Engineering <Emphasis Type="Italic">Corynebacterium glutamicum</Emphasis> for the production of pyruvate

A Corynebacterium glutamicum strain with inactivated pyruvate dehydrogenase complex and a deletion of the gene encoding the pyruvate:quinone oxidoreductase produces about 19 mM l-valine, 28 mM l-alanine and about 55 mM pyruvate from 150 mM glucose. Based on this double mutant C. glutamicum △aceE △pqo, we engineered C. glutamicum for efficient production of pyruvate from glucose by additional deletion of the ldhA gene encoding NAD⁺-dependent l-lactate dehydrogenase (LdhA) and introduction of a attenuated variant of the acetohydroxyacid synthase (△C–T IlvN). The latter modification abolished overflow metabolism towards l-valine and shifted the product spectrum to pyruvate production. In shake flasks, the resulting strain C. glutamicum △aceE △pqo △ldhA △C–T ilvN produced about 190 mM pyruvate with a Y _P/S of 1.36 mol per mol of glucose; however, it still secreted significant amounts of l-alanine. Additional deletion of genes encoding the transaminases AlaT and AvtA reduced l-alanine formation by about 50%. In fed-batch fermentations at high cell densities with adjusted oxygen supply during growth and production (0–5% dissolved oxygen), the newly constructed strain C. glutamicum △aceE △pqo △ldhA △C–T ilvN △alaT △avtA produced more than 500 mM pyruvate with a maximum yield of 0.97 mol per mole of glucose and a productivity of 0.92 mmol g_(CDW)⁻¹ h⁻¹ (i.e., 0.08 g g_(CDW) ⁻¹ h⁻¹) in the production phase.     

Directed Evolution and Structural Analysis of NADPH-Dependent Acetoacetyl Coenzyme A (Acetoacetyl-CoA) Reductase from Ralstonia eutropha Reveals Two Mutations Responsible for Enhanced Kinetics

NADPH-dependent acetoacetyl-coenzyme A (acetoacetyl-CoA) reductase (PhaB) is a key enzyme in the synthesis of poly(3-hydroxybutyrate) [P(3HB)], along with β-ketothiolase (PhaA) and polyhydroxyalkanoate synthase (PhaC). In this study, PhaB from Ralstonia eutropha was engineered by means of directed evolution consisting of an error-prone PCR-mediated mutagenesis and a P(3HB) accumulation-based in vivo screening system using Escherichia coli. From approximately 20,000 mutants, we obtained two mutant candidates bearing Gln47Leu (Q47L) and Thr173Ser (T173S) substitutions. The mutants exhibited k_cat values that were 2.4-fold and 3.5-fold higher than that of the wild-type enzyme, respectively. In fact, the PhaB mutants did exhibit enhanced activity and P(3HB) accumulation when expressed in recombinant Corynebacterium glutamicum. Comparative three-dimensional structural analysis of wild-type PhaB and highly active PhaB mutants revealed that the beneficial mutations affected the flexibility around the active site, which in turn played an important role in substrate recognition. Furthermore, both the kinetic analysis and crystal structure data supported the conclusion that PhaB forms a ternary complex with NADPH and acetoacetyl-CoA. These results suggest that the mutations affected the interaction with substrates, resulting in the acquirement of enhanced activity.     

Direct production of cadaverine from soluble starch using <Emphasis Type="Italic">Corynebacterium glutamicum</Emphasis> coexpressing α-amylase and lysine decarboxylase

Here, we demonstrated the one-step production of cadaverine from starch using a Corynebacterium glutamicum strain coexpressing Streptococcus bovis 148 α-amylase (AmyA) and Escherichia coli K-12 lysine decarboxylase (CadA). We constructed the E. coli–C. glutamicum shuttle vector, which produces CadA under the control of the high constitutive expression (HCE) promoter, and transformed this vector into C. glutamicum CSS secreting AmyA. The engineered C. glutamicum expressed both CadA and AmyA, which retained their activity. We performed cadaverine fermentation using 50 g/l soluble starch as the sole carbon source without pyridoxal-5’-phosphate, which is the coenzyme for CadA. C. glutamicum coexpressing AmyA and CadA successfully produced cadaverine from soluble starch and the yield of cadaverine was 23.4 mM after 21 h. CadA expression levels under the control of the HCE promoter were assumed to be sufficient to convert l-lysine to cadaverine, as there was no accumulation of l-lysine in the culture medium during fermentation. Thus, we demonstrated that C. glutamicum has great potential to produce cadaverine from biomass resources.     

Identification of a suppressor gene for the arginine-auxotrophic <Emphasis Type="Italic">argJ</Emphasis> mutation in <Emphasis Type="Italic">Corynebacterium glutamicum</Emphasis>

We recently proposed a metabolic engineering strategy for l-ornithine production based on the hypothesis that an increased intracellular supply of N-acetylglutamate may further enhance l-ornithine production in a well-defined recombinant strain of Corynebacterium glutamicum. In this work, an argJ-deficient arginine auxotrophic mutant of C. glutamicum is suppressed by a different locus of C. glutamicum ATCC13032. Overexpression of the NCgl1469 open reading frame (ORF), exhibiting N-acetylglutamate synthase (NAGS) activity, was able to complement the C. glutamicum arginine-auxotrophic argJ strain and showed increased NAGS activity from 0.03 to 0.17 units mg⁻¹ protein. Additionally, overexpression of the NCgl1469 ORF resulted in a 39% increase in excreted l-ornithine. These results indicate that the intracellular supply of N-acetylglutamate is a rate-limiting step during l-ornithine production in C. glutamicum.     

Engineering of sugar metabolism of Corynebacterium glutamicum for production of amino acid l-alanine under oxygen deprivation

Corynebacterium glutamicum was genetically engineered to produce l-alanine from sugar under oxygen deprivation. The genes associated with production of organic acids in C. glutamicum were inactivated and the alanine dehydrogenase gene (alaD) from Lysinibacillus sphaericus was overexpressed to direct carbon flux from organic acids to alanine. Although the alaD-expressing strain produced alanine from glucose under oxygen deprivation, its productivity was relatively low due to retarded glucose consumption. Homologous overexpression of the gapA gene encoding glyceraldehyde 3-phosphate dehydrogenase (GAPDH) in the alaD-expressing strain stimulated glucose consumption and consequently improved alanine productivity. In contrast gapA overexpression did not affect glucose consumption under aerobic conditions, indicating that oxygen deprivation engendered inefficient regeneration of NAD⁺ resulting in impaired GAPDH activity and reduced glucose consumption in the alanine-producing strains. Inactivation of the alanine racemase gene allowed production of l-alanine with optical purity greater than 99.5%. The resulting strain produced 98 g l⁻¹ of l-alanine after 32 h in mineral salts medium. Our results show promise for amino acid production under oxygen deprivation.     

Biosynthesis of novel terpolymers poly(lactate-co-3-hydroxybutyrate-co-3-hydroxyvalerate)s in lactate-overproducing mutant Escherichia coli JW0885 by feeding propionate as a precursor of 3-hydroxyvalerate

Novel lactate (LA)-based terpolymers, P[LA-co-3-hydroxybutyrate(3HB)-co-3-hydroxyvalerate(3HV)]s (PLBVs), were produced in LA-overproducing mutant, Escherichia coli JW0885, which was found to be a superior host for the efficient production of LA-based polyesters. Recombinant E. coli JW0885 harboring the genes encoding LA-polymerizing enzyme (Ser325Thr/Gln481Lys mutant of polyhydroxyalkanoate synthase from Pseudomonas sp. 61-3) and three monomer supplying enzymes [propionyl-CoA transferase, β-ketothiolase, and nicotinamide adenine dinucleotide phosphate (reduced form) (NADPH)-dependent acetoacetyl-CoA reductase] was aerobically grown on glucose with feeding of propionate as a precursor of 3-hydroxyvaleryl-CoA (3HV-CoA). Gas chromatography and nuclear magnetic resonance (NMR) analyses revealed that polymers accumulated in the cells were composed of LA, 3HB, and 3HV units, thus being identified as terpolymers, PLBVs. In addition, ¹H-NMR analysis suggested the existence of LA-3HV sequence in the terpolymer. When 100 mg/l of sodium propionate was added into the medium, 3HV fraction in the terpolymer linearly reached up to 7.2 mol%, while LA fraction was inversely decreased. This phenomenon could be due to the change in metabolic fluxes of lactyl-CoA (LA-CoA) and 3HV-CoA depending on the concentration of propionate fed into the medium.     

Metabolic engineering of 1,2-propanediol pathways in <Emphasis Type="Italic">Corynebacterium glutamicum</Emphasis>

We analyzed 1,2-propanediol (1,2-PD) production in metabolically engineered Corynebacterium glutamicum. Wild-type C. glutamicum produced 93 μM 1,2-PD after 132 h incubation under aerobic conditions. No gene encoding the methylglyoxal synthase (MGS) which catalyzes the first step of 1,2-PD synthesis from the glycolytic pathway was detected on the C. glutamicum genome, but several genes annotated as encoding putative aldo-keto reductases (AKRs) were present. AKR functions as a methylglyoxal reductase in the 1,2-PD synthesis pathway. Expressing Escherichia coli mgs gene in C. glutamicum increased 1,2-PD yield 100-fold, suggesting that wild-type C. glutamicum carries the genes downstream of MGS in the 1,2-PD synthesis pathway. Furthermore, simultaneous overexpression of mgs and cgR_2242, one of the genes annotated as AKRs, enhanced 1,2-PD production to 24 mM. This work establishes that 1,2-PD synthesis by C. glutamicum, previously unknown, is possible.     

Metabolic engineering and flux analysis of <Emphasis Type="Italic">Corynebacterium glutamicum</Emphasis> for L-serine production

l-Serine plays a critical role as a building block for cell growth, and thus it is difficult to achieve the direct fermentation of l-serine from glucose. In this study, Corynebacterium glutamicum ATCC 13032 was engineered de novo by blocking and attenuating the conversion of l-serine to pyruvate and glycine, releasing the feedback inhibition by l-serine to 3-phosphoglycerate dehydrogenase (PGDH), in combination with the co-expression of 3-phosphoglycerate kinase (PGK) and feedback-resistant PGDH (PGDH^r). The resulting strain, SER-8, exhibited a lower specific growth rate and significant differences in l-serine levels from Phase I to Phase V as determined for fed-batch fermentation. The intracellular l-serine pool reached (14.22±1.41) μmol g_CDM ⁻¹, which was higher than glycine pool, contrary to fermentation with the wild-type strain. Furthermore, metabolic flux analysis demonstrated that the over-expression of PGK directed the flux of the pentose phosphate pathway (PPP) towards the glycolysis pathway (EMP), and the expression of PGDH^r improved the l-serine biosynthesis pathway. In addition, the flux from l-serine to glycine dropped by 24%, indicating that the deletion of the activator GlyR resulted in down-regulation of serine hydroxymethyltransferase (SHMT) expression. Taken together, our findings imply that l-serine pool management is fundamental for sustaining the viability of C. glutamicum, and improvement of C₁ units generation by introducing the glycine cleavage system (GCV) to degrade the excessive glycine is a promising target for l-serine production in C. glutamicum.     

D-lactic acid production by a genetically engineered strain <Emphasis Type="Italic">Corynebacterium glutamicum</Emphasis>

Based on its ability to produce lactic acid from glucose in mineral salt medium under anaerobic conditions, genetic modifications on Corynebacterium glutamicum Res 167 were carried out with the aim of producing optical pure D-lactic acid, involving the knockout of L-lactate dehydrogenase gene from C. glutamicum and the heterologous expression of D-lactate dehydrogenase gene from Lactobacillus bulgaricus into C. glutamicum. D-lactic acid production of the genetically engineered strain C. glutamicum Res 167Δldh/ldhA was 17.92 g/l (optical purity higher than 99.9%) after 16 h fermentation, which was 32.25% higher than the lactic acid production of the parental strain.     

Amino acid production from rice straw and wheat bran hydrolysates by recombinant pentose-utilizing <Emphasis Type="Italic">Corynebacterium glutamicum</Emphasis>

Corynebacterium glutamicum wild type lacks the ability to utilize the pentose fractions of lignocellulosic hydrolysates, but it is known that recombinants expressing the araBAD operon and/or the xylA gene from Escherichia coli are able to grow with the pentoses xylose and arabinose as sole carbon sources. Recombinant pentose-utilizing strains derived from C. glutamicum wild type or from the l-lysine-producing C. glutamicum strain DM1729 utilized arabinose and/or xylose when these were added as pure chemicals to glucose-based minimal medium or when they were present in acid hydrolysates of rice straw or wheat bran. The recombinants grew to higher biomass concentrations and produced more l-glutamate and l-lysine, respectively, than the empty vector control strains, which utilized the glucose fraction. Typically, arabinose and xylose were co-utilized by the recombinant strains along with glucose either when acid rice straw and wheat bran hydrolysates were used or when blends of pure arabinose, xylose, and glucose were used. With acid hydrolysates growth, amino acid production and sugar consumption were delayed and slower as compared to media with blends of pure arabinose, xylose, and glucose. The ethambutol-triggered production of up to 93 ± 4 mM l-glutamate by the wild type-derived pentose-utilizing recombinant and the production of up to 42 ± 2 mM l-lysine by the recombinant pentose-utilizing lysine producer on media containing acid rice straw or wheat bran hydrolysate as carbon and energy source revealed that acid hydrolysates of agricultural waste materials may provide an alternative feedstock for large-scale amino acid production.     

Direct production of L-lysine from raw corn starch by Corynebacterium glutamicum secreting Streptococcus bovis alpha-amylase using cspB promoter and signal sequence

Corynebacterium glutamicum is an important microorganism in the industrial production of amino acids. We engineered a strain of C. glutamicum that secretes α-amylase from Streptococcus bovis 148 (AmyA) for the efficient utilization of raw starch. Among the promoters and signal sequences tested, those of cspB from C. glutamicum possessed the highest expression level. The fusion gene was introduced into the homoserine dehydrogenase gene locus on the chromosome by homologous recombination. L-Lysine fermentation was conducted using C. glutamicum secreting AmyA in the growth medium containing 50 g/l of raw corn starch as the sole carbon source at various temperatures in the range 30 to 40°C. Efficient L-lysine production and raw starch degradation were achieved at 34 and 37°C, respectively. The α-amylase activity using raw corn starch was more than 2.5 times higher than that using glucose as the sole carbon source during L-lysine fermentation. AmyA expression under the control of cspB promoter was assumed to be induced when raw starch was used as the sole carbon source. These results indicate that efficient simultaneous saccharification and fermentation of raw corn starch to L-lysine were achieved by C. glutamicum secreting AmyA using the cspB promoter and signal sequence.     

Somatic embryo productions by liquid shake culture of embryogenic calluses in <Emphasis Type="Italic">Vigna mungo</Emphasis> (L.) Hepper

The regeneration of plants via somatic embryogenesis liquid shake culture of embryogenic calluses was achieved in Vigna mungo (L.) Hepper (blackgram). The production of embryogenic callus was induced by seeding primary leaf explants of V. mungo onto Murashige and Skoog (MS) (Physiol Plant 15:473–497, 1962) medium supplemented (optimally) with 1.5 mg/l 2,4-dichloro-phenoxyacetic acid. The embryogenic callus was then transferred to liquid MS medium supplemented (optimally) with 0.25 mg/l 2,4-dichloro-phenoxyacetic acid. Globular, heart-shaped, and torpedo-shaped embryos developed in liquid culture. The optimal carbohydrate source for production of somatic embryos was 3% sucrose (compared to glucose, fructose, and maltose). l-Glutamine (20 mg/l) stimulated the production of all somatic embryo stages significantly. Torpedo-shaped embryos were transferred to MS (Physiol Plant 15:473–497, 1962) liquid medium containing 0.5 mg/l abscisic acid to induce the maturation of cotyledonary-stage embryos. Cotyledonary-stage embryos were transferred to 1/2-MS semi-solid basal medium for embryo conversion. Approximately 1–1.5% of the embryos developed into plants.     

Production of <Emphasis Type="SmallCaps">d</Emphasis>-lactic acid by <Emphasis Type="Italic">Corynebacterium glutamicum</Emphasis> under oxygen deprivation

In mineral salts medium under oxygen deprivation, Corynebacterium glutamicum exhibits high productivity of l-lactic acid accompanied with succinic and acetic acids. In taking advantage of this elevated productivity, C. glutamicum was genetically modified to produce d-lactic acid. The modification involved expression of fermentative d-lactate dehydrogenase (d-LDH)-encoding genes from Escherichia coli and Lactobacillus delbrueckii in l-lactate dehydrogenase (l-LDH)-encoding ldhA-null C. glutamicum mutants to yield strains C. glutamicum ΔldhA/pCRB201 and C. glutamicum ΔldhA/pCRB204, respectively. The productivity of C. glutamicum ΔldhA/pCRB204 was fivefold higher than that of C. glutamicum ΔldhA/pCRB201. By using C. glutamicum ΔldhA/pCRB204 cells packed to a high density in mineral salts medium, up to 1,336 mM (120 g l⁻¹) of d-lactic acid of greater than 99.9% optical purity was produced within 30 h.     

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.     

Effect of pyruvate dehydrogenase complex deficiency on <Emphasis Type="SmallCaps">l</Emphasis>-lysine production with <Emphasis Type="Italic">Corynebacterium glutamicum</Emphasis>

Intracellular precursor supply is a critical factor for amino acid productivity of Corynebacterium glutamicum. To test for the effect of improved pyruvate availability on l-lysine production, we deleted the aceE gene encoding the E1p enzyme of the pyruvate dehydrogenase complex (PDHC) in the l-lysine-producer C. glutamicum DM1729 and characterised the resulting strain DM1729-BB1 for growth and l-lysine production. Compared to the host strain, C. glutamicum DM1729-BB1 showed no PDHC activity, was acetate auxotrophic and, after complete consumption of the available carbon sources glucose and acetate, showed a more than 50% lower substrate-specific biomass yield (0.14 vs 0.33 mol C/mol C), an about fourfold higher biomass-specific l-lysine yield (5.27 vs 1.23 mmol/g cell dry weight) and a more than 40% higher substrate-specific l-lysine yield (0.13 vs 0.09 mol C/mol C). Overexpression of the pyruvate carboxylase or diaminopimelate dehydrogenase genes in C. glutamicum DM1729-BB1 resulted in a further increase in the biomass-specific l-lysine yield by 6 and 56%, respectively. In addition to l-lysine, significant amounts of pyruvate, l-alanine and l-valine were produced by C. glutamicum DM1729-BB1 and its derivatives, suggesting a surplus of precursor availability and a further potential to improve l-lysine production by engineering the l-lysine biosynthetic pathway. This study is dedicated to Prof. Dr. Hermann Sahm on the occasion of his 65th birthday.     

Engineering <Emphasis Type="Italic">Bacillus subtilis</Emphasis> for isobutanol production by heterologous Ehrlich pathway construction and the biosynthetic 2-ketoisovalerate precursor pathway overexpression

In the present work, Bacillus subtilis was engineered as the cell factory for isobutanol production due to its high tolerance to isobutanol. Initially, an efficient heterologous Ehrlich pathway controlled by the promoter P₄₃ was introduced into B. subtilis for the isobutanol biosynthesis. Further, investigation of acetolactate synthase of B. subtilis, ketol-acid reductoisomerase, and dihydroxy-acid dehydratase of Corynebacterium glutamicum responsible for 2-ketoisovalerate precursor biosynthesis showed that acetolactate synthase played an important role in isobutanol biosynthesis. The overexpression of acetolactate synthase led to a 2.8-fold isobutanol production compared with the control. Apart from isobutanol, alcoholic profile analysis also confirmed the existence of 1.21 g/L ethanol, 1.06 g/L 2-phenylethanol, as well as traces of 2-methyl-1-butanol and 3-methyl-1-butanol in the fermentation broth. Under microaerobic condition, the engineered B. subtilis produced up to 2.62 g/L isobutanol in shake-flask fed-batch fermentation, which was 21.3% higher than that in batch fermentation.     

New ubiquitous translocators: amino acid export by<Emphasis Type="Italic"> Corynebacterium glutamicum</Emphasis> and<Emphasis Type="Italic"> Escherichia coli</Emphasis>

Molecular access to amino acid excretion by Corynebacterium glutamicum and Escherichia coli led to the identification of structurally novel carriers and novel carrier functions. The exporters LysE, RhtB, ThrE and BrnFE each represent the protoype of new transporter families, which are in part distributed throughout all of the kingdoms of life. LysE of C. glutamicum catalytes the export of basic amino acids. The expression of the carrier gene is regulated by the cell-internal concentration of basic amino acids. This serves, for example, to maintain homoeostasis if an excess of l-lysine or l-arginine inside the cell should arise during growth on complex media. RhtB is one of five paralogous systems in E. coli, of which at least two are relevant for l-threonine production. A third system is relevant for l-cysteine production. It is speculated that the physiological function of these paralogues is related to quorum sensing. ThrE of C. glutamicum exports l-threonine and l-serine. However, a ThrE domain with a putative hydrolytic function points to an as yet unknown role of this exporter. BrnFE in C. glutamicum is a two-component permease exporting branched-chained amino acids from the cell, and an orthologue in B. subtilis exports 4-azaleucine.     

Efficient (R)-3-hydroxybutyrate production using acetyl CoA-regenerating pathway catalyzed by coenzyme A transferase

(R)-3-hydroxybutyrate [(R)-3HB] is a useful precursor in the synthesis of value-added chiral compounds such as antibiotics and vitamins. Typically, (R)-3HB has been microbially produced from sugars via modified (R)-3HB-polymer-synthesizing pathways in which acetyl CoA is converted into (R)-3-hydroxybutyryl-coenzyme A [(R)-3HB-CoA] by β-ketothiolase (PhaA) and acetoacetyl CoA reductase (PhaB). (R)-3HB-CoA is hydrolyzed into (R)-3HB by modifying enzymes or undergoes degradation of the polymerized product. In the present study, we constructed a new (R)-3HB-generating pathway from glucose by using propionyl CoA transferase (PCT). This pathway was designed to excrete (R)-3HB by means of a PCT-catalyzed reaction coupled with regeneration of acetyl CoA, the starting substance for synthesizing (R)-3HB-CoA. Considering the equilibrium reaction of PCT, the PCT-catalyzed (R)-3HB production would be expected to be facilitated by the addition of acetate since it acts as an acceptor of CoA. As expected, the engineered Escherichia coli harboring the phaAB and pct genes produced 1.0 g?L^?1 (R)-3HB from glucose, and with the addition of acetate into the medium, the concentration was increased up to 5.2 g?L^?1, with a productivity of 0.22 g?L^?1 h^?1. The effectiveness of the extracellularly added acetate was evaluated by monitoring the conversion of ¹³C carbonyl carbon-labeled acetate into (R)-3HB using gas chromatography/mass spectrometry. The enantiopurity of (R)-3HB was determined to be 99.2% using chiral liquid chromatography. These results demonstrate that the PCT pathway achieved a rapid co-conversion of glucose and acetate into (R)-3HB.