产异丁醇大肠杆菌工程菌的构建

摘要:酮酸脱羧酶是异丁醇生物合成的关键酶,而大肠杆菌中没有此基因.将乳脂乳球菌NIZO B1157的2-酮酸脱羧酶基因kdcA克隆到非生产菌株大肠杆菌中,同时串联表达与前体物质酮酸相关的alsS、ilvC和ilvD基因,构建了串联表达质粒pSTV29-alsS-ilvC-ilvD-kdcA.大肠杆茵工程茵成功表达了4个基因,并能利用葡萄糖发酵产异丁醇,发酵24h后最高产量为3 g/L.     

产异丁醇关键基因在大肠杆菌中表达的研究

[目的]改造大肠杆菌缬氨酸合成途径,使其能够代谢合成异丁醇.[方法]将乳酸乳球菌(Lactococcus lactis) 1.2829的2-酮异戊酸脱羧酶基因(kivD)和醇脱氢酶基因(adhA)串联克隆到大肠杆菌DH5α宿主中表达.[结果]经过改造的宿主菌发酵24 h后异丁醇产量为0.12 g/L.酶活测定实验发现,kivD和adhA基因在宿主菌中均得到表达,但由于KivD的低表达量导致宿主菌最终的异丁醇合成能力偏低.通过研究温度和pH对KivD和AdhA酶活的影响,最终选定二者的最适温度为30℃,最适pH为6.5. [结论]通过向宿主菌导入外源异丁醇合成基因能够改造其自身代谢途径,从而合成异丁醇.     

苯丙氨酸生物合成途径关键基因的串联表达

目的:改造大肠杆菌苯丙氨酸生物合成的中心代谢途径,优化关键酶基因pheA、aroF、ppsA、tktA的协同表达,进一步提高苯丙氨酸产量。方法:构建重组质粒pZE12-AFPT,鉴定后通过SDS-PAGE观察其蛋白表达量,并转入缺陷菌大肠杆菌MGΔ中构建工程菌,发酵培养后测量苯丙氨酸产量,与本室保存的重组质粒MGΔpZE12-AF做对比;构建重组质粒pZE21-AF和pZA31-PT,将后者转入感受态pZE12-AF和pZE21-AF中,得到双抗性质粒,并比较转化前后苯丙氨酸的产量。结果:工程菌MGΔpZE12-AFPT的苯丙氨酸产量比对照菌株MGΔpZE12-AF提高了近1.6倍,并且实现了4个串联基因的协同表达;质粒pZA31-PT转入pZE12-AF和pZE21-AF后,苯丙氨酸产量比原质粒pZE12-AF和pZE21-AF分别提高了近0.6倍和2.8倍。结论:实现了4个关键酶基因的串联表达,改造了苯丙氨酸的生物合成途径,使得苯丙氨酸产量有所提高,为进一步得到其高产菌株奠定了基础。     

糖丁基梭菌产丁醇途径在大肠杆菌中的构建及发酵

摘要:【目的】通过克隆来源于糖丁基梭菌(Clostridium saccharobutylicum DSM13864)丁醇合成途径的关键酶基因(thlA,bcs-operon和adhE),构建产丁醇大肠杆菌。【方法】以Clostridium saccharobutylicum DSM13864的基因组为模板,分别扩增丁醇途径关键酶基因thlA,bcs-operon(crt-bcd1-etfB2-fixB2-hbd)和adhE,构建了两个重组质粒pETDuet-bcs和pRSFDuet-thlA-adhE,并成功转入E.coli JM109(DE3)实现异源表达,使大肠杆菌具备产丁醇能力。在半厌氧条件下进行重组菌的发酵,并研究不同培养基对产丁醇的影响。【结果】该重组菌在半厌氧条件下经摇瓶发酵丁醇产量达到25.4 mg/L,通过优化培养基后,在TB发酵培养基中丁醇产量可达到34.1 mg/L。【结论】通过构建重组共表达质粒,将糖丁基梭菌来源的丁醇途径关键酶基因在大肠杆菌中表达,成功构建产丁醇大肠杆菌。该研究提供了一株易于操作的丁醇发酵重组大肠杆菌,避免了传统梭菌发酵丁醇生产中苛刻的厌氧条件、易产孢子等限制问题。     

稳定表达MVA途径基因提高番茄红素产量

萜类化合物的直接前体物质异戊烯焦磷酸(IPP)和二甲基烯丙基焦磷酸酯(DMAPP)可以由2-甲基-D-赤藻糖醇-4-磷酸途径(MEP途径)和甲羟戊酸途径(MVA途径)合成。在已经优化MEP合成途径、番茄红素合成途径关键基因表达的重组大肠杆菌LYC101中,引入MVA途径基因,进一步提高重组大肠杆菌合成萜类化合物的能力。质粒pALV23和pALV145是本实验室在研究MVA途径基因协调表达时,用核糖体结合位点(RBS)文库连接MVA途径各基因构建质粒文库,而筛选到的有效提高β-胡萝卜素产量的质粒。首先比较了两个质粒分别在低产和高产番茄红素的菌株中对番茄红素合成的影响。结果表明,两个质粒在高、低产番茄红素的菌株中都可以有效提高番茄红素产量。在高产菌LYC101中pALV23比pALV145使番茄红素产量更高。然后,用CRISPR-Cas9系统辅助同源重组的方法,将MVA途经基因和启动子一共6.7kb的条带整合到LYC101菌株的染色体上,得到遗传稳定的菌株LYC102。LYC102的番茄红素产率达40.9mg/g,是出发菌株LYC101产率的2.19倍,比用质粒表达MVA途径基因的菌株提高了20%。在重组大肠杆菌中同时表达MVA途径和MEP途径,可以有效提高萜类化合物产率;文中构建了不含质粒的、遗传稳定的高产番茄红素菌株,为产业化合成番茄红素提供基础;同时构建平台菌株,可以用于其他萜类化合物合成。     

酿酒酵母gpd1和hor2基因在大肠杆菌中的共表达

利用途径工程的方法,在大肠杆菌中构建一条新的产甘油的代谢途径。从酿酒酵母(Saccharomyces cerevisiae)克隆3-磷酸甘油脱氢酶基因(gpd1)和3-磷酸甘油酯酶基因(hor2),并将两个基因串连到启动子trc的下游,构建由trc启动子控制的能高效表达的多顺反子重组质粒pSE-gpd1-hor2,将重组质粒导入大肠杆菌BL21菌株中,构建得到的重组菌株GxB-gh能将葡萄糖转化为甘油。结果表明重组菌株GxB-gh以葡萄糖为底物进行发酵,甘油产量为46．67g／L,葡萄糖的转化率为42.87％。这为利用工程菌绿色生产甘油进行了前期的探索,也为进一步构建能生产1,3-丙二醇的工程菌打下了良好的基础。     

大肠杆菌astE、rph基因敲除突变株的构建

目的:分别构建大肠杆菌astE、rph基因敲除突变株,并检测其异丁醇耐受性的变化。方法:利用Red重组系统分别敲除大肠杆菌的astE和rph基因,并对所获得的突变株进行异丁醇耐受性相关实验研究。结果:成功构建了astE基因缺失突变株△astE和rph基因缺失突变株Δrph,发现两种突变株的异丁醇耐受性均有所提高。结论:通过缺陷菌株的构建,为未来进一步代谢改造生产异丁醇和研究异丁醇耐受机制奠定了基础。     

基因敲除提高大肠杆菌工程菌生产异丁醇产量的研究

探究pflB、frdAB、fnr和AdhE四基因缺失突变株对大肠杆菌工程菌发酵生产异丁醇的影响。运用Red重组系统敲除大肠杆菌BW25113的pflB、frdAB、fnr和AdhE基因,构建pflB、frdAB、fnr和AdhE四基因缺失突变株E.coliBW25113H,结合本实验室已经构建的表达质粒pSTV29-alsS-ilvC-ilvD-kdcA,并检测该工程菌在1L发酵罐的发酵过程中的生物量、突变菌株的稳定性、异丁醇产量及有机酸含量的变化情况。成功获得pflB、frdAB、fnr和AdhE四基因缺失突变株BW25113H。发酵结果表明,该工程菌能以较长时间,较高比生长速率保持对数生长期,其稳定性较好,异丁醇产量增加了40%。成功构建pflB、frdAB、fnr和AdhE四基因缺失突变株BW25113H,结合非自身发酵途径使异丁醇的产量由3 g/L提升至4.2 g/L。     

产L-苏氨酸重组大肠杆菌的构建和发酵性能

【背景】大肠杆菌由于生长性能优良、遗传背景清晰,常被用作苏氨酸生产菌。【目的】敲除大肠杆菌Escherichia coli THR苏氨酸合成途径的非必需基因,并异源表达苏氨酸合成必需的关键酶,构建一株苏氨酸高产菌株。【方法】利用FLP/FRT重组酶系统,敲除E. coli THR中lysC、pfkB和sstT,同时进行谷氨酸棒杆菌中lysC~(fbr)、thrE和丙酮丁醇梭菌中gapC的重组质粒构建并转化到宿主菌中。【结果】以E. coli THR为出发菌株,敲除其苏氨酸合成途径中表达天冬氨酸激酶Ⅲ (AKⅢ)的基因lysC、磷酸果糖激酶Ⅱ基因pfkB及苏氨酸吸收蛋白表达基因sstT,使菌株积累苏氨酸的产量达到75.64±0.35g/L,比出发菌株增加9.9%。随后异源表达谷氨酸棒杆菌中解除了反馈抑制的天冬氨酸激酶(lysC~(fbr))、苏氨酸分泌转运蛋白(thrE)及丙酮丁醇梭菌中由gapC编码的NADP+依赖型甘油醛-3-磷酸脱氢酶,获得重组菌株E. coli THR6菌株。该菌株积累苏氨酸的产量提高到105.3±0.5 g/L,糖酸转化率提高了43.20%,单位产酸能力提高到5.76 g/g DCW,最大生物量为18.26 g DCW/L。【结论】单独敲除某个基因或改造某个途径不能使苏氨酸大量合成和积累,对多个代谢途径共同改造是构建苏氨酸工程菌的最有效方法。     

基于PTS缺陷型大肠杆菌构建莽草酸生产菌

对大肠杆菌芳香族氨基酸合成途径进行代谢流改造, 以实现高效的生物制备莽草酸。以磷酸烯醇式丙酮酸-糖磷酸转移酶系统(PTS系统)敲除菌DH5α△ptsHIcrr (DHP)为基础, 特异性敲除aroL、ydiB基因并转入受阿拉伯糖诱导表达的T7-RNA聚合酶基因, 最终构建一系列产莽草酸宿主菌。再将aroE、aroB、tktA、glk、aroFfbr组成的系列基因串联起来置于质粒上, 在T7启动子控制下表达, 经摇瓶培养检测得知, 不同重组菌产莽草酸能力与对照相比均有明显提高, 其中DHPYA-T7/pAOC-TGEFB菌株产量最高, 可达到392 mg/L。为进一步构建高表达莽草酸工程菌奠定基础。     

Isobutanol production in Corynebacterium glutamicum: Suppressed succinate by-production by pckA inactivation and enhanced productivity via the Entner–Doudoroff pathway

On the basis of our previous studies of microbial L-valine production under oxygen deprivation, we developed isobutanol-producing Corynebacterium glutamicum strains. The artificial isobutanol synthesis pathway was composed of the first three steps of the L-valine synthesis pathway; and the subsequent Ehrlich Pathway: pyruvate was converted to 2-ketoisovalerate in the former reactions; and the 2-keto acid was decarboxylated into isobutyraldehyde, and subsequently reduced into isobutanol in the latter reactions. Although there exists redox cofactor imbalance in the overall reactions, i.e., NADH is generated via glycolysis whereas NADPH is required to synthesize isobutanol, it was resolved by taking advantage of the NAD-preferring mutant acetohydroxy acid isomeroreductase encoded by ilvC^TM and the NAD-specific alcohol dehydrogenase encoded by adhA. Each enzyme activity to synthesize isobutanol was finely tuned by using two kinds of lac promoter derivatives. Efficient suppression of succinate by-production and improvement of isobutanol yield resulted from inactivation of pckA, which encodes phosphoenolpyruvate carboxykinase, whereas glucose consumption and isobutanol production rates decreased because of the elevated intracellular NADH/NAD⁺ ratio. On the other hand, introduction of the exogenous Entner–Doudoroff pathway effectively enhanced glucose consumption and productivity. Overexpression of phosphoenolpyruvate:carbohydrate phosphotransferase system specific to glucose and deletion of ilvE, which encodes branched-chain amino acid transaminase, further suppressed by-products and improved isobutanol productivity. Finally, the produced isobutanol concentration reached 280 mM at a yield of 84% (mol/mol glucose) in 24 h.     

Redesigning Escherichia coli metabolism for anaerobic production of isobutanol

Fermentation enables the production of reduced metabolites, such as the biofuels ethanol and butanol, from fermentable sugars. This work demonstrates a general approach for designing and constructing a production host that uses a heterologous pathway as an obligately fermentative pathway to produce reduced metabolites, specifically, the biofuel isobutanol. Elementary mode analysis was applied to design an Escherichia coli strain optimized for isobutanol production under strictly anaerobic conditions. The central metabolism of E. coli was decomposed into 38,219 functional, unique, and elementary modes (EMs). The model predictions revealed that during anaerobic growth E. coli cannot produce isobutanol as the sole fermentative product. By deleting 7 chromosomal genes, the total 38,219 EMs were constrained to 12 EMs, 6 of which can produce high yields of isobutanol in a range from 0.29 to 0.41 g isobutanol/g glucose under anaerobic conditions. The remaining 6 EMs rely primarily on the pyruvate dehydrogenase enzyme complex (PDHC) and are typically inhibited under anaerobic conditions. The redesigned E. coli strain was constrained to employ the anaerobic isobutanol pathways through deletion of 7 chromosomal genes, addition of 2 heterologous genes, and overexpression of 5 genes. Here we present the design, construction, and characterization of an isobutanol-producing E. coli strain to illustrate the approach. The model predictions are evaluated in relation to experimental data and strategies proposed to improve anaerobic isobutanol production. We also show that the endogenous alcohol/aldehyde dehydrogenase AdhE is the key enzyme responsible for the production of isobutanol and ethanol under anaerobic conditions. The glycolytic flux can be controlled to regulate the ratio of isobutanol to ethanol production.     

Elucidating and reprogramming Escherichia coli metabolisms for obligate anaerobic n-butanol and isobutanol production

Elementary mode (EM) analysis based on the constraint-based metabolic network modeling was applied to elucidate and compare complex fermentative metabolisms of Escherichia coli for obligate anaerobic production of n-butanol and isobutanol. The result shows that the n-butanol fermentative metabolism was NADH-deficient, while the isobutanol fermentative metabolism was NADH redundant. E. coli could grow and produce n-butanol anaerobically as the sole fermentative product but not achieve the maximum theoretical n-butanol yield. In contrast, for the isobutanol fermentative metabolism, E. coli was required to couple with either ethanol- or succinate-producing pathway to recycle NADH. To overcome these "defective" metabolisms, EM analysis was implemented to reprogram the native fermentative metabolism of E. coli for optimized anaerobic production of n-butanol and isobutanol through multiple gene deletion (~8-9 genes), addition (~6-7 genes), up- and downexpression (~6-7 genes), and cofactor engineering (e.g., NADH, NADPH). The designed strains were forced to couple both growth and anaerobic production of n-butanol and isobutanol, which is a useful characteristic to enhance biofuel production and tolerance through metabolic pathway evolution. Even though the n-butanol and isobutanol fermentative metabolisms were quite different, the designed strains could be engineered to have identical metabolic flux distribution in "core" metabolic pathways mainly supporting cell growth and maintenance. Finally, the model prediction in elucidating and reprogramming the native fermentative metabolism of E. coli for obligate anaerobic production of n-butanol and isobutanol was validated with published experimental data.     

Engineering Corynebacterium glutamicum for isobutanol production

The production of isobutanol in microorganisms has recently been achieved by harnessing the highly active 2-keto acid pathways. Since these 2-keto acids are precursors of amino acids, we aimed to construct an isobutanol production platform in Corynebacterium glutamicum, a well-known amino-acid-producing microorganism. Analysis of this host’s sensitivity to isobutanol toxicity revealed that C. glutamicum shows an increased tolerance to isobutanol relative to Escherichia coli. Overexpression of alsS of Bacillus subtilis, ilvC and ilvD of C. glutamicum, kivd of Lactococcus lactis, and a native alcohol dehydrogenase, adhA, led to the production of 2.6 g/L isobutanol and 0.4 g/L 3-methyl-1-butanol in 48 h. In addition, other higher chain alcohols such as 1-propanol, 2-methyl-1-butanol, 1-butanol, and 2-phenylethanol were also detected as byproducts. Using longer-term batch cultures, isobutanol titers reached 4.0 g/L after 96 h with wild-type C. glutamicum as a host. Upon the inactivation of several genes to direct more carbon through the isobutanol pathway, we increased production by ∼25% to 4.9 g/L isobutanol in a ∆pyc∆ldh background. These results show promise in engineering C. glutamicum for higher chain alcohol production using the 2-keto acid pathways.     

Isobutanol production in engineered Saccharomyces cerevisiae by overexpression of 2-ketoisovalerate decarboxylase and valine biosynthetic enzymes

Engineering of Saccharomyces cerevisiae to produce advanced biofuels such as isobutanol has received much attention because this yeast has a natural capacity to produce higher alcohols. In this study, construction of isobutanol production systems was attempted by overexpression of effective 2-keto acid decarboxylase (KDC) and combinatorial overexpression of valine biosynthetic enzymes in S. cerevisiae D452-2. Among the six putative KDC enzymes from various microorganisms, 2-ketoisovalerate decarboxylase (Kivd) from L. lactis subsp. lactis KACC 13877 was identified as the most suitable KDC for isobutanol production in the yeast. Isobutanol production by the engineered S. cerevisiae was assessed in micro-aerobic batch fermentations using glucose as a sole carbon source. 93?mg/L isobutanol was produced in the Kivd overexpressing strain, which corresponds to a fourfold improvement as compared with the control strain. Isobutanol production was further enhanced to 151?mg/L by additional overexpression of acetolactate synthase (Ilv2p), acetohydroxyacid reductoisomerase (Ilv5p), and dihydroxyacid dehydratase (Ilv3p) in the cytosol.     

乙酰乳酸合成酶基因的克隆与高效表达

【目的】乙酰乳酸合成酶(ALS)是异丁醇生物合成中的关键酶,实现ALS的高效表达对调控异丁醇代谢途径有重要意义。【方法】根据GenBank中ALS的基因序列(alsS)设计引物,以枯草芽孢杆菌168基因组DNA为模板通过PCR扩增技术得到目标酶基因,目的片段全长为1 713 bp。将alsS连接到pET-30a(+)上,得到重组质粒pET-30a(+)-alsS,并在Escherichia coli BL2l(DE3)中实现表达。【结果】对表达条件进行了优化,获得最佳表达条件为:诱导温度30°C,诱导起始菌体OD600为0.6 0.8,诱导剂IPTG浓度为1 mmol/L,诱导时间为6 h。表达的乙酰乳酸合成酶大部分以可溶性形式存在于菌体内,优化后酶活可达到24.4 U/mL,比优化前提高了7.13倍。经HisTrapTMFF亲和层析后获得电泳纯的ALS,比活为95.2 U/mg。【结论】ALS的有效表达为在大肠杆菌体内构建异丁醇代谢途径打下了基础。     

Transposition of the phage D3112 genome in Escherichia coli cells

It has been demonstrated that the genome of phage D3112 of Preudomonas aeruginosa can be transposed into Escherichia coli chromosome as a component of the hybrid plasmid RP4 TcrKms::D3112. Also, transposition of D3112 from E. coli (D3112) chromosome into RP4 plasmid occurs. The phage stimulates the chromosome mobilizing activity of RP4 plasmid, similar to other transposons. E. coli (RP4::D3112) cells were previously shown to form no colonies at 30 degrees C. Auxotrophic mutants and mutants incapable of utilizing different carbohydrates were found among E. coli clones survived after a long incubation at 30 degrees C (at frequencies approximately 10(-3) - 10(-4). These mutants inherited stably the capability to produce D3112 phage. E. coli auxotrophic mutants have arisen indeed as a consequence of phage integration into the E. coli chromosome, since prototrophic transductants derived from these mutants after their treatment with generalized transducing P1 phage have lost the ability to produce D3112 phage. Clones with mutations in Km or Tc genes of RP4 plasmid, occurring at high frequencies (about 3%) were found after introduction of RP4 into E. coli (D3112). These mutant RP4 plasmids carry insertions of D3112 genomes. Clones of E. coli which lost mutant plasmids still produce D3112 and retain their initial auxotrophic mutations.     

The Formation of Higher Alcohols in the Fermentation of Amino Acids by Yeast

It was confirmed that washed yeast cells produced isoamyl alcohol and isobutanol from either pyruvic acid or α-ketoisovaleric acid. At the same time α-ketoisocaproic acid, a presumed intermediate to isoamyl alcohol, was found.

These results seem to support the presumptive scheme that pyruvic acid converts to α-ketoisocaproic acid via acetolactic acid and α-keto,isovaleric acid, from which isoamyl alcohol and isobutanol are formed.