In silico deletion of PtsG gene in Escherichia coli genome-scale model predicts increased succinate production from glycerol

Systems metabolic engineering and in silico analyses are necessary to study gene knockout candidate for enhanced succinic acid production by Escherichia coli. Metabolically engineered E. coli has been reported to produce succinate from glucose and glycerol. However, investigation on in silico deletion of ptsG/b1101 gene in E. coli from glycerol using minimization of metabolic adjustment algorithm with the OptFlux software platform has not yet been elucidated. Herein we report what is to our knowledge the first direct predicted increase in succinate production following in silico deletion of the ptsG gene in E. coli GEM from glycerol with the OptFlux software platform. The result indicates that the deletion of this gene in E. coli GEM predicts increased succinate production that is 20% higher than the wild-type control model. Hence, the mutant model maintained a growth rate that is 77% of the wild-type parent model. It was established that knocking out of the ptsG/b1101 gene in E. coli using glucose as substrate enhanced succinate production, but the exact mechanism of this effect is still obscure. This study informs other studies that the deletion of ptsG/b1101 gene in E. coli GEM predicted increased succinate production, enabling a model-driven experimental inquiry and/or novel biological discovery on the underground metabolic role of this gene in E. coli central metabolism in relation to increasing succinate production when glycerol is the substrate.     

Expression of Galactose Permease and Pyruvate Carboxylase in Escherichia coli ptsG Mutant Increases the Growth Rate and Succinate Yield under Anaerobic Conditions

In Escherichia coli, disruption of ptsG, which encodes the glucose-specific permease of the phosphotransferase transport system (PTS) protein EIICB^Glc, is crucial for high succinate production. This mutation can, however, cause very slow growth and low glucose consumption rates. The ptsG mutant (TUQ2), from wild type E. coli W1485, and E. coli galP (encoding galactose permease) and glk (encoding glucose kinase) gene expression plasmids were constructed. TUQ2 increased the generation time to approximately 4 h and gave a higher final cell density of 0.5 g/l by expression of galP. However, glk expression had no effect on the mutant. After expression of pyruvate carboxylase (PYC) and galactose permease, the ptsG mutant showed higher succinate yield (1.2 mol/mol glucose) and the specific rate of glucose consumption from 0.33 to 0.6 g/1 h. Received 31 August 2005; Revisions requested 27 September 2005; Revisions received 1 November 2005; Accepted 2 November 2005 An erratum to this article is available at .     

Enhanced hydrogen production from glucose by metabolically engineered <Emphasis Type="Italic">Escherichia coli</Emphasis>

To utilize fermentative bacteria for producing the alternative fuel hydrogen, we performed successive rounds of P1 transduction from the Keio Escherichia coli K-12 library to introduce multiple, stable mutations into a single bacterium to direct the metabolic flux toward hydrogen production. E. coli cells convert glucose to various organic acids (such as succinate, pyruvate, lactate, formate, and acetate) to synthesize energy and hydrogen from formate by the formate hydrogen-lyase (FHL) system that consists of hydrogenase 3 and formate dehydrogenase-H. We altered the regulation of FHL by inactivating the repressor encoded by hycA and by overexpressing the activator encoded by fhlA, removed hydrogen uptake activity by deleting hyaB (hydrogenase 1) and hybC (hydrogenase 2), redirected glucose metabolism to formate by using the fdnG, fdoG, narG, focA, focB, poxB, and aceE mutations, and inactivated the succinate and lactate synthesis pathways by deleting frdC and ldhA, respectively. The best of the metabolically engineered strains, BW25113 hyaB hybC hycA fdoG frdC ldhA aceE, increased hydrogen production 4.6-fold from glucose and increased the hydrogen yield twofold from 0.65 to 1.3 mol H₂/mol glucose (maximum, 2 mol H₂/mol glucose).     

Fed-batch culture of Escherichia coli for L-valine production based on in silico flux response analysis

We have previously reported the development of a 100% genetically defined engineered Escherichia coli strain capable of producing L ‐valine from glucose with a high yield of 0.38 g L ‐valine per gram glucose (0.58 mol L ‐valine per mol glucose) by batch culture. Here we report a systems biological strategy of employing flux response analysis in bioprocess development using L ‐valine production by fed‐batch culture as an example. Through the systems‐level analysis, the source of ATP was found to be important for efficient L ‐valine production. There existed a trade‐off between L ‐valine production and biomass formation, which was optimized for the most efficient L ‐valine production. Furthermore, acetic acid feeding strategy was optimized based on flux response analysis. The final fed‐batch cultivation strategy allowed production of 32.3 g/L L ‐valine, the highest concentration reported for E. coli. This approach of employing systems‐level analysis of metabolic fluxes in developing fed‐batch cultivation strategy would also be applicable in developing strategies for the efficient production of other bioproducts. Biotechnol. Bioeng. 2011; 108:934–946. © 2010 Wiley Periodicals, Inc.     

A comparative study of glucose conversion to ethanol by Zymomonas mobilis and a recombinant Escherichia coli

Summary Zymomonas mobilis and recombinant Escherichia coli B (pLOI297) were compared in side-by-side batch fermentations using a synthetic cellulose hydrolysate (glucose/salts) medium with pH control at 6.0 and an inoculation cell density of 35–50 mg dry wt. cells/L. At a nominal glucose concentration of 6%, both cultures achieved near maximal theoretical ethanol yields; however, the Z. mobilis fermentation was complete at 13h compared to 33h for the E.coli fermentation. With approx.12% glucose, the Z. mobilis fermentation was complete in 20h with a process yield of 0.49 g ethanol/g added glucose compared to the E. coli fermentation which remained 20% incomplete after 6 days resulting in a process yield of only 0.32 g/g. Nutrient supplementation (10g tryptone/L) resulted in complete fermentation of 12% glucose (pH 6.3) by the recombinant E. coli in 4 days, with a yield of 0.48 g/g.     

An engineered non-oxidative glycolysis pathway for acetone production in <Emphasis Type="Italic">Escherichia coli</Emphasis>

Objectives

To find new metabolic engineering strategies to improve the yield of acetone in Escherichia coli.

Results

Results of flux balance analysis from a modified Escherichia coli genome-scale metabolic network suggested that the introduction of a non-oxidative glycolysis (NOG) pathway would improve the theoretical acetone yield from 1 to 1.5 mol acetone/mol glucose. By inserting the fxpk gene encoding phosphoketolase from Bifidobacterium adolescentis into the genome, we constructed a NOG pathway in E.coli. The resulting strain produced 47 mM acetone from glucose under aerobic conditions in shake-flasks. The yield of acetone was improved from 0.38 to 0.47 mol acetone/mol glucose which is a significant over the parent strain.

Conclusions

Guided by computational analysis of metabolic networks, we introduced a NOG pathway into E. coli and increased the yield of acetone, which demonstrates the importance of modeling analysis for the novel metabolic engineering strategies.

     

Metabolic evolution of two reducing equivalent-conserving pathways for high-yield succinate production in Escherichia coli

Reducing equivalents are an important cofactor for efficient synthesis of target products. During metabolic evolution to improve succinate production in Escherichia coli strains, two reducing equivalent-conserving pathways were activated to increase succinate yield. The sensitivity of pyruvate dehydrogenase to NADH inhibition was eliminated by three nucleotide mutations in the lpdA gene. Pyruvate dehydrogenase activity increased under anaerobic conditions, which provided additional NADH. The pentose phosphate pathway and transhydrogenase were activated by increased activities of transketolase and soluble transhydrogenase SthA. These data suggest that more carbon flux went through the pentose phosphate pathway, thus leading to production of more reducing equivalent in the form of NADPH, which was then converted to NADH through soluble transhydrogenase for succinate production. Reverse metabolic engineering was further performed in a parent strain, which was not metabolically evolved, to verify the effects of activating these two reducing equivalent-conserving pathways for improving succinate yield. Activating pyruvate dehydrogenase increased succinate yield from 1.12 to 1.31 mol/mol, whereas activating the pentose phosphate pathway and transhydrogenase increased succinate yield from 1.12 to 1.33 mol/mol. Activating these two pathways in combination led to a succinate yield of 1.5 mol/mol (88% of theoretical maximum), suggesting that they exhibited a synergistic effect for improving succinate yield.     

An antiphage Escherichia coli mutant for higher production of L-threonine obtained by atmospheric and room temperature plasma mutagenesis

Phage infection is common during the production of L-threonine by E. coli, and low L-threonine production and glucose conversion percentage are bottlenecks for the efficient commercial production of L-threonine. In this study, 20 antiphage mutants producing high concentration of L-threonine were obtained by atmospheric and room temperature plasma (ARTP) mutagenesis, and an antiphage E. coli variant was characterized that exhibited the highest production of L-threonine Escherichia coli ([E. coli] TRFC-AP). The elimination of fhuA expression in E. coli TRFC-AP was responsible for phage resistance. The biomass and cell growth of E. coli TRFC-AP showed no significant differences from those of the parent strain (E. coli TRFC), and the production of L-threonine (159.3 g L⁻¹) and glucose conversion percentage (51.4%) were increased by 10.9% and 9.1%, respectively, compared with those of E. coli TRFC. During threonine production (culture time of 20 h), E. coli TRFC-AP exhibited higher activities of key enzymes for glucose utilization (hexokinase, glucose phosphate dehydrogenase, phosphofructokinase, phosphoenolpyruvate carboxylase, and PYK) and threonine synthesis (glutamate synthase, aspartokinase, homoserine dehydrogenase, homoserine kinase and threonine synthase) compared to those of E. coli TRFC. The analysis of metabolic flux distribution indicated that the flux of threonine with E. coli TRFC-AP reached 69.8%, an increase of 16.0% compared with that of E. coli TRFC. Overall, higher L-threonine production and glucose conversion percentage were obtained with E. coli TRFC-AP due to increased activities of key enzymes and improved carbon flux for threonine synthesis.     

Escherichia coli yjjPB genes encode a succinate transporter important for succinate production

Under anaerobic conditions, Escherichia coli produces succinate from glucose via the reductive tricarboxylic acid cycle. To date, however, no genes encoding succinate exporters have been established in E. coli. Therefore, we attempted to identify genes encoding succinate exporters by screening an E. coli MG1655 genome library. We identified the yjjPB genes as candidates encoding a succinate transporter, which enhanced succinate production in Pantoea ananatis under aerobic conditions. A complementation assay conducted in Corynebacterium glutamicum strain AJ110655ΔsucE1 demonstrated that both YjjP and YjjB are required for the restoration of succinate production. Furthermore, deletion of yjjPB decreased succinate production in E. coli by 70% under anaerobic conditions. Taken together, these results suggest that YjjPB constitutes a succinate transporter in E. coli and that the products of both genes are required for succinate export.     

Metabolic flux balance analysis and the in silicoanalysis of Escherichia coliK-12 gene deletions

Background

Genome sequencing and bioinformatics are producing detailed lists of the molecular components contained in many prokaryotic organisms. From this 'parts catalogue' of a microbial cell, in silicorepresentations of integrated metabolic functions can be constructed and analyzed using flux balance analysis (FBA). FBA is particularly well-suited to study metabolic networks based on genomic, biochemical, and strain specific information.

Results

Herein, we have utilized FBA to interpret and analyze the metabolic capabilities of Escherichia coli. We have computationally mapped the metabolic capabilities of E. coliusing FBA and examined the optimal utilization of the E. colimetabolic pathways as a function of environmental variables. We have used an in silicoanalysis to identify seven gene products of central metabolism (glycolysis, pentose phosphate pathway, TCA cycle, electron transport system) essential for aerobic growth of E. colion glucose minimal media, and 15 gene products essential for anaerobic growth on glucose minimal media. The in silico tpi ^-, zwf, and pta ^-mutant strains were examined in more detail by mapping the capabilities of these in silicoisogenic strains.

Conclusions

We found that computational models of E. colimetabolism based on physicochemical constraints can be used to interpret mutant behavior. These in silicaresults lead to a further understanding of the complex genotype-phenotype relation. Supplementary information: 10.1186/1471-2105-1-1     

Redirecting carbon flux through <Emphasis Type="Italic">pgi</Emphasis>-deficient and heterologous transhydrogenase toward efficient succinate production in <Emphasis Type="Italic">Corynebacterium glutamicum</Emphasis>

Corynebacterium glutamicum is particularly known for its potentiality in succinate production. We engineered C. glutamicum for the production of succinate. To enhance C₃–C₄ carboxylation efficiency, chromosomal integration of the pyruvate carboxylase gene pyc resulted in strain NC-4. To increase intracellular NADH pools, the pntAB gene from Escherichia coli, encoding for transhydrogenase, was chromosomally integrated into NC-4, leading to strain NC-5. Furthermore, we deleted pgi gene in strain NC-5 to redirect carbon flux to the pentose phosphate pathway (PPP). To solve the drastic reduction of PTS-mediated glucose uptake, the ptsG gene from C. glutamicum, encoding for the glucose-specific transporter, was chromosomally integrated into pgi-deficient strain resulted in strain NC-6. In anaerobic batch fermentation, the production of succinate in pntAB-overexpressing strain NC-5 increased by 14% and a product yield of 1.22 mol/mol was obtained. In anaerobic fed-batch process, succinic acid concentration reached 856 mM by NC-6. The yields of succinate from glucose were 1.37 mol/mol accompanied by a very low level of by-products. Activating PPP and transhydrogenase in combination led to a succinate yield of 1.37 mol/mol, suggesting that they exhibited a synergistic effect for improving succinate yield.     

Identification of active constraints in dynamic flux balance analysis

This study deals with the calibration of dynamic metabolic flux models that are formulated as the maximization of an objective subject to constraints. Two approaches were applied for identifying the constraints from data. In the first approach a minimal active number of limiting constraints is found based on data that are assumed to be bounded within sets whereas, in the second approach, the limiting constraints are found based on parametric sensitivity analysis. The ability of these approaches to finding the active limiting constraints was verified through their application to two case studies: an in‐silico (simulated) data‐based study describing the growth of E. coli and an experimental data‐based study for Bordetella pertussis (B. pertussis). © 2016 American Institute of Chemical Engineers Biotechnol. Prog., 33:26–36, 2017     

Quantification and analysis of metabolic characteristics of aerobic succinate-producing Escherichia coli under different aeration conditions

The production of succinate by engineered Escherichia coli strains has been widely investigated. In this study, quantitative comparison of metabolic fluxes was carried out for the wild-type E. coli strain and a quintuple mutant strain QZ1111 that was designed for the production of succinate aerobically by knocking out five genes (ptsG, poxB, pta, sdhA, iclR) of the wild-type E. coli MG1655. Metabolic flux distributions of both strains were quantified by ¹³C-labeling experiments, together with the determination of physiological parameters and the expression level of key genes. The experimental results indicated that under the same aeration condition the fraction of oxaloacetate molecules originating from phosphoenolpyruvate was increased in E. coli QZ1111 compared to that in the wild-type E. coli MG1655. The glyoxylate shunt was likely activated in E. coli QZ1111 only under high aeration condition but repressed in other conditions, indicating that the deletion of the iclR gene could not completely remove the repression of the glyoxylate shunt with limited oxygen supply. Our results also suggested further genetic manipulation strategies to enhance the production yield of succinate.     

Mutation of the ptsG Gene Results in Increased Production of Succinate in Fermentation of Glucose by Escherichia coli

Escherichia coli NZN111 is blocked in the ability to grow fermentatively on glucose but gave rise spontaneously to a mutant that had this ability. The mutant carries out a balanced fermentation of glucose to give approximately 1 mol of succinate, 0.5 mol of acetate, and 0.5 mol of ethanol per mol of glucose. The causative mutation was mapped to the ptsG gene, which encodes the membrane-bound, glucose-specific permease of the phosphotransferase system, protein EIICB^glc. Replacement of the chromosomal ptsG gene with an insertionally inactivated form also restored growth on glucose and resulted in the same distribution of fermentation products. The physiological characteristics of the spontaneous and null mutants were consistent with loss of function of the ptsG gene product; the mutants possessed greatly reduced glucose phosphotransferase activity and lacked normal glucose repression. Introduction of the null mutant into strains not blocked in the ability to ferment glucose also increased succinate production in those strains. This phenomenon was widespread, occurring in different lineages of E. coli, including E. coli B.     

<Emphasis Type="Italic">In silico</Emphasis> improvement of heterologous biosynthesis of erythromycin precursor 6-deoxyerythronolide B in <Emphasis Type="Italic">Escherichia coli</Emphasis>

The heterologous biosynthesis of 6-deoxyerythronolide B (6dEB), a key intermediate in the biosynthesis of erythromycin, has recently been achieved in Escherichia coli, but the experimental product yield remains low. In this study, in silico strategies were adopted to evaluate and improve the biosynthesis of 6dEB in this strain. The theoretical capability of E. coli to produce 6dEB was first evaluated by analyzing the maximum theoretical molar yield (MTMY) of 6dEB utilizing three carbon sources, glucose, propionate and glycerol. Although propionate is presently most often used experimentally, our results indicated that glucose would be the most feasible substrate for 6dEB production from economic and long-term standpoints. Compared with Saccharomyces cerevisiae and Bacillus subtilis, E. coli was found to be a better heterologous host for the biosynthesis of 6dEB due to the higher MTMY value under the same conditions. Two strategies, including a flux distribution comparison analysis (FDCA) and linear minimization of metabolic adjustment based (LMOMA-based) methods, were proposed and employed for in silico strain improvement of 6dEB production, which yielded several potential gene targets for future experimental validation. In a further analysis, increasing the specific growth rate (SGR) or the non-growth associated maintenance (NGAM) was found to decrease the MTMY; while increasing the specific oxygen uptake rate (SOUR) or the specific carbon source uptake rate (SCUR) increased the MTMY. Taken together, our findings identified key factors directly affecting the MTMY of 6dEB production, which will guide future experimental research or even the industrial production of 6dEB.     

ATP limitation in a pyruvate formate lyase mutant of <Emphasis Type="Italic">Escherichia coli</Emphasis> MG1655 increases glycolytic flux to <Emphasis Type="SmallCaps">d</Emphasis>-lactate

A derivative strain of Escherichia coli MG1655 for d-lactate production was constructed by deleting the pflB, adhE and frdA genes; this strain was designated “CL3.” Results show that the CL3 strain grew 44% slower than its parental strain under nonaerated (fermentative) conditions due to the inactivation of the main acetyl-CoA production pathway. In contrast to E. coli B and W3110 pflB derivatives, we found that the MG1655 pflB derivative is able to grow in mineral media with glucose as the sole carbon source under fermentative conditions. The glycolytic flux was 2.8-fold higher in CL3 when compared to the wild-type strain, and lactate yield on glucose was 95%. Although a low cell mass formed under fermentative conditions with this strain (1.2 g/L), the volumetric productivity of CL3 was 1.31 g/L h. In comparison with the parental strain, CL3 has a 22% lower ATP/ADP ratio. In contrast to wild-type E. coli, the ATP yield from glucose to lactate is 2 ATP/glucose, so CL3 has to improve its glycolytic flux in order to fulfill its ATP needs in order to grow. The aceF deletion in strains MG1655 and CL3 indicates that the pyruvate dehydrogenase (PDH) complex is functional under glucose-fermentative conditions. These results suggest that the pyruvate to acetyl-CoA flux in CL3 is dependent on PDH activity and that the decrease in the ATP/ADP ratio causes an increase in the flux of glucose to lactate.     

Effect of different levels of NADH availability on metabolite distribution in <Emphasis Type="Italic">Escherichia coli</Emphasis> fermentation in minimal and complex media

A range of intracellular NADH availability was achieved by combining external and genetic strategies. The effect of these manipulations on the distribution of metabolites in Escherichia coli was assessed in minimal and complex medium under anoxic conditions. Our in vivo system to increase intracellular NADH availability expressed a heterologous NAD⁺-dependent formate dehydrogenase (FDH) from Candida boidinii in E. coli. The heterologous FDH pathway converted 1 mol formate into 1 mol NADH and carbon dioxide, in contrast to the native FDH where cofactor involvement was not present. Previously, we found that this NADH regeneration system doubled the maximum yield of NADH from 2 mol to 4 mol NADH/mol glucose consumed. In the current study, we found that yields of greater than 4 mol NADH were achieved when carbon sources more reduced than glucose were combined with our in vivo NADH regeneration system. This paper demonstrates experimentally that different levels of NADH availability can be achieved by combining the strategies of feeding the cells with carbon sources which have different oxidation states and regenerating NADH through the heterologous FDH pathway. The general trend of the data is substantially similar for minimal and complex media. The NADH availability obtained positively correlates with the proportion of reduced by-products in the final culture. The maximum theoretical yield for ethanol is obtained from glucose and sorbitol in strains overexpressing the heterologous FDH pathway.     

Enhanced hydrogen production from glucose using ldh- and frd-inactivated Escherichia coli strains

We improved the hydrogen yield from glucose using a genetically modified Escherichia coli. E. coli strain SR15 (ΔldhA, ΔfrdBC), in which glucose metabolism was directed to pyruvate formate lyase (PFL), was constructed. The hydrogen yield of wild-type strain of 1.08 mol/mol glucose, was enhanced to 1.82 mol/mol glucose in strain SR15. This figure is greater than 90 % of the theoretical hydrogen yield of facultative anaerobes (2.0 mol/mol glucose). Moreover, the specific hydrogen production rate of strain SR15 (13.4 mmol h⁻¹ g⁻¹ dry cell) was 1.4-fold higher than that of wild-type strain. In addition, the volumetric hydrogen production rate increased using the process where cells behaved as an effective catalyst. At 94.3 g dry cell/l, a productivity of 793 mmol h⁻¹ l⁻¹ (20.2 l h⁻¹ l⁻¹ at 37 °C) was achieved using SR15. The reported productivity substantially surpasses that of conventional biological hydrogen production processes and can be a trigger for practical applications.     

Heterologous production of 3-hydroxyvalerate in engineered Escherichia coli

3-Hydroxyacids are a group of valuable fine chemicals with numerous applications, and 3-hydroxybutyrate (3-HB) represents the most common species with acetyl-CoA as a precursor. Due to the lack of propionyl-CoA in most, if not all, microorganisms, bio-based production of 3-hydroxyvalerate (3-HV), a longer-chain 3-hydroxyacid member with both acetyl-CoA and propionyl-CoA as two precursors, is often hindered by high costs associated with the supplementation of related carbon sources, such as propionate or valerate. Here, we report the derivation of engineered Escherichia coli strains for the production of 3-HV from unrelated cheap carbon sources, in particular glucose and glycerol. Activation of the sleeping beauty mutase (Sbm) pathway in E. coli enabled the intracellular formation of non-native propionyl-CoA. A selection of enzymes involved in 3-HV biosynthetic pathway from various microorganisms were explored for investigating their effects on 3-HV biosynthesis in E. coli. Glycerol outperformed glucose as the carbon source, and glycerol dissimilation for 3-HV biosynthesis was primarily mediated through the aerobic GlpK-GlpD route. To further enhance 3-HV production, we developed metabolic engineering strategies to redirect more dissimilated carbon flux from the tricarboxylic acid (TCA) cycle to the Sbm pathway, resulting in an enlarged intracellular pool of propionyl-CoA. Both the presence of succinate/succinyl-CoA and their interconversion step in the TCA cycle were identified to critically limit the carbon flux redirection into the Sbm pathway and, therefore, 3-HV biosynthesis. A selection of E. coli host TCA genes encoding enzymes near the succinate node were targeted for manipulation to evaluate the contribution of the three TCA routes (i.e. oxidative TCA cycle, reductive TCA branch, and glyoxylate shunt) to the redirected carbon flux into the Sbm pathway. Finally, the carbon flux redirection into the Sbm pathway was enhanced by simultaneously deregulating glyoxylate shunt and blocking the oxidative TCA cycle, significantly improving 3-HV biosynthesis. With the implementation of these biotechnological and bioprocessing strategies, our engineered E. coli strains can effectively produce 3-HV up to 3.71 g l⁻¹ with a yield of 24.1% based on the consumed glycerol in shake-flask cultures.     

Model-based metabolic engineering enables high yield itaconic acid production by Escherichia coli

Itaconic acid is a high potential platform chemical which is currently industrially produced by Aspergillus terreus. Heterologous production of itaconic acid with Escherichia coli could help to overcome limitations of A. terreus regarding slow growth and high sensitivity to oxygen supply. However, the performance achieved so far with E. coli strains is still low.We introduced a plasmid (pCadCS) carrying genes for itaconic acid production into E. coli and applied a model-based approach to construct a high yield production strain. Based on the concept of minimal cut sets, we identified intervention strategies that guarantee high itaconic acid yield while still allowing growth. One cut set was selected and the corresponding genes were iteratively knocked-out. As a conceptual novelty, we pursued an adaptive approach allowing changes in the model and initially calculated intervention strategy if a genetic modification induces changes in byproduct formation. Using this approach, we iteratively implemented five interventions leading to high yield itaconic acid production in minimal medium with glucose as substrate supplemented with small amounts of glutamic acid. The derived E. coli strain (ita23: MG1655 ∆aceA ∆sucCD ∆pykA ∆pykF ∆pta ∆Picd::cam_BBa_J23115 pCadCS) synthesized 2.27 g/l itaconic acid with an excellent yield of 0.77 mol/(mol glucose). In a fed-batch cultivation, this strain produced 32 g/l itaconic acid with an overall yield of 0.68 mol/(mol glucose) and a peak productivity of 0.45 g/l/h. These values are by far the highest that have ever been achieved for heterologous itaconic acid production and indicate that realistic applications come into reach.