Biochemical production capabilities of Escherichia coli

Microbial metabolism provides at mechanism for the conversion of substrates into useful biochemicals. Utilization of microbes in industrial processes requires a modification of their natural metabolism in order to increase the efficiency of the desired conversion. Redirection of metabolic fluxes forms the basis of the newly defined field of metabolic engineering. In this study we use a flux balance based approach to study the biosynthesis of the 20 amino acids and 4 nucleotides as biochemical products. These amino acids and nucleotides are primary products of biosynthesis as well as important industrial products and precursors for the production of other biochemicals. The biosynthetic reactions of the bacterium Escherichia coli have been formulated into a metabolic network, and growth has been defined as a balanced drain on the metabolite pools corresponding to the cellular composition. Theoretical limits on the conversion of glucose, glycerol, and acetate substrates to biomass as well as the biochemical products have been computed. The substrate that results in the maximal carbon conversion to a particular product is identified. Criteria have been developed to identify metabolic constraints in the optimal solutions. The constraints of stoichiometry, energy, and redox have been determined in the conversions of glucose, glycerol, and acetate substrates into the biochemicals. Flux distributions corresponding to the maximal production of the biochemicals are presented. The goals of metabolic engineering are the optimal redirection of fluxes from generating biomass toward producing the desired biochemical. Optimal biomass generation is shown to decrease in a piecewise linear manner with increasing product formation. In some cases, synergy is observed between biochemical production and growth, leading to an increased overall carbon conversion. Balanced growth and product formation are important in a bioprocess, particularly for nonsecreted products. (c) 1993 John Wiley & Sons, Inc.     

Metabolic engineering of E. coli for improving mevalonate production to promote NADPH regeneration and enhance acetyl-CoA supply

Microbial production of mevalonate from renewable feedstock is a promising and sustainable approach for the production of value-added chemicals. We describe the metabolic engineering of Escherichia coli to enhance mevalonate production from glucose and cellobiose. First, the mevalonate-producing pathway was introduced into E. coli and the expression of the gene atoB, which encodes the gene for acetoacetyl-CoA synthetase, was increased. Then, the deletion of the pgi gene, which encodes phosphoglucose isomerase, increased the NADPH/NADP⁺ ratio in the cells but did not improve mevalonate production. Alternatively, to reduce flux toward the tricarboxylic acid cycle, gltA, which encodes citrate synthetase, was disrupted. The resultant strain, MGΔgltA-MV, increased levels of intracellular acetyl-CoA up to sevenfold higher than the wild-type strain. This strain produced 8.0 g/L of mevalonate from 20 g/L of glucose. We also engineered the sugar supply by displaying β-glucosidase (BGL) on the cell surface. When cellobiose was used as carbon source, the strain lacking gnd displaying BGL efficiently consumed cellobiose and produced mevalonate at 5.7 g/L. The yield of mevalonate was 0.25 g/g glucose (1 g of cellobiose corresponds to 1.1 g of glucose). These results demonstrate the feasibility of producing mevalonate from cellobiose or cellooligosaccharides using an engineered E. coli strain.     

Improved NADPH supply for xylitol production by engineered Escherichia coli with glycolytic mutations

Escherichia coli engineered to uptake xylose while metabolizing glucose was previously shown to produce high levels of xylitol from a mixture of glucose and xylose when expressing NADPH-dependent xylose reductase from Candida boidinii (CbXR) (Cirino et al., Biotechnol Bioeng. 2006;95:1167-1176). We then described the effects of deletions of key metabolic pathways (e.g., Embden-Meyerhof-Parnas and pentose phosphate pathway) and reactions (e.g., transhydrogenase and NADH dehydrogenase) on resting-cell xylitol yield (Y RPG: moles of xylitol produced per mole of glucose consumed) (Chin et al., Biotechnol Bioeng. 2009;102:209-220). These prior results demonstrated the importance of direct NADPH supply by NADP+-utilizing enzymes in central metabolism for driving heterologous NADPH-dependent reactions. This study describes strain modifications that improve coupling between glucose catabolism (oxidation) and xylose reduction using two fundamentally different strategies. We first examined the effects of deleting the phosphofructokinase (pfk) gene(s) on growth-uncoupled xylitol production and found that deleting both pfkA and sthA (encoding the E. coli-soluble transhydrogenase) improved the xylitol Y RPG from 3.4 ± 0.6 to 5.4 ± 0.4. The second strategy focused on coupling aerobic growth on glucose to xylitol production by deleting pgi (encoding phosphoglucose isomerase) and sthA. Impaired growth due to imbalanced NADPH metabolism (Sauer et al., J Biol Chem. 2004;279:6613-6619) was alleviated upon expressing CbXR, resulting in xylitol production similar to that of the growth-uncoupled precursor strains but with much less acetate secretion and more efficient utilization of glucose. Intracellular nicotinamide cofactor levels were also quantified, and the magnitude of the change in the NADPH/NADP+ ratio measured from cells consuming glucose in the absence vs. presence of xylose showed a strong correlation to the resulting Y RPG.     

氨基酸生产的代谢工程研究进展与发展趋势

氨基酸发酵是我国发酵工业的支柱产业,近年来,随着代谢工程的快速发展,氨基酸的代谢工程育种蓬勃发展。传统的正向代谢工程、基于组学分析与计算机模拟的反向代谢工程以及借鉴自然进化的进化代谢工程,都有越来越多的应用。在氨基酸的工业生产中涌现出了一系列具有高效生产、抗逆性强等优良性状的菌株。日益剧烈的市场竞争对菌株的选育提出了新的要求,如开发高附加值氨基酸品种、菌株代谢的动态调控、适应新工艺的要求等。文中介绍了氨基酸生产相关的代谢工程研究进展以及未来的发展趋势。     

Extension of cell membrane boosting squalene production in the engineered Escherichia coli

Squalene is a lipophilic and non-volatile triterpene with many industrial applications for food, pharmaceuticals, and cosmetics. Metabolic engineering focused on optimization of the production pathway suffer from little success in improving titers because of a limited space of the cell membrane accommodating the lipophilic product. Extension of cell membrane would be a promising approach to overcome the storage limitation for successful production of squalene. In this study, Escherichia coli was engineered for squalene production by overexpression of some membrane proteins. The highest production of 612 mg/L was observed in the engineered E. coli with overexpression of Tsr, a serine chemoreceptor protein, which induced invagination of inner membrane to form multilayered structure. It was also observed an increase in unsaturated fatty acid in membrane lipids composition, suggesting cellular response to maintain membrane fluidity against squalene accumulation in the engineered strain. This study potentiates the capability of E. coli for squalene production and provides an effective strategy for the enhanced production of such compounds.     

组合代谢调控提高大肠杆菌对氨基苯甲酸产量

对氨基苯甲酸是一种重要的有机合成中间体,广泛应用于医药、染料等行业。近年来对氨基苯甲酸作为一种潜在的高强度共聚物单体越来越受到重视。对氨基苯甲酸作为叶酸合成的前体之一,其合成在大肠杆菌体内由叶酸合成途径的pabA、pabB和pabC三个基因负责,催化分支酸合成对氨基苯甲酸。本研究以实验室构建的酪氨酸高产工程菌TYR002作为出发菌株,首先弱化双功能分支酸突变酶/预苯酸脱氢酶TyrA的表达,以减少酪氨酸积累,然后利用3种不同强度的组成型启动子分别调控pabA、pabB和pabC的表达。摇瓶发酵表明不同的组合调控模式下大肠杆菌发酵培养基中的对氨基苯甲酸积累量存在显著差异,最高可获得0.67 g/L的摇瓶发酵产量。进一步通过发酵条件优化和分批补料发酵,在5L发酵罐中获得了6.4g/L的对氨基苯甲酸产量。本研究为改善对氨基苯甲酸生物合成效率提供了重要理论参考。     

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.     

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.     

利用代谢工程改善大肠杆菌的3-脱氢莽草酸生产

3-脱氢莽草酸是芳香族氨基酸合成代谢途径中的一种重要中间产物。除可作为一种高效的抗氧化剂,还可用于合成己二酸、香草醛等一些重要的化工产品,具有重要的应用价值。相关研究证明具有去酪氨酸反馈抑制的3-脱氧-D-阿拉伯庚酮糖-7-磷酸合成酶基因aroFFBR以及转酮醇酶基因tktA可以有效影响3-脱氢莽草酸的过量合成。通过增加aroFFBR和tktA串联过量表达的拷贝数,可使工程菌株在摇瓶发酵条件下3-脱氢莽草酸产量提高2.93倍。通过同源重组无痕基因敲除技术依次敲除出发菌大肠杆菌Escherichia coli AB2834的乳酸、乙酸、乙醇等副产物合成途径中的重要基因ldhA、ackA-pta和adhE,可使工程菌株的3-脱氢莽草酸产量进一步提高,达到了1.83 g/L,是初始出发菌株大肠杆菌E.coli AB2834产量的6.7倍。利用5 L发酵罐进行分批补料发酵,62 h后工程菌株3-脱氢莽草酸产量达到了25.48 g/L。本研究可为构建有应用前景的3-脱氢莽草酸生产菌株提供重要参考。     

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.     

In silico design and adaptive evolution of Escherichia coli for production of lactic acid

The development and validation of new methods to help direct rational strain design for metabolite overproduction remains an important problem in metabolic engineering. Here we show that computationally predicted E. coli strain designs, calculated from a genome-scale metabolic model, can lead to successful production strains and that adaptive evolution of the engineered strains can lead to improved production capabilities. Three strain designs for lactate production were implemented yielding a total of 11 evolved production strains that were used to demonstrate the utility of this integrated approach. Strains grown on 2 g/L glucose at 37 degrees C showed lactate titers ranging from 0.87 to 1.75 g/L and secretion rates that were directly coupled to growth rates.     

大肠杆菌细胞工厂的创建技术

大肠杆菌作为一种重要的模式工业微生物,在医药、化工、农业等方面具有广泛的应用.近30年来,多种代谢工程改造的新策略和新技术,被用于设计、构建和优化大肠杆菌化学品细胞工厂,极大地提高了生物法合成化学品的生产速率和产量.文中将从大肠杆菌途径设计、合成途径创建与优化和细胞全局优化三个方面,对大肠杆菌代谢改造起重要推动作用的技...     

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.     

Analysis of NADPH supply during xylitol production by engineered Escherichia coli

Escherichia coli strain PC09 (DeltaxylB, cAMP-independent CRP (crp*) mutant) expressing an NADPH-dependent xylose reductase from Candida boidinii (CbXR) was previously reported to produce xylitol from xylose while metabolizing glucose [Cirino et al. (2006) Biotechnol Bioeng 95(6): 1167-1176]. This study aims to understand the role of NADPH supply in xylitol yield and the contribution of key central carbon metabolism enzymes toward xylitol production. Studies in which the expression of CbXR or a xylose transporter was increased suggest that enzyme activity and xylose transport are not limiting xylitol production in PC09. A constraints-based stoichiometric metabolic network model was used to understand the roles of central carbon metabolism reactions and xylose transport energetics on the theoretical maximum molar xylitol yield (xylitol produced per glucose consumed), and xylitol yields (Y(RPG)) were measured from resting cell biotransformations with various PC09 derivative strains. For the case of xylose-proton symport, omitting the Zwf (glucose-6-phosphate dehydrogenase) or PntAB (membrane-bound transhydrogenase) reactions or TCA cycle activity from the model reduces the theoretical maximum yield from 9.2 to 8.8, 3.6, and 8.0 mol xylitol (mol glucose)(-1), respectively. Experimentally, deleting pgi (encoding phosphoglucose isomerase) from strain PC09 improves the yield from 3.4 to 4.0 mol xylitol (mol glucose)(-1), while deleting either or both E. coli transhydrogenases (sthA and pntA) has no significant effect on the measured yield. Deleting either zwf or sucC (TCA cycle) significantly reduces the yield from 3.4 to 2.0 and 2.3 mol xylitol (mol glucose)(-1), respectively. Expression of a xylose reductase with relaxed cofactor specificity increases the yield to 4.0. The large discrepancy between theoretical maximum and experimentally determined yield values suggests that biocatalysis is compromised by pathways competing for reducing equivalents and dissipating energy. The metabolic role of transhydrogenases during E. coli biocatalysis has remained largely unspecified. Our results demonstrate the importance of direct NADPH supply by NADP+-utilizing enzymes in central metabolism for driving heterologous NADPH-dependent reactions, and suggest that the pool of reduced cofactors available for biotransformation is not readily interchangeable via transhydrogenase.     

Parametric sensitivity of stoichiometric flux balance models applied to wild-type Escherichia coli metabolism

The esterification of lauric acid with geraniol catalyzed by the commercially immobilized lipase preparation from Mucor miehei, Lipozyme(R), was studied in well-stirred flasks. The enzyme support was characterized in terms of its internal and external surface area, protein location, and protein content. It was found that the enzyme was mainly located on the external surface of the support, therefore, internal diffusional limitations were not important. It was also shown that the protein content of the support depends on the size of the particle, with smaller particles containing higher amounts of protein per unit weight. Under the conditions studied, the reaction was not under external mass transfer limitations, and the initial reaction rate depended on the size of the support particles. This was mainly due to the different protein contents on the support as a function of particle size and not to internal or external mass transfer limitations. Also, it was found that the inhibition exerted by water was predominantly a physical effect due to its accumulation around the enzyme. It was also found that the reaction was substrate inhibited by lauric acid, but not by geraniol. (c) 1995 John Wiley & Sons, Inc.     

异源表达多巴脱羧酶促进大肠杆菌从头合成多巴胺

多巴胺是多种天然抗氧化药物生物合成的前体物质,在人体内作为神经递质调控中枢神经系统的多种生理功能,常用于多种类型休克的临床治疗.目前,通过微生物合成技术已经实现了多巴胺的从头合成,但是合成效率很低.针对该问题,在左旋多巴(L-DOPA)大肠杆菌工程菌基础上,利用不同拷贝数质粒表达野猪Sus scrofa来源的多巴脱羧酶...