High-level production of lycopene in metabolically engineered E. coli

Recombinant lycopene was generated by utilizing metabolically engineered Escherichia coli with yields being dependent upon inocula state. Yields were especially low in the case of cultures harboring high-copy plasmids that were established with inocula at the stationary growth phase. On the other hand, cultures derived using low-copy plasmid, however, yielded high amounts of lycopene irrespective of inocula state. Nevertheless, it showed still an inocula dependence pattern in lycopene productivity (mg/l/h). To further increase lycopene productivity, we applied a temperature-shift culture technique (37 → 25 °C). Using this method, we effectively enhanced lycopene productivity without any problematic phenomena. As a result, we were able to increase lycopene yield by approximately 20% compared to previous culture methods. In the present study, we were able to reach a final lycopene yield up to 260 mg/l for 60 h, which corresponds to the highest titer to date for the production of lycopene in E. coli.     

Assessment of bacterial acyltransferases for an efficient lipid production in metabolically engineered strains of E. coli

Microbially produced lipids like triacylglycerols or fatty acid ethyl esters are currently of great interest as fuel replacements or other industrially relevant compounds. They can even be produced by non-oleaginous microbes, like Escherichia coli, upon metabolic engineering. However, there is still much room for improvement regarding the yield for a competitive microbial production of lipids or biofuels. We genetically engineered E. coli by expressing fadD, fadR, pgpB, plsB and ‘tesA in combination with atfA from Acinetobacter baylyi. A total fatty acid contents of up to 16% (w/w) was obtained on complex media, corresponding to approximately 9% (w/w) triacylglycerols and representing the highest titers of fatty acids and triacylglycerols obtained in E. coli under comparable cultivation conditions, so far. To evaluate further possibilities for an optimization of lipid production, ten promising bacterial wax ester synthase/acyl-Coenzyme A:diacylglycerol acyltransferases were tested and compared. While highest triacylglycerol storage was achieved with AtfA, the mutated variant AtfA-G355I turned out to be most suitable for fatty acid ethyl ester biosynthesis and enabled an accumulation of approx. 500 mg/L without external ethanol supplementation.     

Efficient production of lycopene by engineered E. coli strains harboring different types of plasmids

Bioprocess and Biosystems Engineering - The lycopene biosynthetic genes crtE, crtB, and crtI from Deinococcus wulumuqiensis R12 were integrated into three different vector backbones—pET28a,...     

Directed evolution of metabolically engineered Escherichia coli for carotenoid production

We have previously introduced a reconstructed isoprenoid pathway into Escherichia coli that exhibits amplified biosynthetic flux to geranylgeranyl diphosphate (GGPP), a common isoprenoid precursor. It was shown that GGPP synthase is an important rate-controlling enzyme in this reconstructed isoprenoid pathway. In this investigation, we applied directed evolution to GGPP synthase from Archaeoglobus fulgidus to enable the enhanced production of carotenoids in metabolically engineered E. coli. Eight mutants were isolated, and the best one increased lycopene production by 100%. Among the mutants that were isolated, mutation points were clustered in four "hot regions". The "hottest" region is located in the sequence upstream of the coding region, which presumably improves the expression level of the enzyme. The other three are within the coding sequence and are believed to improve the enzyme-specific activity in E coli. These results demonstrate that modulating both enzymatic expression and specific activity are important for optimizing the metabolic flux distribution.     

Homofermentative production of D- or L-lactate in metabolically engineered Escherichia coli RR1

We investigated metabolic engineering of fermentation pathways in Escherichia coli for production of optically pure D- or L-lactate. Several pta mutant strains were examined, and a pta mutant of E. coli RR1 which was deficient in the phosphotransacetylase of the Pta-AckA pathway was found to metabolize glucose to D-lactate and to produce a small amount of succinate by-product under anaerobic conditions. An additional mutation in ppc made the mutant produce D-lactate like a homofermentative lactic acid bacterium. When the pta ppc double mutant was grown to higher biomass concentrations under aerobic conditions before it shifted to the anaerobic phase of D-lactate production, more than 62.2 g of D-lactate per liter was produced in 60 h, and the volumetric productivity was 1.04 g/liter/h. To examine whether the blocked acetate flux could be reoriented to a nonindigenous L-lactate pathway, an L-lactate dehydrogenase gene from Lactobacillus casei was introduced into a pta ldhA strain which lacked phosphotransacetylase and D-lactate dehydrogenase. This recombinant strain was able to metabolize glucose to L-lactate as the major fermentation product, and up to 45 g of L-lactate per liter was produced in 67 h. These results demonstrate that the central fermentation metabolism of E. coli can be reoriented to the production of D-lactate, an indigenous fermentation product, or to the production of L-lactate, a nonindigenous fermentation product.     

Synthetic mutualism in engineered E. coli mutant strains as functional basis for microbial production consortia

In nature, microorganisms often reside in symbiotic co-existence providing nutrition, stability, and protection for each partner by applying “division of labor.” This principle may also be used for the overproduction of targeted compounds in bioprocesses. It requires the engineering of a synthetic co-culture with distributed tasks for each partner. Thereby, the competition on precursors, redox cofactors, and energy—which occurs in a single host—is prevented. Current applications often focus on unidirectional interactions, that is, the product of partner A is used for the completion of biosynthesis by partner B. Here, we present a synthetically engineered Escherichia coli co-culture of two engineered mutant strains marked by the essential interaction of the partners which is achieved by implemented auxotrophies. The tryptophan auxotrophic strain E. coli ANT-3, only requiring small amounts of the aromatic amino acid, provides the auxotrophic anthranilate for the tryptophan producer E. coli TRP-3. The latter produces a surplus of tryptophan which is used to showcase the suitability of the co-culture to access related products in future applications. Co-culture characterization revealed that the microbial consortium is remarkably functionally stable for a broad range of inoculation ratios. The range of robust and functional interaction may even be extended by proper glucose feeding which was shown in a two-compartment bioreactor setting with filtrate exchange. This system even enables the use of the co-culture in a parallel two-level temperature setting which opens the door to access temperature sensitive products via heterologous production in E. coli in a continuous manner.     

Efficient production of 2-deoxy-scyllo-inosose from d-glucose by metabolically engineered recombinant Escherichia coli

2-Deoxy-scyllo-inosose (DOI) is a six-membered carbocycle formed from d-glucose-6-phosphate catalyzed by 2-deoxy-scyllo-inosose synthase (DOIS), a key enzyme in the biosynthesis of 2-deoxystreptamine-containing aminocyclitol antibiotics. DOI is valuable as a starting material for the benzene-free synthesis of catechol and other benzenoids. We constructed a series of metabolically engineered Escherichia coli strains by introducing a DOIS gene (btrC) from Bacillus circulans and disrupting genes for phosphoglucose isomerase, d-glucose-6-phosphate dehydrogenase, and phosphoglucomutase (pgi, zwf and pgm, respectively). It was found that deletion of the pgi gene, pgi and zwf genes, pgi and pgm genes, or all pgi, zwf and pgm genes significantly improved DOI production by recombinant E. coli in 2YTG medium (3% glucose) up to 7.4, 6.1, 11.6, and 8.4 g l(-1), respectively, compared with that achieved by wild-type recombinant E. coli (1.5 g l(-1)). Moreover, E. coli mutants with disrupted pgi, zwf and pgm genes showed strongly enhanced DOI productivity of up to 29.5 g l(-1) (99% yield) in the presence of mannitol as a supplemental carbon source. These results demonstrated that DOI production by metabolically engineered recombinant E. coli may provide a novel, efficient approach to the production of benzenoids from renewable d-glucose.     

Strategies for efficient repetitive production of succinate using metabolically engineered Escherichia coli

Escherichia coli AFP111, a pflB, ldhA, ptsG triple mutant of E. coli W1485, can be recovered for additional succinate production in fresh medium after two-stage fermentation (an aerobic growth stage followed by an anaerobic production stage). However, the specific productivity is lower than that of two-stage fermentation. In this study, three strategies were compared for reusing the cells. It was found when cells were aerobically cultivated at the end of two-stage fermentation without supplementing any carbon source, metabolites (mainly succinate and acetate) could be consumed. As a result, enzyme activities involved in the reductive arm of tricarboxylic acid cycle and the glyoxylate shunt were enhanced, yielding a succinate specific productivity above 1 2 5  \textmg  \textg_DCW ^{- 1}  \texth ^{- 1} 1 2 5\;{\text{mg}}\;{\text{g}}_{\rm DCW}^{ - 1} \,{\text{h}}^{ - 1} and a mass yield above 0.90 g g⁻¹ in the subsequent anaerobic fermentation. In addition, the intracellular NADH of cells subjected to aerobic cultivation with metabolites increased by more than 3.6 times and the ratio of NADH to NAD⁺ increased from 0.4 to 1.3, which were both favorable for driving the TCA branch to succinate.     

Uncovering the gene knockout landscape for improved lycopene production in E. coli

Systematic and combinatorial genetic approaches for the identification of gene knockout and overexpression targets have been effectively employed in the improvement of cellular phenotypes. Previously, we demonstrated how two of these tools, metabolic modeling and transposon mutagenesis, can be combined to identify strains of interest spanning the metabolic landscape of recombinant lycopene production in Escherichia coli. However, it is unknown how to best select multiple-gene knockout targets. Hence, this study seeks to understand how the overall order of gene selection, or search trajectory, biases the exploration and topology of the metabolic landscape. In particular, transposon mutagenesis and selection were employed in the background of eight different knockout genotypes. Collectively, 800,000 mutants were analyzed in hopes of exhaustively identifying all advantageous gene knockout targets. Several interesting observations, including clusters of gene functions, recurrence, and divergent genotypes, demonstrate the complexity of mapping only one genotype to one phenotype. One particularly interesting mutant, the ΔhnrΔyliE genotype, exhibited a drastically improved lycopene production capacity in basic minimal medium in comparison to the best strains identified in previous studies.     

In silico and in vivo stability analysis of a heterologous biosynthetic pathway for 1,4-butanediol production in metabolically engineered E. coli

Recently, several approaches have been published in order to develop a functional biosynthesis route for the non-natural compound 1,4-butanediol (BDO) in E. coli using glucose as a sole carbon source or starting from xylose. Among these studies, there was reported as high as 18 g/L product concentration achieved by industrial strains, however BDO production varies greatly in case of the reviewed studies. Our motivation was to build a simple heterologous pathway for this compound in E. coli and to design an appropriate cellular chassis based on a systemic biology approach, using constraint-based flux balance analysis and bi-level optimization for gene knock-out prediction. Thus, the present study reports, at the “proof-of concept” level, our findings related to model-driven development of a metabolically engineered E. coli strain lacking key genes for ethanol, lactate and formate production (ΔpflB, ΔldhA and ΔadhE), with a three-step biosynthetic pathway. We found this strain to produce a limited quantity of 1,4-BDO (.89 mg/L BDO under microaerobic conditions and .82 mg/L under anaerobic conditions). Using glycerol as carbon source, an approach, which to our knowledge has not been tackled before, our results suggest that further metabolic optimization is needed (gene-introductions or knock-outs, promoter fine-tuning) to address the redox potential imbalance problem and to achieve development of an industrially sustainable strain. Our experimental data on culture conditions, growth dynamics and fermentation parameters can consist a base for ongoing research on gene expression profiles and genetic stability of such metabolically engineered E. coli strains.     

Succinic acid production from sucrose and molasses by metabolically engineered E. coli using a cell surface display system

To achieve sucrose-metabolizing capability, different sucrose utilization operons have been introduced into E. coli that cannot utilize sucrose. However, these engineered strains still suffer from low growth rates and low sucrose uptake rates. In this study, cell surface display system was adopted in engineered E. coli AFP111 for succinic acid production from sucrose and molasses directly. Invertase (CscA) from E. coli W was successfully anchored to outer membrane by fusion with OmpC anchoring motif, and the displayed CscA showed high extracellular activity. Compared with the sucrose permease system, the cell surface display system consumed less ATP during sucrose metabolism. When less ATP was consumed by AFP111/pTrcC-cscA, the succinic acid productivity from sucrose was 23% higher than that by AFP111/pCR2.1-cscBKA that having the sucrose permease system. As a result, 41 g L⁻¹ and 36.3 g L⁻¹ succinic acid were produced by AFP111/pTrcC-cscA from sucrose and sugarcane molasses respectively at 34 h in 3-L fermentor during dual-phase fermentation. In addition, 79 g L⁻¹ succinic acid was accumulated with recovered AFP111/pTrcC-cscA cells at the end of dual-phase fermentation in 3-L fermentor, and the overall yield was 1.19 mol mol⁻¹ hexose.     

An engineered E.coli strain for the production of glycoglycerolipids

The glycolipid synthase MG517 from Mycoplasma genitalium catalyzes the glucosyl transfer from UDPGlc to diacylglycerol producing glycoglycerolipids (GGL) (Andrés et al., 2011). The enzyme was functional in E. coli accumulating GGL in the plasma membrane. A metabolic engineering strategy for GGL production was evaluated using this microorganism. To increase the levels of GGL precursors, UDPGlc and diacylglycerol, GalU and PlsC enzymes involved in their biosynthesis were overexpressed. Seven engineered strains were obtained containing different combinations of the mg517 with galU and plsC genes. Diacylglycerol synthesis showed to be limiting and the strain overexpressing MG517 and PlsC achieved the highest GGL yield. The new lipids were mono, di- and triglucosyldiacylglycerol with different acyl combinations in each compound. It indicates that the successive glucosyl transferase activities of MG517 have different acyl chain specificity for the acceptor substrate. GGL represented up to 6mg per g of dry weight.     

Effects of growth mode and pyruvate carboxylase on succinic acid production by metabolically engineered strains of Escherichia coli

Escherichia coli NZN111, which lacks activities for pyruvate-formate lyase and lactate dehydrogenase, and AFP111, a derivative which contains an additional mutation in ptsG (a gene encoding an enzyme of the glucose phophotransferase system), accumulate significant levels of succinic acid (succinate) under anaerobic conditions. Plasmid pTrc99A-pyc, which expresses the Rhizobium etli pyruvate carboxylase enzyme, was introduced into both strains. We compared growth, substrate consumption, product formation, and activities of seven key enzymes (acetate kinase, fumarate reductase, glucokinase, isocitrate dehydrogenase, isocitrate lyase, phosphoenolpyruvate carboxylase, and pyruvate carboxylase) from glucose for NZN111, NZN111/pTrc99A-pyc, AFP111, and AFP111/pTrc99A-pyc under both exclusively anaerobic and dual-phase conditions (an aerobic growth phase followed by an anaerobic production phase). The highest succinate mass yield was attained with AFP111/pTrc99A-pyc under dual-phase conditions with low pyruvate carboxylase activity. Dual-phase conditions led to significant isocitrate lyase activity in both NZN111 and AFP111, while under exclusively anaerobic conditions, an absence of isocitrate lyase activity resulted in significant pyruvate accumulation. Enzyme assays indicated that under dual-phase conditions, carbon flows not only through the reductive arm of the tricarboxylic acid cycle for succinate generation but also through the glyoxylate shunt and thus provides the cells with metabolic flexibility in the formation of succinate. Significant glucokinase activity in AFP111 compared to NZN111 similarly permits increased metabolic flexibility of AFP111. The differences between the strains and the benefit of pyruvate carboxylase under both exclusively anaerobic and dual-phase conditions are discussed in light of the cellular constraint for a redox balance.     

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。     

Effect of flue gas components on succinate production and CO2 fixation by metabolically engineered Escherichia coli

Escherichia coli pfl ldhA ptsG (AFP111) was studied for succinate production in defined medium using trace gases typically found in flue gas; i.e. oxygen (O₂), nitrogen dioxide (NO₂), sulfur dioxide (SO₂) and carbon monoxide (CO). Following aerobic cell growth, cells were exposed to 50% CO₂ and 3–10% O₂, or 50–300 ppm NO₂, SO₂ or CO during the succinate production phase. Although 3% O₂ did not significantly affect succinate formation, 10% O₂ reduced the final succinate concentration from 33 to 17 g/L, specific productivity from 1.90 to 1.13 mmol/g h and yield from 1.15 to 0.81 mol/mol glucose. The effect of O₂ correlated with the culture redox potential (ORP) with more reducing conditions favoring succinate production. The trace gases NO₂ and SO₂ also reduced the rate of succinate formation by as much as 50%, and led to a greater than twofold increase in pyruvate formation. Similar concentrations of CO showed no effect on succinate production rate or yield. Using synthetic flue gas AFP111 generated 12 g/L succinate with a specific productivity of 0.73 mmol/g h and a yield of 0.65 mol/mol.     

甲羟戊酸途径限速步骤研究及其在产番茄红素重组大肠杆菌中的应用

甲羟戊酸途径(MVA途径)被引入重组大肠杆菌中,能够提高重组大肠杆菌中萜类化合物的合成能力。但因重组大肠杆菌中萜类化合物合成途径中间产物积累,导致细胞生长和萜类化合物合成受到限制。本研究在稳定表达MVA途径以及优化2-甲基-D-赤藻糖醇-4-磷酸途径(MEP途径)、番茄红素合成途径关键基因表达的重组大肠杆菌LYC103中,用质粒高表达MVA途径和番茄红素合成途径关键基因,挖掘该途径的限速步骤。结果表明,ispA、crtE、mvaK1、idi和mvaD基因过表达后,细胞生长没有明显变化,番茄红素产量依次提高了13.5%、16.5%、17.95%、33.7%和61.1%,说明这几个基因可能是合成番茄红素的限速步骤。mvaK1、mvaK2、mvaD三个基因在同一操纵子上,用mRNA稳定区(RNA stabilizing region)进行启动子文库(mRSL)调控mvaK1,相当于对3个基因同时调控。用高效基因组编辑技术(CAGO)对mvaK1基因的mRNA稳定区进行启动子文库的调控,得到菌株LYC104。番茄红素产量与对照菌株LYC103相比增加了2倍,细胞生长提高了32%。然后,利用CR...