Overproduction of glycogen in Escherichia coli blocked in the acetate pathway improves cell growth

Excessive production of acetate is a problem frequently encountered in aerobic high-cell-density fermentations of Escherichia coli. Here, we have examined genetic alterations resulting in glycogen overproduction as a possible means to direct the flux of carbon away from the acetate pool. Glycogen overaccumulation was achieved either by using a regulatory glgQ mutation or by transforming cells with a plasmid containing the glycogen biosynthesis genes glgC (encoding ADPG pyrophosphorylase) and glgA (encoding glycogen synthase) under their native promoter. Both strategies resulted in an approximately five-fold increase in glycogen levels but had no significant effect on acetate excretion. The glgC and glgA genes were then placed under the control of the isopropyl---D-thiogalactopyranoside (IPTG) inducible tac promoter, and this construct was used to stimulate glycogen production in a mutant defective in acetate biosynthesis due to deletion of the ack (acetate kinase) and pta (phosphotransacetylase) genes. If glycogen overproduction in the ack pta strain was induced during the late log phase, biomass production increased by 15 to 20% relative to uninduced controls. Glycogen overaccumulation had a significant influence on carbon partitioning: The output of carbon dioxide peaked earlier than in the control strain, and the levels of an unusual fermentation byproduct, pyruvate, were reduced. Exogenous pyruvate was metabolized more rapidly, suggesting higher activity of gluconeogenesis or the tricarboxylic acid (TCA) cycle as a result of glycogen overproduction. Potential mechanisms of the observed metabolic alterations are discussed. Our results suggest that ack pta mutants over producing glycogen may be a suitable starting point for constructing E. coli strains with improved characteristics in high-cell-density fermentations. (c) 1994 John Wiley & Sons, Inc.     

系统代谢工程改造树干毕赤酵母生产琥珀酸

为提高树干毕赤酵母发酵生产琥珀酸的产量,借助基因组规模代谢网络模型iTL885获得琥珀酸合成的最佳代谢途径为扩增icl1基因和敲除sdh1基因。在此基础上,借助代谢工程策略构建过量表达异柠檬酸裂解酶基因icl1的重组菌株FPLicl、缺失琥珀酸脱氢酶基因sdh1的重组菌株FPLΔsdh和缺失sdh1基因同时过量表达icl1基因的重组菌株FPLΔsdh-icl。结果表明:3株重组菌的异柠檬酸裂解酶活性由0.33 U/mg分别增加为1.6、5.6和6.6U/mg;而琥珀酸脱氢酶活性则从13.8 U/mg分别降为10.7、0.3和0.3 U/mg。在以木糖为C源的培养基中,3株重组菌生产琥珀酸的能力分别是0.30、1.20和1.60 g/L。     

共表达烟酸转磷酸核糖激酶和丙酮酸羧化酶对大肠杆菌NZN111产丁二酸的影响

构建了共表达烟酸转磷酸核糖激酶(NAPRTase)和丙酮酸羧化酶(PYC)的重组质粒pTrc99a-pncB-pyc,并考察了重组菌E.coli NZN111/pTrc99a-pncB-pyc生产丁二酸的能力。结果表明:重组菌NZN111/pTrc99a-pncB-pyc的NAPRTase和PYC的比酶活达到最高,分别为20.75和1.04 U/mg,同时,辅酶NADH、NAD+及NAD(H)总量达到最高。厌氧摇瓶发酵结果:48 h能够消耗17.5 g/L的葡萄糖生成14.08 g/L的丁二酸,而丙酮酸的产量大幅度降低,仅为0.11 g/L。本研究为基因工程菌大肠杆菌厌氧条件下发酵生产丁二酸提供了一定的基础。     

Modification of central metabolic pathway in escherichia coli to reduce acetate accumulation by heterologous expression of the bacillus subtilis acetolactate synthase gene

A novel metabolic engineering technique involving the redirection ofcellular carbon fluxes was employed to reduce acetate production in an Escherichia coli culture. Metabolic engineering was achieved by cloning E. coli the gene for the Bacillus subtilis acetolactate synthase (ALS), an enzyme capable of catalyzing the conversion of pyruvate to nonacidic and less harmful species. The heterologous expression of the ALS catabolic enzyme in Escherichia coli drastically modified the cellular glycolytic fluxes. In particular, acetate excretion, which is a common characteristic of E. coli, as well as a physiological burden, was minimized. The residual acetate level was kept under control and maintained at a level that was below the toxic threshold. The expression of the biologically active ALS enzyme in E. coli did not result in any detectable changes on either cell growth rate or cell yields. The alternative product, acetoin, was shown to be 50 times less harmful than acetate. Similarities in the growth pattern of two different E. coli strains, RR1 and GJT001, under all cultivation conditions suggested that the ability of ALS to reduce acetate accumulation is generic and not strain-specific. (c) 1994 John Wiley & Sons, Inc.     

Metabolic engineering of Escherichia coli for the production of medium-chain-length polyhydroxyalkanoates rich in specific monomers

The Escherichia coli fabG(Ec) gene and the Pseudomonas aeruginosa rhlG(Pa) gene, which encode 3-ketoacyl-acyl carrier protein reductase, were expressed in E. coli W3110 and its fadA mutant strain WA101 to examine their roles in medium-chain-length (MCL) polyhydroxyalkanoate (PHA) biosynthesis from fatty acids. When one of these 3-ketoacyl-acyl carrier protein reductase genes was co-expressed with the Pseudomonas sp. 61-3 PHA synthase gene (phaC2(Ps)) in E. coli W3110, MCL-PHA composed mainly of 3-hydroxyoctanoate and 3-hydroxydecanoate was synthesized from sodium decanoate. When the fabG(Ec) gene and the phaC2(Ps) gene were co-expressed in the fadA mutant E. coli strain WA101, MCL-PHA rich in 3-hydroxydecanoate monomer up to 93 mol% was accumulated from sodium decanoate. This was possible by efficiently redirecting 3-ketoacyl-coenzymes A from the beta-oxidation pathway to the PHA biosynthesis pathway without losing two carbon units, the strategy of which can be extended for the production of MCL-PHAs rich in other specific monomers.     

Metabolic engineering of Escherichia coli for the production of succinic acid from glucose

Bio-based succinate production from renewable resources has prospective economic and environmental benefits that caused heightened interest towards the study of succinate-producing microorganisms. The pathways of succinate formation have been well studied, and microorganisms that are capable of biomass convertion into the target substance (bacteria of the genera Actinobacillus, Anaerobiospirillum, and Mannheimia) have been isolated and characterized; however, the realization of economically feasible industrial processes using native producers still remains a challenge. Traditionally, the Escherichia coli bacterium has been used as a workhouse to develop new processes for the biosynthesis of many valuable chemicals due to the extensive knowledge of its metabolism, available genetic tools, and good growth characteristics, combined with low nutrient requirements. This review is focused on modern rational approaches to the construction of recombinant E. coli strains that efficiently produce succinic acid from glucose.     

A metabolic model of cellular energetics and carbon flux during aerobic Escherichia coli fermentation

An integrated metabolic model for the production of acetate by Escherichia coli growing on glucose under aerobic conditions was presented previously (Ko et al., 1993). The resulting model equations can be used to explain phenomena often observed with industrial fermentations, i.e., increased acetate production which follows from high glucose uptake rate, a low dissolved oxygen concentration, a high specific growth rate, or a combination of these conditions. However, several questions still need to be addressed. First, cell composition is growth rate and media dependent. Second, the macromolecular composition varied between E. coli strains. And finally, a model that represents the carbon fluxes between the Embden-Meyerhof-Parnas (EMP) and the hexose monophosphate (HMP) pathways when cells are subject to internal and/or external stresses is still not well defined. In the present work, we have made an effort to account for these effects, and the resulting model equations show good agreement for wild-type and recombinant E. coli experimental data for the acetate concentration, the onset of acetate secretion, and cell yield based on glucose. These results are useful for optimizing aerobic E. coli fermentation processes. More specifically, we have determined the EMP pathway carbon flux profiles required by the integrated metabolic model for an accurate fit of the acetic acid profile data from a wild-type E. coli strain ML308. These EMP carbon flux profiles were correlated with a dimensionless measurement of biomass and then used to predict the acetic acid profiles for E. coli strain F-122 expressing human immunodeficiency virus-(HIV(528)) beta-galactosidase fusion protein. The effect of different macromolecular compositions and growth rates between these two E. coli strains required a constant scaling factor for improved quantitative predictions.     

Carbon dioxide increases acid resistance in Escherichia coli

AIMS: To investigate how carbon dioxide affects the acid resistance of Escherichia coli. METHODS AND RESULTS: Escherichia coli W3110 was grown in minimal EG medium at pH 7.5, and cells were adapted at pH 5.5 at 37 degrees C with and without supply of carbon dioxide and nitrogen gases. The number of colonies grown on LB medium was measured after cells were challenged in minimal EG medium of pH 2.5 at 37 degrees C under various conditions. When carbon dioxide was supplied at both the acid adaptation and challenge stages, 94% of cells survived after the acid challenge for 1 h, while the survival rates were 50 and 67% when nitrogen gas and glutamate were supplied respectively. After the acid challenge for 3 h, the survival rate observed with the carbon dioxide gas supply was again 2.5-fold higher than those with the nitrogen gas supply. CONCLUSION: Carbon dioxide was shown to participate in the maintenance of high viability under acidic conditions. SIGNIFICANCE AND IMPACT OF THE STUDY: This study provides useful information for research into bacterial pathogenesis, fermentation and food preservation.     

Process development of succinic acid production by Escherichia coli NZN111 using acetate as an aerobic carbon source

Escherichia coli strain NZN111 could convert glucose to succinic acid efficiently in anaerobic conditions after the induction of gluconeogenic carbon sources in aerobic conditions. Acetate shows a strong effect on both yield and productivity of succinic acid. In this study, the fed-batch process of succinic acid production by NZN111 using acetate in a chemically defined medium in the aerobic stage was investigated and developed. Increasing cell density could increase succinic acid with a productivity of 3.97 g/(L h) in the first 8 h of the anaerobic phase with an overall yield of 1.42 mol/mol glucose in a 5 L fermentor. However, there was strong repression from succinic acid in the later anaerobic stage. When succinic acid exceeded 30 g/L, the glucose consumption rate began to drop sharply along with the succinic acid production rate. Supplementation with glucose from 30 to 70 g/L in the anaerobic stage showed little effect on succinic acid production. Acetic acid and pyruvic acid accumulated had no effect on succinic acid formation because of their low concentration. With acetate as the sole carbon source for aerobic cultivation in the following scale-up, 60.09 g/L of succinic acid was produced with a yield of 1.37 mol/mol in a 50 L bioreactor.     

Inhibition of succinic acid production in metabolically engineered Escherichia coli by neutralizing agent,organic acids,and osmolarity

The economical viability of biochemical succinic acid production is a result of many processing parameters including final succinic acid concentration, recovery of succinate, and the volumetric productivity. Maintaining volumetric productivities >2.5 g L^?1 h^?1 is important if production of succinic acid from renewable resources should be competitive. In this work, the effects of organic acids, osmolarity, and neutralizing agent (NH₄OH, KOH, NaOH, K₂CO₃, and Na₂CO₃) on the fermentative succinic acid production by Escherichia coli AFP184 were investigated. The highest concentration of succinic acid, 77 g L^?1, was obtained with Na₂CO₃. In general, irrespective of the base used, succinic acid productivity per viable cell was significantly reduced as the concentration of the produced acid increased. Increased osmolarity resulting from base addition during succinate production only marginally affected the productivity per viable cell. Addition of the osmoprotectant glycine betaine to cultures resulted in an increased aerobic growth rate and anaerobic glucose consumption rate, but decreased succinic acid yield. When using NH₄OH productivity completely ceased at a succinic acid concentration of ～40 g L^?1. Volumetric productivities remained at 2.5 g L^?1 h^?1 for up to 10 h longer when K‐ or Na‐bases where used instead of NH₄OH. The decrease in cellular succinic acid productivity observed during the anaerobic phase was found to be due to increased organic acid concentrations rather than medium osmolarity. © 2009 American Institute of Chemical Engineers Biotechnol. Prog., 2009     

Kinetic characterization in batch and continuous culture of Escherichia coli mutants affected in phosphoenolpyruvate metabolism: differences in acetic acid production

The growth kinetics of an Escherichia coli wild type strain and two derivative mutants were examined in batch cultures and in glucose-limited chemostats. One mutant (PB12) had an inactive phosphotranferase transport system and the other (PB25) had interrupted pykA and pykF genes that code for the two pyruvate kinase isoenzymes. In both batch and continuous culture, important differences in acetic acid accumulation and other metabolic activities were found. Compared to the wild type strain, we observed a reduction in acetic acid accumulation of 25 and 80% in PB25 and PB12 strains respectively, in batch culture. Continuous culture experiments revealed that compared to the other two strains, PB25 accumulated less acetic acid as a function of dilution rate. In continuous cultures, oxidoreductase metabolic activities were substantially affected in the two mutant strains. These changes in turn were reflected in different levels of biomass and CO₂ production, and in oxygen consumption.     

Use of glucose starvation to limit growth and induce protein production in Escherichia coli

The use of glucose starvation to uncouple the production of recombinant beta-galactosidase from cell growth in Escherichia coli was investigated. A lacZ operon fusion to the carbon starvation-inducible cst-1 locus was used to control beta-galactosidase synthesis. beta-Galactosidase induction was observed only under aerobic starvation conditions, and its expression continued for 6 h following the onset of glucose starvation. The cessation of beta-galactosidase expression closely correlated with the exhaustion of acetate, an overflow metabolite of glucose, from the culture medium. Our results suggest the primary role of acetate in cst-1-controlled protein expression is that of an energy source. Using this information, we metered acetate to a glucose-starved culture and produced a metabolically sluggish state, where growth was limited to a low linear rate and production of recombiant beta-galactosidase occurred continuously throughout the experiment. The cst-1 controlled beta-galactosidase synthesis was also induced at low dilution rates in a glucose-limited chemostat, suggesting possible applications to high-density cell systems such as glucose-limited recycle reactors. This work demonstrates that by using an appropriate promoter system and nutrient limitation, growth can be restrained while recombinant protein production is induced and maintained.     

Effects of redox potential control on succinic acid production by engineered Escherichia coli under anaerobic conditions

The effects of oxido-reduction potential (ORP) control on succinic acid production have been investigated in Escherichia coli LL016. In LL016, two CO₂ fixation pathways were achieved and NAD⁺ supply was enhanced by co-expression of heterologous pyruvate carboxylase (PYC) and nicotinic acid phosphoribosyltransferase (NAPRTase). During anaerobic fermentation, cell growth and metabolite distribution were changed with redox potential levels in the range of −200 to −400 mV. From the results, the ORP level of −400 mV was preferable, which resulted in the high succinic acid concentration (28.6 g/L) and high succinic acid productivity (0.33 g/L/h). Meanwhile, the yield of succinic acid at the ORP level of −400 mV was 39% higher than that at the ORP level of −200 mV. In addition, a higher NADH/NAD⁺ ratio and increased enzyme activities were also achieved by regulating the culture to a more reductive environment, which further enhanced the succinic acid production.     

Metabolic engineering of l-leucine production in Escherichia coli and Corynebacterium glutamicum: a review

l-Leucine, as an essential branched-chain amino acid for humans and animals, has recently been attracting much attention because of its potential for a fast-growing market demand. The applicability ranges from flavor enhancers, animal feed additives and ingredients in cosmetic to specialty nutrients in pharmaceutical and medical fields. Microbial fermentation is the major method for producing l-leucine by using Escherichia coli and Corynebacterium glutamicum as host bacteria. This review gives an overview of the metabolic pathway of l-leucine (i.e. production, import and export systems) and highlights the main regulatory mechanisms of operons in E. coli and C. glutamicum l-leucine biosynthesis. We summarize here the current trends in metabolic engineering techniques and strategies for manipulating l-leucine producing strains. Finally, future perspectives to construct industrially advantageous strains are considered with respect to recent advances in biology.     

Fermentation of sugar mixtures using Escherichia coli catabolite repression mutants engineered for production of L-lactic acid

Conversion of lignocellulose to lactic acid requires strains capable of fermenting sugar mixtures of glucose and xylose. Recombinant Escherichia coli strains were engineered to selectively produce L-lactic acid and then used to ferment sugar mixtures. Three of these strains were catabolite repression mutants (ptsG ⁻) that have the ability to simultaneously ferment glucose and xylose. The best results were obtained for ptsG ⁻ strain FBR19. FBR19 cultures had a yield of 0.77 (g lactic acid/g added sugar) when used to ferment a 100 g/l total equal mixture of glucose and xylose. The strain also consumed 75% of the xylose. In comparison, the ptsG ⁺ strains had yields of 0.47–0.48 g/g and consumed 18–22% of the xylose. FBR19 was subsequently used to ferment a variety of glucose (0–40 g/l) and xylose (40 g/l) mixtures. The lactic acid yields ranged from 0.74 to 1.00 g/g. Further experiments were conducted to discover the mechanism leading to the poor yields for ptsG ⁺ strains. Xylose isomerase (XI) activity, a marker for induction of xylose metabolism, was monitored for FBR19 and a ptsG ⁺ control during fermentations of a sugar mixture. Crude protein extracts prepared from FBR19 had 10–12 times the specific XI activity of comparable samples from ptsG ⁺ strains. Therefore, higher expression of xylose metabolic genes in the ptsG ⁻ strain may be responsible for superior conversion of xylose to product compared to the ptsG ⁺ fermentations. Received 14 December 2000/ Accepted in revised form 28 June 2002     

大肠杆菌L-色氨酸合成的代谢流分析简

目的：从代谢流的层面研究育种过程中基因操作对色氨酸积累的影响,为色氨酸菌种选育的设计思路提供理论指导和验证。方法：根据实验菌株的代谢特点构建￡一色氨酸代谢网络图,对出发菌株TRTH0709,及其重组菌株TRTH1013、TRTH1105和TRTH1107在30L发酵罐中进行分批流加发酵试验,在发酵进入稳定期后的26．28h,分别检测主要胞外代谢物的浓度并计算变化速率。结果和结论：得到了各菌株在拟稳态下的代谢流分布图。转酮酶基因（tktA）和磷酸烯醇式丙酮酸合成酶基因（ppsA）过表达能显著影响中心代谢途径,使代谢流向有利于色氨酸合成的方向改变,贮碳因子基因（csrA）敲除的影响较小,但在tktA和ppsA过表达质粒存在的情况下对色氨酸合成的代谢流有明显的促进作用。进一步的菌种改造仍有待进行,葡萄糖转运系统的替代和三羧酸循环的减弱是主要方向。     

An integrated metabolic modeling approach to describe the energy efficiency of Escherichia coli fermentations under oxygen-limited conditions: Cellular energetics, carbon flux, and acetate production

An integrated metabolic model for the production of acetate by growing Escherichia coli on glucose under aerobic conditions is presented. The model is based on parameters which are easily determined by experiments. Forming the basis for this integrated metabolic model are the 12 principal precursor metabolites for biosynthetic pathways, the Embden-Meyerhof-Parnas pathway, the pentose phosphate cycle, the tricarboxylic acid cycle and the anapleurotic reactions, the Crabtree effect, the Pasteur effect, and the details of bacterial respiration. The result can be used to explain phenomena often observed in industrial fermentations, i.e., increased acetate production which follows from high glucose uptake rate, a low oxygen concentration, a high specific growth rate, or a combination of these conditions. (c) 1993 John Wiley & Sons, Inc.     

Applicability of CoA/acetyl-CoA manipulation system to enhance isoamyl acetate production in Escherichia coli

Coenzyme A (CoA) and its thioester derivatives are important precursor molecules for many industrially useful compounds such as esters, PHBs, lycopene and polyketides. Previously, in our lab we could increase the intracellular levels of CoA and acetyl-Coenzyme A (acetyl-CoA) by overexpressing one of the upstream rate-controlling enzymes pantothenate kinase with a concomitant supplementation of the precursor pantothenic acid to the cell culture medium. In this study, we showed that the CoA/acetyl-CoA manipulation system could be used to increase the productivity of industrially useful compounds derived from acetyl-CoA. We chose the production of isoamyl acetate as a model system. Isoamyl acetate is an important flavor component of sake yeast and holds a great commercial value. Alcohol acetyl transferase (AAT) condenses isoamyl alcohol and acetyl-CoA to produce isoamyl acetate. The gene ATF2, coding for this AAT was cloned and expressed in Escherichia coli. This genetic engineered E. coli produces isoamyl acetate, an ester, from intracellular acetyl-CoA when isoamyl alcohol is added externally to the cell culture medium. In the current study, we showed that in a strain bearing ATF2 gene, an increase in intracellular CoA/acetyl-CoA by overexpressing panK leads to an increase in isoamyl acetate production. Additionally, the cofactor manipulation technique was combined with more traditional approach of competing pathway deletions to further increase isoamyl acetate production. The acetate production pathway competes with isoamyl acetate production for the common intracellular metabolite acetyl-CoA. Earlier we have shown that acetate pathway deletion (ackA-pta) increases isoamyl acetate production. The acetate production pathway was inactivated under elevated CoA/acetyl-CoA conditions, which lead to a further increase in isoamyl acetate production.