provided by mRNA and protein expression profiling approaches and resulting in a phenotype useful to the biotechnology community.     

Novel insight into the secretory expression of recombinant enzymes in Escherichia coli

The secretory expression of recombinant enzymes in Escherichia coli has generally been a challenging task. In the present study, we investigated the expression of the extracellular enzyme cyclodextrin glycosyltransferase in E. coli. Our results indicated that when the overexpressed pre-proteins were not translocated across the inner membrane in a timely manner, they aggregated near the inner side of the E. coli inner membrane, resulting in the formation of insoluble inclusion bodies, which eventually blocked the pre-protein translocation channels and subsequently impeded further protein secretion. This mechanism suggests that for the efficient production of extracellular enzymes in E. coli, it is very important to maintain a balance between the rate of pre-protein synthesis and translocation, which can be achieved by altering the cultivation process. Our findings provide novel insight into the secretory expression of extracellular enzymes and may shed light on the further development of new strategies for extracellular protein production in E. coli.     

Advanced water splitting for green hydrogen gas production through complete oxidation of starch by in vitro metabolic engineering

Starch is a natural energy storage compound and is hypothesized to be a high-energy density chemical compound or solar fuel. In contrast to industrial hydrolysis of starch to glucose, an alternative ATP-free phosphorylation of starch was designed to generate cost-effective glucose 6-phosphate by using five thermophilic enzymes (i.e., isoamylase, alpha-glucan phosphorylase, 4-α-glucanotransferase, phosphoglucomutase, and polyphosphate glucokinase). This enzymatic phosphorolysis is energetically advantageous because the energy of α-1,4-glycosidic bonds among anhydroglucose units is conserved in the form of phosphorylated glucose. Furthermore, we demonstrated an in vitro 17-thermophilic enzyme pathway that can convert all glucose units of starch, regardless of branched and linear contents, with water to hydrogen at a theoretic yield (i.e., 12 H₂ per glucose), three times of the theoretical yield from dark microbial fermentation. The use of a biomimetic electron transport chain enabled to achieve a maximum volumetric productivity of 90.2 mmol of H₂/L/h at 20 g/L starch. The complete oxidation of starch to hydrogen by this in vitro synthetic (enzymatic) biosystem suggests that starch as a natural solar fuel becomes a high-density hydrogen storage compound with a gravimetric density of more than 14% H₂-based mass and an electricity density of more than 3000 W h/kg of starch.     

Anaerobic fermentation of glycerol by Escherichia coli: a new platform for metabolic engineering

The worldwide surplus of glycerol generated as inevitable byproduct of biodiesel fuel and oleochemical production is resulting in the shutdown of traditional glycerol-producing/refining plants and new applications are needed for this now abundant carbon source. In this article we report our finding that Escherichia coli can ferment glycerol in a pH-dependent manner. We hypothesize that glycerol fermentation is linked to the availability of CO(2), which under acidic conditions is produced by the oxidation of formate by the enzyme formate hydrogen lyase (FHL). In agreement with this hypothesis, glycerol fermentation was severely impaired by blocking the activity of FHL. We demonstrated that, unlike CO(2), hydrogen (the other product of FHL-mediated formate oxidation) had a negative impact on cell growth and glycerol fermentation. In addition, supplementation of the medium with CO(2) partially restored the ability of an FHL-deficient strain to ferment glycerol. High pH resulted in low CO(2) generation (low activity of FHL) and availability (most CO(2) is converted to bicarbonate), and consequently very inefficient fermentation of glycerol. Most of the fermented glycerol was recovered in the reduced compounds ethanol and succinate (93% of the product mixture), which reflects the highly reduced state of glycerol and confirms the fermentative nature of this process. Since glycerol is a cheap, abundant, and highly reduced carbon source, our findings should enable the development of an E. coli-based platform for the anaerobic production of reduced chemicals from glycerol at yields higher than those obtained from common sugars, such as glucose.     

Escherichia coli W as a new platform strain for the enhanced production of L-valine by systems metabolic engineering

A less frequently employed Escherichia coli strain W, yet possessing useful metabolic characteristics such as less acetic acid production and high L ‐valine tolerance, was metabolically engineered for the production of L ‐valine. The ilvA gene was deleted to make more pyruvate, a key precursor for L ‐valine, available for enhanced L ‐valine biosynthesis. The lacI gene was deleted to allow constitutive expression of genes under the tac or trc promoter. The ilvBN^mut genes encoding feedback‐resistant acetohydroxy acid synthase (AHAS) I and the L ‐valine biosynthetic ilvCED genes encoding acetohydroxy acid isomeroreductase, dihydroxy acid dehydratase, and branched chain amino acid aminotransferase, respectively, were amplified by plasmid‐based overexpression. The global regulator Lrp and L ‐valine exporter YgaZH were also amplified by plasmid‐based overexpression. The engineered E. coli W (ΔlacI ΔilvA) strain overexpressing the ilvBN^mut, ilvCED, ygaZH, and lrp genes was able to produce an impressively high concentration of 60.7 g/L L ‐valine by fed‐batch culture in 29.5 h, resulting in a high volumetric productivity of 2.06 g/L/h. The most notable finding is that there was no other byproduct produced during L ‐valine production. The results obtained in this study suggest that E. coli W can be a good alternative to Corynebacterium glutamicum and E. coli K‐12, which have so far been the most efficient L ‐valine producer. Furthermore, it is expected that various bioproducts including other amino acids might be more efficiently produced by this revisited platform strain of E. coli. Bioeng. 2011; 108:1140–1147. © 2010 Wiley Periodicals, Inc.     

Metabolic engineering strategies for butanol production in Escherichia coli

The global market of butanol is increasing due to its growing applications as solvent, flavoring agent, and chemical precursor of several other compounds. Recently, the superior properties of n-butanol as a biofuel over ethanol have stimulated even more interest. (Bio)butanol is natively produced together with ethanol and acetone by Clostridium species through acetone-butanol-ethanol fermentation, at noncompetitive, low titers compared to petrochemical production. Different butanol production pathways have been expressed in Escherichia coli, a more accessible host compared to Clostridium species, to improve butanol titers and rates. The bioproduction of butanol is here reviewed from a historical and theoretical perspective. All tested rational metabolic engineering strategies in E. coli to increase butanol titers are reviewed: manipulation of central carbon metabolism, elimination of competing pathways, cofactor balancing, development of new pathways, expression of homologous enzymes, consumption of different substrates, and molecular biology strategies. The progress in the field of metabolic modeling and pathway generation algorithms and their potential application to butanol production are also summarized here. The main goals are to gather all the strategies, evaluate the respective progress obtained, identify, and exploit the outstanding challenges.     

Metabolic engineering of Escherichia coli for the production of 1,2-propanediol from glycerol

Due to its availability, low‐price, and high degree of reduction, glycerol has become an attractive carbon source for the production of fuels and reduced chemicals. Using the platform we have established from the identification of key pathways mediating fermentative metabolism of glycerol, this work reports the engineering of Escherichia coli for the conversion of glycerol into 1,2‐propanediol (1,2‐PDO). A functional 1,2‐PDO pathway was engineered through a combination of overexpression of genes involved in its synthesis from the key intermediate dihydroxyacetone phosphate (DHAP) and the manipulation of the fermentative glycerol utilization pathway. The former included the overexpression of methylglyoxal synthase (mgsA), glycerol dehydrogenase (gldA), and aldehyde oxidoreductase (yqhD). Manipulation of the glycerol utilization pathway through the replacement of the native E. coli PEP‐dependent dihydroxyacetone kinase (DHAK) with an ATP‐dependent DHAK from C. freundii increased the availability of DHAP allowing for higher 1,2‐PDO production. Analysis of the major fermentative pathways indentified ethanol as a required co‐product while increases in 1,2‐PDO titer and yield were achieved through the disruption of the pathways for acetate and lactate production. Combination of these key metabolic manipulations resulted in an engineered E. coli strain capable of producing 5.6 g/L 1,2‐PDO, at a yield of 21.3% (w/w). This strain also performed well when crude glycerol, a by‐product of biodiesel production, was used as the substrate. The titer and yield achieved in this study were favorable to those obtained with the use of E. coli for the production of 1,2‐PDO from common sugars. Biotechnol. Bioeng. 2011; 108:867–879. © 2010 Wiley Periodicals, Inc.     

枯草芽孢杆菌代谢工程改造的策略与工具

作为一种食品安全级的典型工业模式微生物,枯草芽孢杆菌Bacillus subtilis由于具有非致病性、胞外分泌蛋白能力强以及无明显的密码子偏爱性等特点,现已被广泛应用于代谢工程领域。近年来,随着分子生物学和基因工程技术等的迅速发展,多种研究策略和工具被用于构建枯草芽孢杆菌底盘细胞进行生物制品的高效合成。文中从启动子工程、基因编辑、基因回路、辅因子工程以及途径酶组装等方面介绍枯草芽孢杆菌在代谢工程领域的研究历程,并总结其在生物制品生产中的相关应用,最后对其未来的研究方向进行展望。     

Biosynthesis of paromamine derivatives in engineered Escherichia coli by heterologous expression

Aims: Paromamine is a vital and common intermediate in the biosynthesis of 4,5 and 4,6‐disubstituted 2‐deoxystreptamine (DOS)‐containing aminoglycosides. Our aim is to develop an engineered Escherichia coli system for heterologous production of paromamine. Methods and Results: We have constructed a mutant of E. coli BL21 (DE3) by disrupting glucose‐6‐phosphate isomerase (pgi) of primary metabolic pathway to increase glucose‐6‐phosphate pool inside the host. Disruption was carried out by λ Red/ET recombination following the protocol mentioned in the kit. Recombinants bearing 2‐deoxy‐scyllo‐inosose (DOI), DOS and paromamine producing genes were constructed from butirosin gene cluster and heterologously expressed in engineered host designed as E. coli BL21 (DE3) Δpgi. Secondary metabolites produced by the recombinants fermentated in 2YTG medium were extracted, and analysis of the extracts showed there is formation of DOI, DOS and paromamine. Conclusions: Escherichia coli system is engineered for heterologous expression of paromamine derivatives of aminoglycoside biosynthesis. Significance and Impact of the Study: This is the first report of heterologous expression of paromamine gene set in E. coli. Hence a new platform is established in E. coli system for the production of paromamine which is useful for the exploration of novel aminoglycosides by combinatorial biosynthesis of 4,5‐ and 4,6‐disubtituted route of DOS‐containing aminoglycosides.     

代谢工程改造大肠杆菌合成丙二酸

丙二酸是一种重要的有机二元羧酸,其应用价值遍及化工、医药、食品等领域。本文以大肠杆菌为底盘细胞,过表达了ppc、aspC、panD、pa0132、yneI和pyc基因,成功构建了丙二酸合成重组菌株大肠杆菌BL21(TPP)。该菌株在摇瓶发酵条件下,丙二酸产量达到0.61 g/L。在5 L发酵罐水平,采用间歇补料的方式丙二酸的积累量达3.32 g/L。本研究应用了融合蛋白技术,将ppc和aspC、pa0132和yneI分别进行融合表达,构建了工程菌BL21(SCR)。在摇瓶发酵水平,该菌株丙二酸的积累量达到了0.83 g/L,较出发菌株BL21(TPP)提高了36%。在5 L发酵罐中,工程菌BL21(SCR)的丙二酸产量最高达5.61 g/L,较出发菌株BL21(TPP)提高了69%。本研究实现了丙二酸在大肠杆菌中的生物合成,为构建丙二酸合成的细胞工厂提供了理论依据和技术基础,同时也对其他二元羧酸的生物合成具有启发和指导意义。     

In vitro metabolic engineering of hydrogen production at theoretical yield from sucrose

Hydrogen is one of the most important industrial chemicals and will be arguably the best fuel in the future. Hydrogen production from less costly renewable sugars can provide affordable hydrogen, decrease reliance on fossil fuels, and achieve nearly zero net greenhouse gas emissions, but current chemical and biological means suffer from low hydrogen yields and/or severe reaction conditions. An in vitro synthetic enzymatic pathway comprised of 15 enzymes was designed to split water powered by sucrose to hydrogen. Hydrogen and carbon dioxide were spontaneously generated from sucrose or glucose and water mediated by enzyme cocktails containing up to15 enzymes under mild reaction conditions (i.e. 37 °C and atm). In a batch reaction, the hydrogen yield was 23.2 mol of dihydrogen per mole of sucrose, i.e., 96.7% of the theoretical yield (i.e., 12 dihydrogen per hexose). In a fed-batch reaction, increasing substrate concentration led to 3.3-fold enhancement in reaction rate to 9.74 mmol of H₂/L/h. These proof-of-concept results suggest that catabolic water splitting powered by sugars catalyzed by enzyme cocktails could be an appealing green hydrogen production approach.     

外源基因在大肠杆菌中的高效表达

为了提高外源蛋白在大杨杆菌中的表达量,人们对大肠杆菌表达系统进行了许多研究。作者综述了有关外源基因在大肠杆菌中高效表达的研究进展。