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 of menaquinone-8 pathway of Escherichia coli as a microbial platform for vitamin K production

Menaquinone-8 (MK-8, vitamin K) is composed of a non-polar side chain and a polar head group. Escherichia coli was chosen and metabolically engineered as a microbial platform for production of MK-8. MK-8 content in E. coli was significantly enhanced by modulating two precursor pools, which supply a non-polar side chain and a polar head group, and further increased by blocking formation of the competitor ubiquinone-8 (Q-8). Overexpression of E. coli IspA, DXR, or IDI increased MK-8 content up to twofold. A similar positive effect was also observed when E. coli MenA, MenB, MenC, MenD, MenE, MenF, or UbiE was overexpressed. The Q-8-deficient ubiCA mutant enhanced MK-8 content by 30% compared to wild-type E. coli. When MenA or MenD was overexpressed, MK-8 content was enhanced fivefold compared with wild-type E. coli.     

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.     

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.     

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。     

A “plug‐n‐play” modular metabolic system for the production of apocarotenoids

Apocarotenoids, such as α‐, β‐ionone, and retinol, have high commercial values in the food and cosmetic industries. The demand for natural ingredients has been increasing dramatically in recent years. However, attempts to overproduce β‐ionone in microorganisms have been limited by the complexity of the biosynthetic pathway. Here, an Escherichia coli‐based modular system was developed to produce various apocarotenoids. Incorporation of enzyme engineering approaches (N‐terminal truncation and protein fusion) into modular metabolic engineering strategy significantly improved α‐ionone production from 0.5 mg/L to 30 mg/L in flasks, producing 480 mg/L of α‐ionone in fed‐batch fermentation. By modifying apocarotenoid genetic module, this platform strain was successfully re‐engineered to produce 32 mg/L and 500 mg/L of β‐ionone in flask and bioreactor, respectively (>80‐fold higher than previously reported). Similarly, 33 mg/L of retinoids was produced in flask by reconstructing apocarotenoid module, demonstrating the versatility of the “plug‐n‐play” modular system. Collectively, this study highlights the importance of the strategy of simultaneous modular pathway optimization and enzyme engineering to overproduce valuable chemicals in microbes.     

Strain engineering for high‐level 5‐aminolevulinic acid production in Escherichia coli

Herein, we report the development of a microbial bioprocess for high‐level production of 5‐aminolevulinic acid (5‐ALA), a valuable non‐proteinogenic amino acid with multiple applications in medical, agricultural, and food industries, using Escherichia coli as a cell factory. We first implemented the Shemin (i.e., C4) pathway for heterologous 5‐ALA biosynthesis in E. coli. To reduce, but not to abolish, the carbon flux toward essential tetrapyrrole/porphyrin biosynthesis, we applied clustered regularly interspersed short palindromic repeats interference (CRISPRi) to repress hemB expression, leading to extracellular 5‐ALA accumulation. We then applied metabolic engineering strategies to direct more dissimilated carbon flux toward the key precursor of succinyl‐CoA for enhanced 5‐ALA biosynthesis. Using these engineered E. coli strains for bioreactor cultivation, we successfully demonstrated high‐level 5‐ALA biosynthesis from glycerol (~30 g L^?1) under both microaerobic and aerobic conditions, achieving up to 5.95 g L^?1 (36.9% of the theoretical maximum yield) and 6.93 g L^?1 (50.9% of the theoretical maximum yield) 5‐ALA, respectively. This study represents one of the most effective bio‐based production of 5‐ALA from a structurally unrelated carbon to date, highlighting the importance of integrated strain engineering and bioprocessing strategies to enhance bio‐based production.     

Metabolic engineering of Escherichia coli for the production of fumaric acid

Fumaric acid is a naturally occurring organic acid that is an intermediate of the tricarboxylic acid cycle. Fungal species belonging to Rhizopus have traditionally been employed for the production of fumaric acid. In this study, Escherichia coli was metabolically engineered for the production of fumaric acid under aerobic condition. For the aerobic production of fumaric acid, the iclR gene was deleted to redirect the carbon flux through the glyoxylate shunt. In addition, the fumA, fumB, and fumC genes were also deleted to enhance fumaric acid formation. The resulting strain was able to produce 1.45 g/L of fumaric acid from 15 g/L of glucose in flask culture. Based on in silico flux response analysis, this base strain was further engineered by plasmid‐based overexpression of the native ppc gene, encoding phosphoenolpyruvate carboxylase (PPC), from the strong tac promoter, which resulted in the production of 4.09 g/L of fumaric acid. Additionally, the arcA and ptsG genes were deleted to reinforce the oxidative TCA cycle flux, and the aspA gene was deleted to block the conversion of fumaric acid into L ‐aspartic acid. Since it is desirable to avoid the use of inducer, the lacI gene was also deleted. To increase glucose uptake rate and fumaric acid productivity, the native promoter of the galP gene was replaced with the strong trc promoter. Fed‐batch culture of the final strain CWF812 allowed production of 28.2 g/L fumaric acid in 63 h with the overall yield and productivity of 0.389 g fumaric acid/g glucose and 0.448 g/L/h, respectively. This study demonstrates the possibility for the efficient production of fumaric acid by metabolically engineered E. coli. Biotechnol. Bioeng. 2013; 110: 2025–2034. © 2013 Wiley Periodicals, Inc.     

Improved E. coli erythromycin A production through the application of metabolic and bioprocess engineering

In this report, small-scale culture and bioreactor experiments were used to compare and improve the heterologous production of the antibiotic erythromycin A across a series of engineered prototype Escherichia coli strains. The original strain, termed BAP1(pBPJW130, pBPJW144, pHZT1, pHZT2, pHZT4, pGro7), was designed to allow full erythromycin A biosynthesis from the exogenous addition of propionate. This strain was then compared against two alternatives hypothesized to increase final product titer. Strain TB3(pBPJW130, pBPJW144, pHZT1, pHZT2, pHZT4, pGro7) is a derivative of BAP1 designed to increase biosynthetic pathway carbon flow as a result of a ygfH deletion; whereas, strain TB3(pBPJW130, pBPJW144, pHZT1, pHZT2, pHZT4-2, pGro7) provided an extra copy of a key deoxysugar glycosyltransferase gene. Production was compared across the three strains with TB3(pBPJW130, pBPJW144, pHZT1, pHZT2, pHZT4, pGro7) showing significant improvement in erythronolide B (EB), 3-mycarosylerythronolide B (MEB), and erythromycin A titers. This strain was further tested in the context of batch bioreactor production experiments with time-course titers leveling at 4 mg/L, representing an approximately sevenfold increase in final erythromycin A titer.     

Influence of expression of the pet operon on intracellular metabolic fluxes of Escherichia coli

Fermentation patterns of Escherichia coli HB101 carrying plasmids expressing cloned genes of Zymomonas mobilis pyruvate decarboxylase (PDC) and alcohol dehydrogenase li (ADH) were determined in glucose-limited complex medium in pH-controlled anaerobic batch cultivations. Time profiles of glucose, dry cell weight, succinate, formate, acetate, and ethanol were determined, as were the activities of ADH and PDC. Fluxes through the central carbon pathways were calculated for each construct utilizing exponential phase data on extracellular components and assuming quasi-steady state for intermediate metabolites. Overall biomass yields were greatest for cells expressing both PDC and ADH activities. Yields of carbon catabolite end products were similar for all PDC-expressing strains and different from those for other strains. Relative to its glucose uptake rate, the strain with greatest PDC and ADH activities produces formate and acetate more slowly and ethanol more rapidly than other strains. Strong influences of plasmid presence and metabolic coupling complicate detailed interpretations of the data.     

微生物木糖发酵产乙醇的代谢工程

利用木质纤维素发酵生产乙醇具有广泛的应用前景。而自然界中缺少有效转化木糖为乙醇的微生物是充分利用纤维素水解产物、提高乙醇产率、降低生产成本的关键因素。多年来研究者利用分子生物学技术对微生物菌株进行了代谢工程改造,使其能更有效地利用木糖生产乙醇。以下主要对运动发酵单胞菌、大肠杆菌和酵母等候选产乙醇微生物的木糖代谢工程研究进展进行了概述。     

Metabolic engineering of Escherichia coli for the production of cadaverine: A five carbon diamine

A five carbon linear chain diamine, cadaverine (1,5‐diaminopentane), is an important platform chemical having many applications in chemical industry. Bio‐based production of cadaverine from renewable feedstock is a promising and sustainable alternative to the petroleum‐based chemical synthesis. Here, we report development of a metabolically engineered strain of Escherichia coli that overproduces cadaverine in glucose mineral salts medium. First, cadaverine degradation and utilization pathways were inactivated. Next, L ‐lysine decarboxylase, which converts L ‐lysine directly to cadaverine, was amplified by plasmid‐based overexpression of the cadA gene under the strong tac promoter. Furthermore, the L ‐lysine biosynthetic pool was increased by the overexpression of the dapA gene encoding dihydrodipicolinate synthase through the replacement of the native promoter with the strong trc promoter in the genome. The final engineered strain was able to produce 9.61 g L⁻¹ of cadaverine with a productivity of 0.32 g L⁻¹ h⁻¹ by fed‐batch cultivation. The strategy reported here should be useful for the bio‐based production of cadaverine from renewable resources. Biotechnol. Bioeng. 2011; 108:93–103. © 2010 Wiley Periodicals, Inc.     

Co‐culture engineering for microbial biosynthesis of 3‐amino‐benzoic acid in Escherichia coli

3‐amino‐benzoic acid (3AB) is an important building block molecule for production of a wide range of important compounds such as natural products with various biological activities. In the present study, we established a microbial biosynthetic system for de novo 3AB production from the simple substrate glucose. First, the active 3AB biosynthetic pathway was reconstituted in the bacterium Escherichia coli, which resulted in the production of 1.5 mg/L 3AB. In an effort to improve the production, an E. coli‐E. coli co‐culture system was engineered to modularize the biosynthetic pathway between an upstream strain and an downstream strain. Specifically, the upstream biosynthetic module was contained in a fixed E. coli strain, whereas a series of E. coli strains were engineered to accommodate the downstream biosynthetic module and screened for optimal production performance. The best co‐culture system was found to improve 3AB production by 15 fold, compared to the mono‐culture approach. Further engineering of the co‐culture system resulted in biosynthesis of 48 mg/L 3AB. Our results demonstrate co‐culture engineering can be a powerful new approach in the broad field of metabolic engineering.     

Culture conditions' impact on succinate production by a high succinate producing Escherichia coli strain

This work aimed to identify the key operational factors that significantly affect succinate production by the high succinate producing Escherichia coli strain SBS550MG (pHL413), which bears mutations inactivating genes adhE ldhA iclR ackpta::Cm(R) and overexpresses the pyruvate carboxylase from Lactococcus lactis. The considered factors included glucose concentration, cell density, CO(2) concentration in the gas stream, pH, and temperature. The results showed that high glucose concentrations inhibited succinate production and that there is a compromise between the total succinate productivity and succinate specific productivity, where the total productivity increased with the increase in cell density and the specific productivity decreased with cell density, probably due to mass transfer limitation. On the other hand, a CO(2) concentration of 100% in the gas stream showed the highest specific succinate productivity, probably by favoring pyruvate carboxylation, increasing the OAA pool that later is converted into succinate. A full factorial design of experiments was applied to analyze the pH and temperature effects on succinate production in batch bioreactors, where succinate yield was not significantly affected by either temperature (37 to 43°C) or pH (6.5 to 7.5). Additionally, the temperature effect on succinate productivity and titer was not significant, in the range tested. On the other hand, a pH of 6.5 showed very low productivity, whereas pH values of 7.0 and 7.5 resulted in significantly higher specific productivities and higher titers. The increase on pH value from 7.0 to 7.5 did not show significant improvement. Then, pH 7.0 should be chosen because it involves a lower cost in base addition.     

Escherichia coli genome-scale metabolic gene knockout of lactate dehydrogenase (ldhA), increases succinate production from glycerol

Genome-scale metabolic model (GEM) of Escherichia coli has been published with applications in predicting metabolic engineering capabilities on different carbon sources and directing biological discovery. The use of glycerol as an alternative carbon source is economically viable in biorefinery. The use of GEM for predicting metabolic gene deletion of lactate dehydrogenase (ldhA) for increasing succinate production in Escherichia coli from glycerol carbon source remained largely unexplored. Here, I hypothesized that metabolic gene knockout of ldhA in E. coli from glycerol could increase succinate production. A proof-of-principle strain was constructed and designated as E. coli BMS5 (ΔldhA), by predicting increased succinate production in E. coli GEM and confirmed the predicted outcomes using wet cell experiments. The mutant GEM (ΔldhA) predicted 11% increase in succinate production from glycerol compared to its wild-type model (iAF1260), and the E. coli BMS5 (ΔldhA) showed 1.05 g/l and its corresponding wild-type produced .05 g/l (23-fold increase). The proof-of-principle strain constructed in this study confirmed the aforementioned hypothesis and further elucidated the fact that E. coli GEM can prospectively and effectively predict metabolic engineering interventions using glycerol as substrate and could serve as platform for new strain design strategies and biological discovery.     

Improved heterologous production of the nonribosomal peptide‐polyketide siderophore yersiniabactin through metabolic engineering and induction optimization

Biosynthesis of complex natural products like polyketides and nonribosomal peptides using Escherichia coli as a heterologous host provides an opportunity to access these molecules. The value in doing so stems from the fact that many compounds hold some therapeutic or other beneficial property and their original production hosts are intractable for a variety of reasons. In this work, metabolic engineering and induction variable optimization were used to increase production of the polyketide‐nonribosomal peptide compound yersiniabactin, a siderophore that has been utilized to selectively remove metals from various solid and aqueous samples. Specifically, several precursor substrate support pathways were altered through gene expression and exogenous supplementation in order to boost production of the final compound. The gene expression induction process was also analyzed to identify the temperatures and inducer concentrations resulting in highest final production levels. When combined, yersiniabactin production was extended to ～175 mg L^?1. © 2016 American Institute of Chemical Engineers Biotechnol. Prog., 32:1412–1417, 2016     

Host strain influences on supercoiled plasmid DNA production in Escherichia coli: Implications for efficient design of large-scale processes

We set out to investigate if E. coli genotype plays a significant role in host strain selection for optimal processing of plasmid DNA based on both quality and quantity of supercoiling. Firstly 17 E. coli commercial and non-commercial strains were selected and their available genetic backgrounds were researched in the open literature. Growth characteristics of all the strains were considered and made impartial by using a common medium and growth condition platform. By keeping the growth conditions constant for each strain/plasmid combination, we are only looking at one variable which is the host strain. The second step was to attempt to correlate the findings with common genotype characteristics (e.g. mutations such as endA or recA). We found that one can screen the number of strains which are likely to give good productivity early on, before any further optimisation and verification is performed, both for small and large plasmids. Also, it is worth noting that complex plasmid interactions with each strain prevent the use of genotype alone in making an intelligent choice for supercoiling optimisation. This leads to a third optimisation step selecting a few of the potentially high performing strains based on high DNA yield and supercoiling, with a view to identify the factors which need improvement in strain design and bioreactor optimisation. We found that high specific growth rates of some strains did not affect the level of DNA supercoiling but did influence the total plasmid yield, potentially an important aspect in the design of fermentation strategy. Interestingly, a few host/plasmid combinations result in what appears to be runaway plasmid replication.