Improved succinate production in Corynebacterium glutamicum by engineering glyoxylate pathway and succinate export system

A dual route for anaerobic succinate production was engineered into Corynebacterium glutamicum. The glyoxylate pathway was reconstructed by overexpressing isocitrate lyase, malate synthase and citrate synthase. The engineered strain produced succinate with a yield of 1.34 mol (mol glucose)^?1. Further overexpression of succinate exporter, SucE, increased succinate yield to 1.43 mol (mol glucose)^?1. Metabolic flux analysis revealed that the glyoxylate pathway was further activated by engineering succinate export system. Using an anaerobic fed-batch fermentation process, the final strain produced 926 mM succinate (= 109 g l^?1) with an overall volumetric productivity of 9.4 mM h^?1 and an average yield of 1.32 mol (mol glucose)^?1.     

Phosphotransferase-dependent glucose transport in Corynebacterium glutamicum

G.M. MALIN AND G.I. BOURD. 1991. The transport system for glucose and its non-metabolizable analogue methyl-α-D-glucoside (MG) has been described in Corynebacterium glutamicum. The initial product of the transport reaction was shown to be a phosphate ester of MG (MGP). Free MG appeared inside the cells as a result of MGP dephosphorylation. The bacteria transported MG with an apparent K_m of 0.08 ± 0.017 mmol/l and V_max of 21 ± 2.3 nmol/(min × mg dry wt). Toluenized cells and crude cell extracts catalysed phosphoenolpyruvate (PEP)-dependent phosphorylation of MG and glucose. Both the membrane and the cytoplasmic fractions of bacterial extracts were required for phosphotransferase reaction. Most of the spontaneous mutants resistant to 2-deoxyglucose (DG), xylitol and 5-thioglucose were defective both in transport and in PEP-dependent phosphorylation of MG. Some strains were defective only in glucose utilization and some were also unable to grow on a number of other sugars. The phosphotransferase activity in extracts from mutant cells was restored by the addition of either membrane or cytoplasmic fraction from wild type bacteria. It was concluded that Corynebacterium glutamicum accumulated glucose and MG by means of a PEP-dependent phosphotransferase system (PTS).     

Biosynthesis of pinene from glucose using metabolically-engineered Corynebacterium glutamicum

Pinene is a monoterpenes (C₁₀) that is produced in a genetically-engineered microbial host for its industrial applications in fragrances, flavoring agents, pharmaceuticals, and biofuels. Herein, we have metabolically-engineered Corynebacterium glutamicum, to produce pinene and studied its toxicity in C. glutamicum. Geranyl diphosphate synthases (GPPS) and pinene synthases (PS), obtained from Pinus taeda and Abies grandis, were co-expressed with over-expressed native 1-deoxy-d-xylulose-5-phosphate synthase (Dxs) and isopentenyl diphosphate isomerase (Idi) from C. glutamicum using CoryneBrick vector. Most strains expressing PS-GPPSs produced detectable amounts of pinene, but co-expression of DXS and IDI with PS (P. taeda) and GPPS (A. grandis) resulted in 27 μg ± 7 α-pinene g^?1 cell dry weight, which is the first report in C. glutamicum. Further engineering of PS and GPPS in the C. glutamicum strain may increase pinene production.     

Glutamic acid production with gel-entrapped Corynebacterium glutamicum

A glutamic acid producing microorganism (Corynebacterium glutamicum) is entrapped in a polyacrylamide gel. These immobilized microorganisms were used to produce glutamic acid in successive batches of fresh medium. Free microorganisms similarly used produced much less glutamic acid under similar conditions.     

L-valine production with pyruvate dehydrogenase complex-deficient Corynebacterium glutamicum

Corynebacterium glutamicum was engineered for the production of L-valine from glucose by deletion of the aceE gene encoding the E1p enzyme of the pyruvate dehydrogenase complex and additional overexpression of the ilvBNCE genes encoding the L-valine biosynthetic enzymes acetohydroxyacid synthase, isomeroreductase, and transaminase B. In the absence of cellular growth, C. glutamicum DeltaaceE showed a relatively high intracellular concentration of pyruvate (25.9 mM) and produced significant amounts of pyruvate, L-alanine, and L-valine from glucose as the sole carbon source. Lactate or acetate was not formed. Plasmid-bound overexpression of ilvBNCE in C. glutamicum DeltaaceE resulted in an approximately 10-fold-lower intracellular pyruvate concentration (2.3 mM) and a shift of the extracellular product pattern from pyruvate and L-alanine towards L-valine. In fed-batch fermentations at high cell densities and an excess of glucose, C. glutamicum DeltaaceE(pJC4ilvBNCE) produced up to 210 mM L-valine with a volumetric productivity of 10.0 mM h(-1) (1.17 g l(-1) h(-1)) and a maximum yield of about 0.6 mol per mol (0.4 g per g) of glucose.     

Bio-based production of organic acids with Corynebacterium glutamicum

The shortage of oil resources, the steadily rising oil prices and the impact of its use on the environment evokes an increasing political, industrial and technical interest for development of safe and efficient processes for the production of chemicals from renewable biomass. Thus, microbial fermentation of renewable feedstocks found its way in white biotechnology, complementing more and more traditional crude oil-based chemical processes. Rational strain design of appropriate microorganisms has become possible due to steadily increasing knowledge on metabolism and pathway regulation of industrially relevant organisms and, aside from process engineering and optimization, has an outstanding impact on improving the performance of such hosts. Corynebacterium glutamicum is well known as workhorse for the industrial production of numerous amino acids. However, recent studies also explored the usefulness of this organism for the production of several organic acids and great efforts have been made for improvement of the performance. This review summarizes the current knowledge and recent achievements on metabolic engineering approaches to tailor C. glutamicum for the bio-based production of organic acids. We focus here on the fermentative production of pyruvate, l-and d-lactate, 2-ketoisovalerate, 2-ketoglutarate, and succinate. These organic acids represent a class of compounds with manifold application ranges, e.g. in pharmaceutical and cosmetics industry, as food additives, and economically very interesting, as precursors for a variety of bulk chemicals and commercially important polymers.Funding Information Work in the laboratories of the authors was supported by the Fachagentur Nachwachsende Rohstoffe (FNR) of the Bundesministerium für Ernährung, Landwirtschaft und Verbraucherschutz (BMELV; FNR Grants 220-095-08A and 220-095-08D; Bio-ProChemBB project, ERA-IB programme), by the Deutsche Bundesstiftung Umwelt (DBU Grant AZ13040/05) and the Evonik Degussa AG.     

Engineering Corynebacterium glutamicum for isobutanol production

The production of isobutanol in microorganisms has recently been achieved by harnessing the highly active 2-keto acid pathways. Since these 2-keto acids are precursors of amino acids, we aimed to construct an isobutanol production platform in Corynebacterium glutamicum, a well-known amino-acid-producing microorganism. Analysis of this host’s sensitivity to isobutanol toxicity revealed that C. glutamicum shows an increased tolerance to isobutanol relative to Escherichia coli. Overexpression of alsS of Bacillus subtilis, ilvC and ilvD of C. glutamicum, kivd of Lactococcus lactis, and a native alcohol dehydrogenase, adhA, led to the production of 2.6 g/L isobutanol and 0.4 g/L 3-methyl-1-butanol in 48 h. In addition, other higher chain alcohols such as 1-propanol, 2-methyl-1-butanol, 1-butanol, and 2-phenylethanol were also detected as byproducts. Using longer-term batch cultures, isobutanol titers reached 4.0 g/L after 96 h with wild-type C. glutamicum as a host. Upon the inactivation of several genes to direct more carbon through the isobutanol pathway, we increased production by ∼25% to 4.9 g/L isobutanol in a ∆pyc∆ldh background. These results show promise in engineering C. glutamicum for higher chain alcohol production using the 2-keto acid pathways.     

Putrescine production by engineered Corynebacterium glutamicum

Here, we report the engineering of the industrially relevant Corynebacterium glutamicum for putrescine production. C. glutamicum grew well in the presence of up to 500 mM of putrescine. A reduction of the growth rate by 34% and of biomass formation by 39% was observed at 750 mM of putrescine. C. glutamicum was enabled to produce putrescine by heterologous expression of genes encoding enzymes of the arginine- and ornithine decarboxylase pathways from Escherichia coli. The results showed that the putrescine yield by recombinant C. glutamicum strains provided with the arginine-decarboxylase pathway was 40 times lower than the yield by strains provided with the ornithine decarboxylase pathway. The highest production efficiency was reached by overexpression of speC, encoding the ornithine decarboxylase from E. coli, in combination with chromosomal deletion of genes encoding the arginine repressor ArgR and the ornithine carbamoyltransferase ArgF. In shake-flask batch cultures this strain produced putrescine up to 6 g/L with a space time yield of 0.1 g/L/h. The overall product yield was about 24 mol% (0.12 g/g of glucose).     

H+-ATPase defect in Corynebacterium glutamicum abolishes glutamic acid production with enhancement of glucose consumption rate

A mutant of Corynebacterim glutamicum ('Brevibacterium flayum') ATCC14067 with a reduced H+-ATPase activity, F172-8, was obtained as a spontaneous neomycin-resistant mutant. The ATPase activity of strain F172-8 was reduced to about 25% of that of the parental strain. Strain F172-8 was cultured in a glutamic-acid fermentation medium containing 100 g/l of glucose using ajar fermentor. It was found that glucose consumption per cell during the exponential phase was higher by 70% in the mutant than in the parent. The respiration rate per cell of the mutant also increased to twice as much as that of the parent. However, the growth rate of the mutant was lower than that of the parent. Under those conditions, the parent produced more than 40 g/l glutamic acid, while the mutant hardly produced any glutamic acid. Instead the mutant produced 24.6 g/l lactic acid as the main metabolite of glucose. Remarkably, the accumulation of pyruvate and pyruvate-family amino acids, i.e., alanine and valine, was detected in the mutant. On the other hand, the parent accumulated alpha-ketoglutaric acid and a glutamate-family amino acid, proline, as major by-products. It was concluded that the decrease in the H+-ATPase activity caused the above-mentioned metabolic changes in strain F172-8, because a revertant of strain F172-8, R2-1, with a H+-ATPase activity of 70% of that of strain ATCC14067, showed a fermentation profile similar to that of the parent. Sequence analyses of the atp operon genes of these strains identified one point mutation in the gamma subunit in strain F172-8.     

Detoxification of furfural in Corynebacterium glutamicum under aerobic and anaerobic conditions

The toxic fermentation inhibitors in lignocellulosic hydrolysates raise serious problems for the microbial production of fuels and chemicals. Furfural is considered to be one of the most toxic compounds among these inhibitors. Here, we describe the detoxification of furfural in Corynebacterium glutamicum ATCC13032 under both aerobic and anaerobic conditions. Under aerobic culture conditions, furfuryl alcohol and 2-furoic acid were produced as detoxification products of furfural. The ratio of the products varied depending on the initial furfural concentration. Neither furfuryl alcohol nor 2-furoic acid showed any toxic effect on cell growth, and both compounds were determined to be the end products of furfural degradation. Interestingly, unlike under aerobic conditions, most of the furfural was converted to furfuryl alcohol under anaerobic conditions, without affecting the glucose consumption rate. Both the NADH/NAD⁺ and NADPH/NADP⁺ ratio decreased in the accordance with furfural concentration under both aerobic and anaerobic conditions. These results indicate the presence of a single or multiple endogenous enzymes with broad and high affinity for furfural and co-factors in C. glutamicum ATCC13032.     

Corynebacterium glutamicum tailored for efficient isobutanol production

We recently engineered Corynebacterium glutamicum for aerobic production of 2-ketoisovalerate by inactivation of the pyruvate dehydrogenase complex, pyruvate:quinone oxidoreductase, transaminase B, and additional overexpression of the ilvBNCD genes, encoding acetohydroxyacid synthase, acetohydroxyacid isomeroreductase, and dihydroxyacid dehydratase. Based on this strain, we engineered C. glutamicum for the production of isobutanol from glucose under oxygen deprivation conditions by inactivation of l-lactate and malate dehydrogenases, implementation of ketoacid decarboxylase from Lactococcus lactis, alcohol dehydrogenase 2 (ADH2) from Saccharomyces cerevisiae, and expression of the pntAB transhydrogenase genes from Escherichia coli. The resulting strain produced isobutanol with a substrate-specific yield (Y_P/S) of 0.60 ± 0.02 mol per mol of glucose. Interestingly, a chromosomally encoded alcohol dehydrogenase rather than the plasmid-encoded ADH2 from S. cerevisiae was involved in isobutanol formation with C. glutamicum, and overexpression of the corresponding adhA gene increased the Y_P/S to 0.77 ± 0.01 mol of isobutanol per mol of glucose. Inactivation of the malic enzyme significantly reduced the Y_P/S, indicating that the metabolic cycle consisting of pyruvate and/or phosphoenolpyruvate carboxylase, malate dehydrogenase, and malic enzyme is responsible for the conversion of NADH+H⁺ to NADPH+H⁺. In fed-batch fermentations with an aerobic growth phase and an oxygen-depleted production phase, the most promising strain, C. glutamicum ΔaceE Δpqo ΔilvE ΔldhA Δmdh(pJC4ilvBNCD-pntAB)(pBB1kivd-adhA), produced about 175 mM isobutanol, with a volumetric productivity of 4.4 mM h⁻¹, and showed an overall Y_P/S of about 0.48 mol per mol of glucose in the production phase.     

Optimisation of a culture medium containing fish silage for L-lysine production by Corynebacterium glutamicum

In a first step the effects of 10 components of a culture medium designed for L-lysine production were evaluated with a 2(10-6) factorial design. Among them, glucose, fish silage, and ammonium sulphate showed a significant effect. In a second step, an orthogonal-central composite experimental design and response surface methodology was performed with five from the 10 initial compounds. The determination coefficient (R2) of the fitted second-order model was 0.990. L-lysine production with the optimised medium increased 2.6 times as compared with the original medium.     

Metabolic engineering of Corynebacterium glutamicum to produce GDP-l-fucose from glucose and mannose

Wild-type Corynebacterium glutamicum was metabolically engineered to convert glucose and mannose into guanosine 5′-diphosphate (GDP)-l-fucose, a precursor of fucosyl-oligosaccharides, which are involved in various biological and pathological functions. This was done by introducing the gmd and wcaG genes of Escherichia coli encoding GDP-d-mannose-4,6-dehydratase and GDP-4-keto-6-deoxy-d-mannose-3,5-epimerase-4-reductase, respectively, which are known as key enzymes in the production of GDP-l-fucose from GDP-d-mannose. Coexpression of the genes allowed the recombinant C. glutamicum cells to produce GDP-l-fucose in a minimal medium containing glucose and mannose as carbon sources. The specific product formation rate was much higher during growth on mannose than on glucose. In addition, the specific product formation rate was further increased by coexpressing the endogenous phosphomanno-mutase gene (manB) and GTP-mannose-1-phosphate guanylyl-transferase gene (manC), which are involved in the conversion of mannose-6-phosphate into GDP-d-mannose. However, the overexpression of manA encoding mannose-6-phosphate isomerase, catalyzing interconversion of mannose-6-phosphate and fructose-6-phosphate showed a negative effect on formation of the target product. Overall, coexpression of gmd, wcaG, manB and manC in C. glutamicum enabled production of GDP-l-fucose at the specific rate of 0.11 mg g cell^?1 h^?1. The specific GDP-l-fucose content reached 5.5 mg g cell^?1, which is a 2.4-fold higher than that of the recombinant E. coli overexpressing gmd, wcaG, manB and manC under comparable conditions. Well-established metabolic engineering tools may permit optimization of the carbon and cofactor metabolisms of C. glutamicum to further improve their production capacity.     

Modelling L-glutamic acid production with Corynebacterium glutamicum under biotin limitation

The production of L-glutamic acid with Corynebacterium glutamicum under biotin limitation was studied. Assuming a formal type of cell maturation, an adequate formal kinetic model was developed. This model includes growth, dependent on biotin, and uses the same retention term for describing the lag phase and cell maturation. Special attention was paid to the graphical interpretation of the performance between the variables, which is relevant for kinetics. Comparison between experiments and the model resulted in different degrees of agreement. However, the main trend of the experimental patterns of the complex bioprocess can clearly be mirrored in this model.     

L-Tyrosine production by Polyauxotrophic Mutants of Corynebacterium glutamicum

Polyauxotrophic mutants of Corynebacterium glutamicum which have additional requirements to L-phenylalanine were derived from L-tyrosine producing strains of phenylalanine auxotrophs, C. glutamicum KY 9189 and C. glutamicum KY 10233, and screened for L-tyrosine production. The increase of L-tyrosine production was noted in many auxotrophic mutants derived from both strains. Especially some double auxotrophs which require phenylalanine and purine, phenylalanine and histidine, or phenylalanine and cysteine produced significantly higher amounts of L-tyrosine compared to the parents, A phenylalanine and purine double auxotrophic strain LM–96 produced L-tyrosine at a concentration of 15.1 mg per ml in the medium containing 20% sucrose. L-Tyrosine production by the strain decreased at high concentrations of L-phenylalanine.