<Emphasis Type="Italic">Corynebacterium glutamicum</Emphasis> tailored for high-yield L-valine production

We recently engineered the wild type of Corynebacterium glutamicum for the growth-decoupled production of L: -valine from glucose by inactivation of the pyruvate dehydrogenase complex and additional overexpression of the ilvBNCE genes, encoding the L-valine biosynthetic enzymes acetohydroxyacid synthase, isomeroreductase, and transaminase B. Based on the first generation of pyruvate-dehydrogenase-complex-deficient C. glutamicum strains, a second generation of high-yield L-valine producers was constructed by successive deletion of the genes encoding pyruvate:quinone oxidoreductase, phosphoglucose isomerase, and pyruvate carboxylase and overexpression of ilvBNCE. In fed-batch fermentations at high cell densities, the newly constructed strains produced up to 410 mM (48 g/l) L-valine, showed a maximum yield of 0.75 to 0.86 mol/mol (0.49 to 0.56 g/g) of glucose in the production phase and, in contrast to the first generation strains, excreted neither pyruvate nor any other by-product tested.     

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.     

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.     

Two-step production of gamma-aminobutyric acid from cassava powder using <Emphasis Type="Italic">Corynebacterium glutamicum</Emphasis> and <Emphasis Type="Italic">Lactobacillus plantarum</Emphasis>

Production of gamma-aminobutyric acid (GABA) from crop biomass such as cassava in high concentration is desirable, but difficult to achieve. A safe biotechnological route was investigated to produce GABA from cassava powder by C. glutamicum G01 and L. plantarum GB01-21. Liquefied cassava powder was first transformed to glutamic acid by simultaneous saccharification and fermentation with C. glutamicum G01, followed by biotransformation of glutamic acid to GABA with resting cells of L. plantarum GB01-21 in the reaction medium. After optimizing the reaction conditions, the maximum concentration of GABA reached 80.5 g/L with a GABA productivity of 2.68 g/L/h. This is the highest yield ever reported of GABA production from cassava-derived glucose. The bioprocess provides the added advantage of employing nonpathogenic microorganisms, C. glutamicum and L. plantarum, in microbial production of GABA from cassava biomass, which can be used in the food and pharmaceutical industries.     

Cyclohexanone-induced stress metabolism of <Emphasis Type="Italic">Escherichia coli</Emphasis> and <Emphasis Type="Italic">Corynebacterium glutamicum</Emphasis>

Solvent stress occurs during whole-cell biocatalysis of organic chemicals. Organic substrates and/or products may accumulate in the cellular membranes of whole cells, causing structural destabilization of the membranes, which leads to disturbances in cellular carbon and energy metabolism. Here, we investigate the effect of cyclohexanone on carbon metabolism in Escherichia coli BL21 and Corynebacterium glutamicum ATCC13032. Adding cyclohexanone to the culture medium (i.e., glucose mineral medium) resulted in a decreased specific growth rate and increased cellular maintenance energy in both strains of bacteria. Notably, carbon metabolism, which is mainly involved to increase cellular maintenance energy, was very different between the bacteria. Carbon flux into the acetic acid fermentation pathway was dominantly enhanced in E. coli, whereas the TCA cycle appeared to be activated in C. glutamicum. In fact, carbon flux into the TCA cycle in E. coli appeared to be reduced with increasing amounts of cyclohexanone in the culture medium. Metabolic engineering of E. coli cells to maintain or improve TCA cycle activity and, presumably, that of the electron transport chain, which are involved in regeneration of cofactors (e.g., NAD(P)H and ATP) and formation of toxic metabolites (e.g., acetic acid), may be useful in increasing solvent tolerance and biotransformation of organic chemicals (e.g., cyclohexanone).     

Native promoters of <Emphasis Type="Italic">Corynebacterium glutamicum</Emphasis> and its application in <Emphasis Type="SmallCaps">l</Emphasis>-lysine production

Objective

To identify useful native promoters of Corynebacterium glutamicum for fine-tuning of gene expression in metabolic engineering.

Results

Sixteen native promoters of C. glutamicum were characterized. These promoters covered a strength range of 31-fold with small increments and exhibited relatively stable activity during the whole growth phase using β-galactosidase as the reporter. The mRNA level and enzymatic activity of the lacZ reporter gene exhibited high correlation (R ² = 0.96) under the control of these promoters. Sequence analysis found that strong promoters had high similarity of the -10 hexamer to the consensus sequence and preference of the AT-rich UP element upstream the -35 region. To test the utility of the promoter library, the characterized native promoters were applied to modulate the sucCD-encoded succinyl-CoA synthetase expression for l-lysine overproduction.

Conclusions

The native promoters with various strengths realize the efficient and precise regulation of gene expression in metabolic engineering of C. glutamicum.

     

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.     

Updates on industrial production of amino acids using <Emphasis Type="Italic">Corynebacterium glutamicum</Emphasis>

l-Amino acids find various applications in biotechnology. l-Glutamic acid and its salts are used as flavor enhancers. Other l-amino acids are used as food or feed additives, in parenteral nutrition or as building blocks for the chemical and pharmaceutical industries. l-amino acids are synthesized from precursors of central carbon metabolism. Based on the knowledge of the biochemical pathways microbial fermentation processes of food, feed and pharma amino acids have been developed. Production strains of Corynebacterium glutamicum, which has been used safely for more than 50 years in food biotechnology, and Escherichia coli are constantly improved using metabolic engineering approaches. Research towards new processes is ongoing. Fermentative production of l-amino acids in the million-ton-scale has shaped modern biotechnology and its markets continue to grow steadily. This review focusses on recent achievements in strain development for amino acid production including the use of CRISPRi/dCas9, genome-reduced strains, biosensors and synthetic pathways to enable utilization of alternative carbon sources.     

Functional analysis of arabinofuranosidases and a xylanase of <Emphasis Type="Italic">Corynebacterium alkanolyticum</Emphasis> for arabinoxylan utilization in <Emphasis Type="Italic">Corynebacterium glutamicum</Emphasis>

Xylooligosaccharides (XOSs) and arabinoxylooligosaccharides (AXOSs) are major oligosaccharides derived from arabinoxylan. In our previous report, Corynebacterium glutamicum was engineered to utilize XOSs by introducing Corynebacterium alkanolyticum xyloside transporter and β-xylosidase. However, this strain was unable to consume AXOSs due to the absence of α-l-arabinofuranosidase activity. In this study, to confer AXOS utilization ability on C. glutamicum, two putative arabinofuranosidase genes (abf51A and abf51B) were isolated from C. alkanolyticum by the combination of degenerate PCR and genome walking methods. Recombinant Abf51A and Abf51B heterologously expressed in Escherichia coli showed arabinofuranosidase activities toward 4-nitrophenyl-α-l-arabinofuranoside with k _cat values of 150 and 63, respectively, with optimum at pH 6.0 to 6.5. However, Abf51A showed only a slight activity toward AXOSs and was more susceptible to product inhibition by arabinose and xylose than Abf51B. Introduction of abf51B gene into the C. glutamicum XOS-utilizing strain enabled it to utilize AXOSs as well as XOSs. The xylI gene encoding a putative xylanase was found upstream of the C. alkanolyticum xyloside transporter genes. A signal peptide was predicted at the N-terminus of the xylI-encoding polypeptide, which indicated XylI was a secreted protein. Recombinant mature XylI protein heterologously expressed in E. coli showed a xylanase activity toward xylans from various plant sources with optimum at pH 6.5, and C. glutamicum recombinant strain expressing native XylI released xylose, xylobiose, xylotriose, and arabino-xylobiose from arabinoxylan. Finally, introduction of the xylI gene into the C. glutamicum AXOS-utilizing strain enabled it to directly utilize arabinoxylan.     

<Emphasis Type="Italic">Corynebacterium glutamicum</Emphasis> possesses two <Emphasis Type="Italic">secA</Emphasis> homologous genes that are essential for viability

SecA is a central component of the bacterial Sec preprotein translocase. Besides the housekeeping SecA (SecA1), some mostly pathogenic Gram-positive bacteria possess an accessory SecA (SecA2) that is involved in the export of a few substrates only. Here we show that neither of the two secA homologous genes present in the genome of the non-pathogenic bacterium Corynebacterium glutamicum can be deleted, unless a copy of the respective gene is provided in trans on a plasmid. This finding is in marked contrast to all other cases examined so far making C. glutamicum the first reported bacterium possessing two essential SecA proteins.     

Double deletion of <Emphasis Type="Italic">dtsR1</Emphasis> and <Emphasis Type="Italic">pyc</Emphasis> induce efficient <Emphasis Type="SmallCaps">l</Emphasis>-glutamate overproduction in <Emphasis Type="Italic">Corynebacterium glutamicum</Emphasis>

Corynebacterium glutamicum strains are used for the fermentative production of l-glutamate. Five C. glutamicum deletion mutants were isolated by two rounds of selection for homologous recombination and identified by Southern blot analysis. The growth, glucose consumption and glutamate production of the mutants were analyzed and compared with the wild-type ATCC 13032 strain. Double disruption of dtsR1 (encoding a subunit of acetyl-CoA carboxylase complex) and pyc (encoding pyruvate carboxylase) caused efficient overproduction of l-glutamate in C. glutamicum; production was much higher than that of the wild-type strain and ΔdtsR1 strain under glutamate-inducing conditions. In the absence of any inducing conditions, the amount of glutamate produced by the double-deletion strain ΔdtsR1Δpyc was more than that of the mutant ΔdtsR1. The activity of phosphoenolpyruvate carboxylase (PEPC) was found to be higher in the ΔdtsR1Δpyc strain than in the ΔdtsR1 strain and the wild-type strain. Therefore, PEPC appears to be an important anaplerotic enzyme for glutamate synthesis in ΔdtsR1 derivatives. Moreover, this conclusion was confirmed by overexpression of ppc and pyc in the two double-deletion strains (ΔdtsR1Δppc and ΔdtsR1Δpyc), respectively. Based on the data generated in this investigation, we suggest a new method that will improve glutamate production strains and provide a better understanding of the interaction(s) between the anaplerotic pathway and fatty acid synthesis.     

Anaerobic growth and potential for amino acid production by nitrate respiration in <Emphasis Type="Italic">Corynebacterium glutamicum</Emphasis>

Oxygen limitation is a crucial problem in amino acid fermentation by Corynebacterium glutamicum. Toward this subject, our study was initiated by analysis of the oxygen-requiring properties of C. glutamicum, generally regarded as a strict aerobe. This organism formed colonies on agar plates up to relatively low oxygen concentrations (0.5% O₂), while no visible colonies were formed in the absence of O₂. However, in the presence of nitrate (), the organism exhibited limited growth anaerobically with production of nitrite (), indicating that C. glutamicum can use nitrate as a final electron acceptor. Assays of cell extracts from aerobic and hypoxic cultures yielded comparable nitrate reductase activities, irrespective of nitrate levels. Genome analysis revealed a narK2GHJI cluster potentially relevant to nitrate reductase and transport. Disruptions of narG and narJ abolished the nitrate-dependent anaerobic growth with the loss of nitrate reductase activity. Disruption of the putative nitrate/nitrite antiporter gene narK2 did not affect the enzyme activity but impaired the anaerobic growth. These indicate that this locus is responsible for nitrate respiration. Agar piece assays using l-lysine- and l-arginine-producing strains showed that production of both amino acids occurred anaerobically by nitrate respiration, indicating the potential of C. glutamicum for anaerobic amino acid production.     

Site-directed integration system using a combination of mutant <Emphasis Type="Italic">lox</Emphasis> sites for <Emphasis Type="Italic">Corynebacterium glutamicum</Emphasis>

The engineering of Corynebacterium glutamicum is important for enhanced production of biochemicals. To construct an optimal C. glutamicum genome, a precise site-directed gene integration method was developed by using a pair of mutant lox sites, one a right element (RE) mutant lox site and the other a left element (LE) mutant lox site. Two DNA fragments, 5.7 and 10.2 kb-long, were successfully integrated into the genome. The recombination efficiency of this system compared to that obtained by single crossover by homologous recombination was 2 orders of magnitude higher. Moreover, the integrated DNA remained stably maintained on removal of Cre recombinase. The Cre/mutant lox system thus represents a potentially attractive tool for integration of foreign DNA in the course of the engineering of C. glutamicum traits.     

An efficient succinic acid production process in a metabolically engineered <Emphasis Type="Italic">Corynebacterium glutamicum</Emphasis> strain

A Corynebacterium glutamicum strain (ΔldhA-pCRA717) that overexpresses the pyc gene encoding pyruvate carboxylase while simultaneously exhibiting a disrupted ldhA gene encoding l-lactate dehydrogenase was investigated in detail for succinic acid production. Succinic acid was shown to be efficiently produced at high-cell density under oxygen deprivation with intermittent addition of sodium bicarbonate and glucose. Succinic acid concentration reached 1.24 M (146 g l⁻¹) within 46 h. The yields of succinic acid and acetic acid from glucose were 1.40 mol mol⁻¹ (0.92 g g⁻¹) and 0.29 mol mol⁻¹ (0.10 g g⁻¹), respectively. The succinic acid production rate and yield depended on medium bicarbonate concentration rather than glucose concentration. Consumption of bicarbonate accompanied with succinic acid production implied that added bicarbonate was used for succinic acid synthesis.     

Engineering of an <Emphasis Type="SmallCaps">l</Emphasis>-arabinose metabolic pathway in <Emphasis Type="Italic">Corynebacterium glutamicum</Emphasis>

Corynebacterium glutamicum was metabolically engineered to broaden its substrate utilization range to include the pentose sugar l-arabinose, a product of the degradation of lignocellulosic biomass. The resultant CRA1 recombinant strain expressed the Escherichia coli genes araA, araB, and araD encoding l-arabinose isomerase, l-ribulokinase, and l-ribulose-5-phosphate 4-epimerase, respectively, under the control of a constitutive promoter. Unlike the wild-type strain, CRA1 was able to grow on mineral salts medium containing l-arabinose as the sole carbon and energy source. The three cloned genes were expressed to the same levels whether cells were cultured in the presence of d-glucose or l-arabinose. Under oxygen deprivation and with l-arabinose as the sole carbon and energy source, strain CRA1 carbon flow was redirected to produce up to 40, 37, and 11%, respectively, of the theoretical yields of succinic, lactic, and acetic acids. Using a sugar mixture containing 5% d-glucose and 1% l-arabinose under oxygen deprivation, CRA1 cells metabolized l-arabinose at a constant rate, resulting in combined organic acids yield based on the amount of sugar mixture consumed after d-glucose depletion (83%) that was comparable to that before d-glucose depletion (89%). Strain CRA1 is, therefore, able to utilize l-arabinose as a substrate for organic acid production even in the presence of d-glucose.     

Inhibitor-associated transposition events in<Emphasis Type="Italic"> Corynebacterium glutamicum</Emphasis>

In up to 100% of all bacteria grown in the presence of initially inhibitory concentrations of five diverse inhibitors, an extra copy of the resident insertion element IS31831 was found in specific chromosomal regions, the sites of which apparently depended on the inhibitor used. Thus, in nine out of nine independently isolated cyanide-associated transpositions, the acquired copy was located within an ORF encoding a protein related to the hypothetical but conserved protein YeiH of Escherichia coli. A putative Sox box upstream of the yeiH gene implicates superoxide as a potential regulator of the gene, a possibility further supported by the finding that superoxide dismutase (SodA) is overexpressed in cells cultured in cyanide-containing medium. Neither the cyanide-associated nor any of the other transposition mutations appeared to confer any discernible phenotypic advantage upon cells grown in the presence or absence of the inhibitors, as revealed most stringently by mixed-cell experiments. An alternative, albeit heterodox, explanation for the emergence of the mutants postulates a very high rate of transpositional activity in the presence of inhibitors. The initial emergence of the mutants was found to depend crucially upon the cell density. Thus, when growth medium was supplemented with 50 mM fluoropyruvate and inoculated to a density of 2×10⁷ cfu/ml, single colonies with heterogeneous restriction fragment length polymorphisms (RFLPs) were routinely isolated at a frequency of 6 to 16% after 1–2 days of incubation. After 3 days, 10–36% of the colonies showed RFLPs, but the type was now dominated by the fluoropyruvate-specific RFLP, which, at higher resolution, invariably proved to be heterogeneous. This heterogeneity proved that these specific mutants were of multiple origin, indicating that clonal enrichment was irrelevant to their emergence. It is suggested that the presence of the inhibitor induces the development of hyper-transpositional activity, which is regulated by a soluble bacterial product.Communicated by W. Arber     

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.