Metabolic design in the amino-acid-producing bacteriumCorynebacterium glutamicum

The Gram-positive bacteriumCorynebacterium glutamicum is used for the industrial production of amino acids,e.g. ofl-glutamate andl-lysine. By cloning and expressing the various genes of thel-lysine pathway inC. glutamicum we could demonstrate that an increase of the flux ofl-4-aspartaldehydate tol-lysine could be obtained in strains with increased dihydro-dipicolinate synthase activity. Recently we detected that inC. glutamicum two pathways exist for the synthesis ofdl-2,6-diaminopimelate andl-lysine. Mutants defective in one pathway are still able to synthesize enoughl-lysine for growth but thel-lysine secretion is reduced to 50–70%. Using NMR-spectroscopy we could calculate how much of thel-lysine secreted into the medium is synthesizedvia the one and the other pathway. Amplification of the feedback-inhibition-insensitive-homoserine dehydrogenase and homoserine kinase in a highl-lysine-overproducing strain made it possible to channell of the carbon flow from the intermediate 4-aspartaldehydate toward homoserine, resulting in a high accumulation ofl-threonine. For a further flux froml-threonine tol-isoleucine the allosteric control of threonine dehydratase was eliminated. Dedicated to Dr. Z. Vaněk on the occasion of his 70th birthday Presented at theIUMS Congresses '94-7th International Congress of Bacteriology and Applied Microbiology Division, Prague, July 3–8, 1994 (Bacteriological Symposium BS-12Regulation of Microbial Product Overproduction).     

Production of <Emphasis Type="SmallCaps">l</Emphasis>-Lysine from starch by <Emphasis Type="BoldItalic">Corynebacterium glutamicum</Emphasis> displaying α-amylase on its cell surface

We engineered a Corynebacterium glutamicum strain displaying α-amylase from Streptococcus bovis 148 (AmyA) on its cell surface to produce amino acids directly from starch. We used PgsA from Bacillus subtilis as an anchor protein, and the N-terminus of α-amylase was fused to the PgsA. The genes of the fusion protein were integrated into the homoserine dehydrogenase gene locus on the chromosome by homologous recombination. l-Lysine fermentation was carried out using C. glutamicum displaying AmyA in the growth medium containing 50 g/l soluble starch as the sole carbon source. We performed l-lysine fermentation at various temperatures (30–40°C) and pHs (6.0–7.0), as the optimal temperatures and pHs of AmyA and C. glutamicum differ significantly. The highest l-lysine yield was recorded at 30°C and pH 7.0. The amount of soluble starch was reduced to 18.29 g/l, and 6.04 g/l l-lysine was produced in 24 h. The l-lysine yield obtained using soluble starch as the sole carbon source was higher than that using glucose as the sole carbon source after 24 h when the same amount of substrates was added. The results shown in the current study demonstrate that C. glutamicum displaying α-amylase has a potential to directly convert soluble starch to amino acids.     

Feedback inhibition of homoserine dehydrogenase and threonine deaminase in the genusBifidobacterium

Feedback inhibition of crude and purified extracts of homoserine dehydrogenase and threonine deaminase activities in the genusBifidobacterium was studied. Homoserine dehydrogenase was partially or completely inhibited byl-threonine, and a marked inhibitory effect byl-isoleucine on threonine deaminase was observed. In the speciesBifidobacterium cuniculi high levels ofl-valine reversed the inhibitory effect ofl-isoleucine. The -aminobutyric acid-resistant mutant Ru 326/106 of the speciesB. ruminale, overproducer ofl-isoleucine, had a derepressed homoserine dehydrogenase and a lesser feedback inhibition byl-threonine. Homoserine dehydrogenase appeared to be in bifids specifically NAD dependent. The regulatory mechanisms of aspartate family amino acid biosynthesis in bifidobacteria was discussed.     

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.     

Regulation of acetohydroxy acid synthase in Corynebacterium glutamicum during fermentation of α-ketobutyrate to l-isoleucine

Summary Corynebacterium glutamicum ATCC 13 032 produces 13 g/l l-isoleucine from 200 mM -ketobutyrate as a synthetic precursor. In fed batch cultures up to 19 g/l l-isoleucine is formed. For optimal conversion the addition of 0.3 mM l-valine plus 0.3 mM l-leucine to the fermentation medium is required. The affinity constants for the acetohydroxy acid synthase (AHAS) were determined. (This enzyme directs the flow of -ketobutyrate plus pyruvate towards l-isoleucine and that of two moles of pyruvate to l-valine and l-leucine, respectively.) For -ketobutyrate the K _m is 4.8×10^-3 M, and V _max 0.58 U/mg, for pyruvate the K _m is 8.4×10^-3 M, and V _max 0.37 U/mg. Due to these characteristics the presence of high -ketobutyrate concentrations apparently results in a l-valine, l-leucine deficiency. This in turn leads to a derepression of the AHAS synthesis from 0.03 U/mg to 0.29 U/mg and high l-isoleucine production is favoured. The derepression of the AHAS synthesis induced by the l-valine, l-leucine shortage was directly proven with a l-valine, l-leucine, l-isoleucine auxotrophic mutant where the starvation of each amino acid resulted in an increased AHAS level. This is in accordance with the fact that only one AHAS enzyme could be verified by chromatographic and electrophoretic separations as being responsible for the synthesis of all three branched-chain amino-acids.     

Breeding ofl-threonine hyper-producer ofEscherichia coli W

Summary l-Threonine hyper-producing mutants were obtained fromEscherichia coli W strain KY-8366, by reducingl-threonine degradation activity and enhancingl-threonine biosynthetic activity. Anl-threonine degradation reaction test using resting cells of KY-8366 suggested that the main pathway ofl-threonine degradation by KY-8366 is via glycine. A strain with reducedl-threonine degradation activity was obtained among those mutants that could not utilizel-threonine as sole nitrogen source. Rifampicin-resistant mutants andl-lysine plus methionine-insentitive mutants were isolated. These mutants showed enhanced aspartokinase levels and accumulated morel-threonine than the parental strains. Mutant H-4290 accumulated 58 g/l ofl-threonine.     

Effect of tween 80 and dimethyl sulfoxide on biosynthesis ofl-lysine in regulatory mutants ofCorynebacterium glutamicum

By using dimethyl sulfoxide or Tween 80 (1 or 0.2 %), the production ofl-lysine was increased by 20–28 and 23–25%, respectively, in regulatory mutant strains ofCorynebacterium glutamicum. The stimulation observed is supposed to be caused by influencing cellular surface structures. Translated by Č. Novotny     

Regulation of aspartokinase activity in non-fermentative,marine eubacteria

Summary Cell-free extracts of gram-negative, non-fermentative, marine eubacteria were assayed for aspartokinase activity. The organisms tested included polarly flagellated species and groups which had GC contents in their DNAs of 46 to 64 moles % (Alteromonas, Pseudomonas) as well as species which had peritrichous flagellation and moles % GC contents of 53 to 68 (Alcaligenes). The results of these studies suggested that in all the strains tested, aspartokinase activity was catalyzed by a single enzyme. On the basis of the effect ofl-threonine,l-lysine,l-methionine, andl-isoleucine on activity, five different types of aspartokinases (designated I through V) were delineated. In aspartokinase types I through IV,l-threonine andl-lysine inhibited activity by means of a concerted feedback inhibition; in type V, activity was inhibited byl-threonine but unaffected byl-lysine. In types I, III, and IV,l-threonine andl-lysine alone were inhibitory, while in type II these effectors had virtually no effect on activity when tested singly. Three distinct responses were observed in the presence of two other end products of the aspartate pathway,l-methionine andl-isoleucine. In types I and II, these two amino acids usually stimulated activity and overcame the inhibition byl-threonine andl-lysine; in types IV and V,l-methionine andl-isoleucine had no effect; and in type III these amino acids inhibited activity. The results of this study indicate that the aspartokinases of a number of species and groups of marine bacteria have similarities and differences which should be of use in making future taxonomic groupings.     

Living cell reaction process forl-isoleucine andl-valine production

Summary A new process (Living Cell Reaction Process) forl-isoleucine production using viable, non-growing cells ofBrevibacterium flavum AB-07 was optimised using ethanol as the energy source and -ketobutyric acid (-KB) as precursor.l-valine also could be produced from glucose at high yield by this process. This process differs from the usual fermentation method in that non-growing cells are used, and the production ofl-isoleucine andl-valine were carried out under conditions of repressed cell division and growth. Minimal medium missing the essential growth factor, biotin was employed as the reaction mixture for the production ofl-isoleucine andl-valine. The productivity ofl-isoleucine andl-valine were 200 mmol·l^–1 · day^–1 (molecular yield to -KB: 95%) and 300 mmol · l^–1 · day^–1 (molecular yield to glucose: 80%) respectively. The content ofl-isoleucine andl-valine in total amino acids produced in the each mixture were 97% and 96% respectively.     

Factors enhancing l-valine production by the growth-limited l-isoleucine auxotrophic strain Corynebacterium glutamicum ΔilvA ΔpanB ilvNM13 (pECKAilvBNC)

Cell growth limitation is known to be an important condition that enhances l-valine synthesis in Corynebacterium glutamicum recombinant strains with l-isoleucine auxotrophy. To identify whether it is the limited availability of l-isoleucine itself or the l-isoleucine limitation-induced rel-dependent ppGpp-mediated stringent response that is essential for the enhancement of l-valine synthesis in growth-limited C. glutamicum cells, we deleted the rel gene, thereby constructing a relaxed (rel ⁻ ) C. glutamicum ΔilvA ΔpanB Δrel ilvNM13 (pECKAilvBNC) strain. Variations in enzyme activity and l-valine synthesis in rel ⁺ and rel ⁻ strains under conditions of l-isoleucine excess and limitation were investigated. A sharp increase in acetohydroxy acid synthase (AHAS) activity, a slight increase in acetohydroxyacid isomeroreductase (AHAIR) activity, and a dramatic increase in l-valine synthesis were observed in both rel ⁺ and rel ⁻ cells exposed to l-isoleucine limitation. Although the positive effect of induction of the stringent response on AHAS and AHAIR upregulation in cells was not confirmed, we found the stringent response to be beneficial for maintaining increased AHAS, dihydroxyacid dehydratase, and transaminase B activity and l-valine synthesis in cells during the stationary growth phase.     

l-threonine production by l-aspartate- and l-homoserine-resistant mutant of Escherichia coli

Summary Growth and l-threonine productivity of l-threonine producer Escherichia coli H-4290 were inhibited by precursor amino acids, l-homoserine and l-aspartate. l-Threonine hyper-producers were isolated among the mutants resistant to l-homoserine and l-aspartate. Mutants H-4351 (Hom^r) and H-4578 (Hom^r, Asp^r) accumulated 22.2 g/l and 24.3 g/l of l-threonine in test tube cultures, while the parental strain H-4290 accumulated 18.2 g/l. The enzyme level of aspartokinase I (first enzyme of the threonine operon) was enhanced 2.3 times (H-4351) and 3 times (H-4578) that of H-4290. Mutant H-4578 accumulated 76 g/l of l-threonine in a 2-l jar fermentor after 75 h cultivation.Abbreviations DAP diaminopimeric acid - Met ^l poor growth in methionine-free medium - AHV -amino--hydroxyvaleric acid - Thr-N^- lack of ability to utilize l-threonine as a nitrogen source - Rif rifampicin - Lys+Met^r resistant to l-lysine and dl-methionine     

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.     

Physiological aspects of l-lysine production: effect of nutritional limitations on a producing strain of Corynebacterium glutamicum

The effect of nutritional limitations, such as phosphorus and carbon, on the production of l-lysine by Corynebacterium glutamicum was studied in continuous culture. We observed that phosphate-limited cultures at low growth rates were favourable to l-lysine production. l-Lysine was produced when a culture at low dilution rate (0.03 h^–1) was established. A dilution rate of about 0.04 h^–1 should be maintained in order to assure good productivity and an l-lysine yield of 0.53 g/g. Under carbon-limiting conditions the maintenance energy and growth yield of 0.03 g/g·g^–1·h^–1 and 0.41 g/g, respectively, have been obtained. Under these limiting conditions the l-lysine production was not favoured even at lower dilution rates.Correspondence to: N. Coello     

Characterisation of kinetic parameters and metabolic transition of Corynebacterium glutamicum on l-lysine production in continuous culture

Kinetic parameters and physiological states of Corynebacterium glutamicum at the growing and l-lysine-overproducing phase were characterised in continuous culture on threonine-limited complex and minimal media. High l-lysine productivity occurred at dilution rates ranging from 0.1 h^–1 to 0.3 h^–1 on threonine-limited complex medium, and at dilution rates ranging from 0.1 h^–1 to 0.15 h^–1 in minimal medium. l-Lysine yields of 0.25 g/g (0.31 g/g as l-lysine hydrochloride) in complex medium, and of 0.17 g/g (0.21 g/g as l-lysine hydrochloride) in minimal medium, corresponding respectively to intrinsic yields of 0.533 g/g and 0.572 g/g were obtained. These intrinsic yield factors are closed to the theoretical ones (0.608 g/g, 0.75 mol/mol). Intrinsic biomass yields were calculated as 0.658 g/g in complex medium and 0.283 g/g in minimal medium. CO₂ production has been clearly related to l-lysine production. According to our results on specific uptake rates and specific productivities in complex medium, metabolic rearrangement should occur during the transition from the growing phase to the l-lysine-overproducing phase. This phenomenon was further investigated.     

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.     

Improved d,l-α-hydroxybutyrate conversion to l-isoleucine with Corynebacterium glutamicum mutants with increased d-lactate utilization

Summary Corynebacterium glutamicum possesses NAD-independent lactate dehydrogenases. The d-lactate dehydrogenase is consitutive, the l-lactate dehydrogenase is inducible. Enzyme measurements, gel electrophoretic studies and mutant studies suggest that both enzymes are responsible for the oxidation of the chemically synthesized precursor dl--hydroxybutyrate. Mutants with increased d-lactate utilization were selected. In mutant dl-4 the specific activity of the d-lactate dehydrogenase is increased 3 fold. This mutant utilizes the d-isomer of hydroxybutyrate to completion, which does not occur in the wild type. This results in the formation of 103 mmol/l l-isoleucine by mutant dl-4 as compared to 71 mmol/l in its ancestor.     

Carbohydrate metabolism in Corynebacterium glutamicum and applications for the metabolic engineering of l-lysine production strains

Carbohydrates exclusively serve as feedstock for industrial amino acid production with Corynebacterium glutamicum. Due to the industrial interest, knowledge about the pathways for carbohydrate metabolization in C. glutamicum steadily increases, enabling the rational design of optimized strains and production processes. In this review, we provide an overview of the metabolic pathways for utilization of hexoses (glucose, fructose), disaccharides (sucrose, maltose), pentoses (d-ribose, l-arabinose, d-xylose), gluconate, and β-glucosides present in C. glutamicum. Recent approaches of metabolic engineering of l-lysine production strains based on the known pathways are described and evaluated with respect to l-lysine yields.     

Effects of a Feedback-Resistant Aspartokinase III Gene on L-Isoleucine Production in Escherichia coli K-12

An L-isoleucine-overproducing recombinant strain of E. coli, TVD5, was also found to overproduce L-valine. The L-isoleucine productivity of TVD5 was markedly decreased by addition of L-lysine to the medium. Introduction of a gene encoding feedback-resistant aspartokinase III increased L-isoleucine productivity and decreased L-valine by-production. The resulting strain accumulated 12 g/l L-isoleucine from 40 g/l glucose, and suppression of L-isoleucine productivity by L-lysine was relieved.