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.     

Microbial production of l-leucine from α-ketoisocaproate by Corynebacterium glutamicum

Summary A process for l-leucine production was studied using Corynebacterium glutamicum for the conversion of -ketoisocaproate. When this precursor was added to the culture medium in a concentration of 20 g/l about 16 g/l l-leucine were formed after a fermentation time of 57 h and the molar yield was 91%. Using a fed-batch culture it was possible to produce 24 g/l of l-leucine from 32 g/l of -ketoisocaproate within 23 h. Enzymatic studies indicate that in this glutamate-producing bacterium -ketoisocaproate is converted into l-leucine via the transaminase B reaction and l-glutamate is regenerated by the glutamate dehydrogenase. By the addition of -ketoisocaproate to the culture medium the specific activity of transaminase B was increased threefold.     

Disruption of genes for the enhanced biosynthesis of α-ketoglutarate in Corynebacterium glutamicum

The development of microbial strains for the enhanced production of α-ketoglutarate (α-KG) was investigated using a strain of Corynebacterium glutamicum that overproduces of l-glutamate, by disrupting three genes involved in the α-KG biosynthetic pathway. The pathways competing with the biosynthesis of α-KG were blocked by knocking out aceA (encoding isocitrate lyase, ICL), gdh (encoding glutamate dehydrogenase, l-gluDH), and gltB (encoding glutamate synthase or glutamate-2-oxoglutarate aminotransferase, GOGAT). The strain with aceA, gltB, and gdh disrupted showed reduced ICL activity and no GOGAT and l-gluDH activities, resulting in up to 16-fold more α-KG production than the control strain in flask culture. These results suggest that l-gluDH is the key enzyme in the conversion of α-KG to l-glutamate; therefore, prevention of this step could promote α-KG accumulation. The inactivation of ICL leads the carbon flow to α-KG by blocking the glyoxylate pathway. However, the disruption of gltB did not affect the biosynthesis of α-KG. Our results can be applied in the industrial production of α-KG by using C. glutamicum as producer.     

Role of poly-β-hydroxybutyric acid in cyst formation byAzotobacter

Several parameters associated with the growth ofAzotobacter vinelandii in liquid culture were examined in order to investigate the relationship between the accumulation and degradation of poly-β-hydroxybutyric acid (PHB), the development of viscous capsular components, and cyst formation. The amount of intracellular PHB, which increased markedly during the log phase of growth, reached a maximum during the early stationary phase and subsequently declined. During polymer degradation there was a concurrent increase in the extent of encystment in the cultures supplemented with CaCO₃. An increase was noted in the viscosity of culture supernatants during polymer degradation when CaCO₃ was deleted from the medium and the culture pH was controlled by the periodic addition of 0.1m KOH. The extent of encystment and the amount of PHB accumulated were directly proportional to the substrate concentration. The PHB was selectively labeled by the addition of sodium acetate-2-¹⁴C to late log-phase cells. During polymer utilization in either encysting or nonencysting cultures 20% of the label was evolved as CO₂. In the nonencysting cultures, 45% of the radioactivity was distributed between residual PHB and other cellular components, and 35% was in the supernatant polysaccharide-like material. Intact cysts retained 80% of the label. Experiments with ruptured cysts indicated that about 35% of the radioactivity was present in the intine material.     

Corynebacterium glutamicum,a natural overproducer of succinic acid?

Corynebacterium glutamicum is well known as an important industrial amino acid producer. For a few years, its ability to produce organic acids, under micro‐aerobic or anaerobic conditions was demonstrated. This study is focused on the identification of the culture parameters influencing the organic acids production and, in particular, the succinate production, by this bacterium. Corynebacterium glutamicum 2262, used throughout this study, was a wild‐type strain, which was not genetically designed for the production of succinate. The oxygenation level and the residual glucose concentration appeared as two critical parameters for the organic acids production. The maximal succinate concentration (4.9 g L^?1) corresponded to the lower k_La value of 5 h^?1. Above 5 h^?1, a transient accumulation of the succinate was observed. Interestingly, the stop in the succinate production was concomitant with a lower threshold glucose concentration of 9 g L^?1. Taking into account this threshold, a fed‐batch culture was performed to optimize the succinate production with C. glutamicum 2262. The results showed that this wild‐type strain was able to produce 93.6 g L^?1 of succinate, which is one of the highest concentration reported in the literature.     

Leucine biosynthesis in Alcaligenes eutrophus H16: Influence of amino acid additions on the formation of active α-isopropylmalate synthase and α-acetohydroxy acid synthase

The -isopropylmalate synthase of the chemolithoautotrophic Alcaligenes eutrophus H16 is apparently a soluble enzyme but is strongly adsorbed to cell particles in ruptured cell suspensions. This was not observed with -acetohydroxy acid synthase or threonine deaminase. The formation of these regulatory enzymes of the branched chain amino acid biosynthesis pathway generally decreased with decreased growth rates. The addition of 5 mM valine plus isoleucine with and without 5 mM threonine caused a 6.6- and a 4-fold increase, respectively, in the formation of active -isopropylmalate synthase, but caused a strong decrease in the -actohydroxy acid synthase. The level of active -isopropylmalate synthase is apparently regulated by the level of leucine; whereas, the level of the -acetohydroxy acid synthase and threonine deaminase is influenced by the presence of several amino acids. A catabolic threonine deaminase was not encountered.Abbreviations IRS -Isopropylamalate - AHA -acetohydroxy acid - TDA throninedeaminase This paper is dedicated to Professor H. G. Schlegel, University Göttingen, on the occasion of his 60th birthday. I am grateful to a great teacher and scientist, who in his unique way stimulated enthusiasm and fascination in microbiology in his students throughout the years     

Mechanism of Concerted Inhibition of α2β2-type Hetero-oligomeric Aspartate Kinase from Corynebacterium glutamicum

Aspartate kinase (AK) is the first and committed enzyme of the biosynthetic pathway producing aspartate family amino acids, lysine, threonine, and methionine. AK from Corynebacterium glutamicum (CgAK), a bacterium used for industrial fermentation of amino acids, including glutamate and lysine, is inhibited by lysine and threonine in a concerted manner. To elucidate the mechanism of this unique regulation in CgAK, we determined the crystal structures in several forms: an inhibitory form complexed with both lysine and threonine, an active form complexed with only threonine, and a feedback inhibition-resistant mutant (S301F) complexed with both lysine and threonine. CgAK has a characteristic α₂β₂-type heterotetrameric structure made up of two α subunits and two β subunits. Comparison of the crystal structures between inhibitory and active forms revealed that binding inhibitors causes a conformational change to a closed inhibitory form, and the interaction between the catalytic domain in the α subunit and β subunit (regulatory subunit) is a key event for stabilizing the inhibitory form. This study shows not only the first crystal structures of α₂β₂-type AK but also the mechanism of concerted inhibition in CgAK.     

Enhancement of γ-aminobutyric acid production in recombinant Corynebacterium glutamicum by co-expressing two glutamate decarboxylase genes from Lactobacillus brevis

γ-Aminobutyric acid (GABA), a non-protein amino acid, is a bioactive component in the food, feed and pharmaceutical fields. To establish an effective single-step production system for GABA, a recombinant Corynebacterium glutamicum strain co-expressing two glutamate decarboxylase (GAD) genes (gadB1 and gadB2) derived from Lactobacillus brevis Lb85 was constructed. Compared with the GABA production of the gadB1 or gadB2 single-expressing strains, GABA production by the gadB1–gadB2 co-expressing strain increased more than twofold. By optimising urea supplementation, the total production of l-glutamate and GABA increased from 22.57 ± 1.24 to 30.18 ± 1.33 g L^?1, and GABA production increased from 4.02 ± 0.95 to 18.66 ± 2.11 g L^?1 after 84-h cultivation. Under optimal urea supplementation, l-glutamate continued to be consumed, GABA continued to accumulate after 36 h of fermentation, and the pH level fluctuated. GABA production increased to a maximum level of 27.13 ± 0.54 g L^?1 after 120-h flask cultivation and 26.32 g L^?1 after 60-h fed-batch fermentation. The conversion ratio of l-glutamate to GABA reached 0.60–0.74 mol mol^?1. By co-expressing gadB1 and gadB2 and optimising the urea addition method, C. glutamicum was genetically improved for de novo biosynthesis of GABA from its own accumulated l-glutamate.     

Biosynthesis and in vitro enzymatic synthesis of the isoleucine conjugate of 12-oxo-phytodienoic acid from the isoleucine conjugate of α-linolenic acid

The isoleucine conjugate of 12-oxo-phytodienoic acid (OPDA-Ile), a new member of the jasmonate family, was recently identified in Arabidopsis thaliana and might be a signaling molecule in plants. However, the biosynthesis and function of OPDA-Ile remains elusive. This study reports an in vitro enzymatic method for synthesizing OPDA-Ile, which is catalyzed by reactions of lipoxygenase (LOX), allene oxide synthase (AOS), and allene oxide cyclase (AOC) using isoleucine conjugates of α -linolenic acid (LA-Ile) as the substrate. A. thaliana fed LA-Ile exhibited a marked increase in the OPDA-Ile concentration. LA-Ile was also detected in A. thaliana. Furthermore, stable isotope labelled LA-Ile was incorporated into OPDA-Ile. Thus, OPDA-Ile is biosynthesized via the cyclization of LA-Ile in A. thaliana.     

Engineering of Corynebacterium glutamicum for high-level γ-aminobutyric acid production from glycerol by dynamic metabolic control

Synthetic biology seeks to reprogram microbial cells for efficient production of value-added compounds from low-cost renewable substrates. A great challenge of chemicals biosynthesis is the competition between cell metabolism and target product synthesis for limited cellular resource. Dynamic regulation provides an effective strategy for fine-tuning metabolic flux to maximize chemicals production. In this work, we created a tunable growth phase-dependent autonomous bifunctional genetic switch (GABS) by coupling growth phase responsive promoters and degrons to dynamically redirect the carbon flux for metabolic state switching from cell growth mode to production mode, and achieved high-level GABA production from low-value glycerol in Corynebacterium glutamicum. A ribosome binding sites (RBS)-library-based pathway optimization strategy was firstly developed to reconstruct and optimize the glycerol utilization pathway in C. glutamicum, and the resulting strain CgGly2 displayed excellent glycerol utilization ability. Then, the initial GABA-producing strain was constructed by deleting the GABA degradation pathway and introducing an exogenous GABA synthetic pathway, which led to 5.26 g/L of GABA production from glycerol. In order to resolve the conflicts of carbon flux between cell growth and GABA production, we used the GABS to reconstruct the GABA synthetic metabolic network, in which the competitive modules of GABA biosynthesis, including the tricarboxylic acid (TCA) cycle module and the arginine biosynthesis module, were dynamically down-regulated while the synthetic modules were dynamically up-regulated after sufficient biomass accumulation. Finally, the resulting strain G7-1 accumulated 45.6 g/L of GABA with a yield of 0.4 g/g glycerol, which was the highest titer of GABA ever reported from low-value glycerol. Therefore, these results provide a promising technology to dynamically balance the metabolic flux for the efficient production of other high value-added chemicals from a low-value substrate in C. glutamicum.     

Enhanced production of α-ketoglutarate by fed-batch culture in the metabolically engineered strains of Corynebacterium glutamicum

The fed-batch culture system was employed to enhance production of α-ketoglutarate (α-KG) by the strainsof Corynebacterium glutamicum, whose genes encoding the key enzymes responsible for the biosynthesis of L-glutamate from α-KG were deleted. In a shake flask fermentation, C. glutamicum JH110 in which the 3 genes, gdh (encoding glutamate dehydrogenase), gltB (encoding glutamate synthase), and aceA (encoding isocitrate lyase) were disrupted showed the highest production of α-KG (12.4 g/L) compared to the strains JH102 (gdh mutant), JH103 (gltB mutant), and JH107 (gdh gltB double mutant). In the fed-batch cultures using a 5 L-jar fermenter, the strain JH107 produced more α-KG (19.5 g/L), but less glutamic acid (23.3 g/L) than those produced by the parent strain HH109, as well as JH102. The production of α-KG was significantly enhanced and the accumulation of glutamicacid was minimized by the ammonium-limited fed-batch cultures employing C. glutamicum JH107. Further improvement of α-KG production by the strain JH107 was achieved through the ammonium-limited fed-batch culture with the feeding of molasses, and the levels of α-KG and glutamic acid produced were 51.1 and 0.01 g/L, respectively.     

Novel formation of α-amino acid from α-oxo acids and ammonia in an aqueous medium

In the course of a study of possible mechanisms for chemical evolution in the primeval sea, we found the novel formation of -amino acids and N-acylamino acids from -oxo acids and ammonia in an aqueous medium. Glyoxylic acid reacted with ammonia to form N-oxalylglycine, which gave glycine in a 5–39% yield after hydrolysis with 6N HCl. Pyruvic acid and ammonia reacted to give N-acetylalanine, which formed alanine in a 3–7% overall yield upon hydrolysis. The pH optima in these reactions were between pH 3 and 4. These reactions were further extended to the formation of other amino acids. Glutamic acid, phenylalanine and alanine were formed from -ketoglutaric acid, phenylpyruvic acid and oxaloacetic acid, respectively, under similar conditions. N-Succinylglutamic acid was obtained as an intermediate in glutamic acid synthesis. Phenylacetylphenyl-alanineamide was also isolated as an intermediate in phenylalanine synthesis. Alanine, rather than aspartic acid, was produced from oxaloacetic acid. These reactions provide a novel route for the prebiotic synthesis of amino acids. A mechanism for the reactions will be proposed.     

Synthesis of β-alanine from l-aspartate using l-aspartate-α-decarboxylase from Corynebacterium glutamicum

β-Alanine is mainly produced by chemical methods in current industrial processes. Here, panD from Corynebacterium glutamicum encoding l-aspartate-α-decarboxylase (ADC) was cloned and expressed in Escherichia coli BL21(DE3). ADC _C.g catalyzes the α-decarboxylation of l-aspartate to β-alanine. The purified ADC _C.g was optimal at 55 °C and pH 6 with excellent stability at 16–37 °C and pH 4–7. A pH–stat directed, fed-batch feeding strategy was developed for enzymatic synthesis of β-alanine to keep the pH value within 6–7.2 and thus attenuate substrate inhibition. A maximum conversion of 97.2 % was obtained with an initial 5 g l-aspartate/l and another three feedings of 0.5 % (w/v) l-aspartate at 8 h intervals. The final β-alanine concentration was 12.85 g/l after 36 h. This is the first study concerning the enzymatic production of β-alanine by using ADC.     

Significance of Arg3, Arg54, and Tyr58 of l-aspartate α-decarboxylase from Corynebacterium glutamicum in the process of self-cleavage

Purpose of work

We have elucidated the significance of three key amino acid residues of l-aspartate α-decarboxylase that act remotely from its cleavage site for its functional self-cleavage as well as for its catalytic activity. These results provide useful fundamental information for engineering l-aspartate α-decarboxylase. l-Aspartate α-decarboxylase (ADC) from Corynebacterium glutamicum, and encoded by panD, was cloned and expressed in Escherichia coli and then purified. Three amino acid residues were found to be related to ADC self-cleavage. Mutating R3 to either A, Q, N, L, D, or E produced only the unprocessed pro-enzyme. Although mutating R54 and Y58 into A or K and A or T, respectively, partly influenced ADC self-cleavage, the specific activity of each of the four ßmutants decreased to 3.5, 4, 2.4, and 2.6 U mg^?1, respectively, compared with a specific activity of 690 U mg^?1 for the wild-type enzyme. Thus, R3 triggers ADC self-cleavage and completes the modification of the active site with assistance by R54 and Y58. These results will help to engineer ADC for improved industrial applications.     

Functional Characterization of Corynebacterium alkanolyticum β-Xylosidase and Xyloside ABC Transporter in Corynebacterium glutamicum

The Corynebacterium alkanolyticum xylEFGD gene cluster comprises the xylD gene that encodes an intracellular β-xylosidase next to the xylEFG operon encoding a substrate-binding protein and two membrane permease proteins of a xyloside ABC transporter. Cloning of the cluster revealed a recombinant β-xylosidase of moderately high activity (turnover for p-nitrophenyl-β-d-xylopyranoside of 111 ± 4 s⁻¹), weak α-l-arabinofuranosidase activity (turnover for p-nitrophenyl-α-l-arabinofuranoside of 5 ± 1 s⁻¹), and high tolerance to product inhibition (K_i for xylose of 67.6 ± 2.6 mM). Heterologous expression of the entire cluster under the control of the strong constitutive tac promoter in the Corynebacterium glutamicum xylose-fermenting strain X1 enabled the resultant strain X1EFGD to rapidly utilize not only xylooligosaccharides but also arabino-xylooligosaccharides. The ability to utilize arabino-xylooligosaccharides depended on cgR_2369, a gene encoding a multitask ATP-binding protein. Heterologous expression of the contiguous xylD gene in strain X1 led to strain X1D with 10-fold greater β-xylosidase activity than strain X1EFGD, albeit with a total loss of arabino-xylooligosaccharide utilization ability and only half the ability to utilize xylooligosaccharides. The findings suggest some inherent ability of C. glutamicum to take up xylooligosaccharides, an ability that is enhanced by in the presence of a functional xylEFG-encoded xyloside ABC transporter. The finding that xylEFG imparts nonnative ability to take up arabino-xylooligosaccharides should be useful in constructing industrial strains with efficient fermentation of arabinoxylan, a major component of lignocellulosic biomass hydrolysates.     

Identification and expression of the 11β-steroid hydroxylase from Cochliobolus lunatus in Corynebacterium glutamicum

Hydroxylation of steroids has acquired special relevance for the pharmaceutical industries. Particularly, the 11β-hydroxylation of steroids is a reaction of biotechnological importance currently carried out at industrial scale by the fungus Cochliobolus lunatus. In this work, we have identified the genes encoding the cytochrome CYP103168 and the reductase CPR64795 of C. lunatus responsible for the 11β-hydroxylase activity in this fungus, which is the key step for the preparative synthesis of cortisol in industry. A recombinant Corynebacterium glutamicum strain harbouring a plasmid expressing both genes forming a synthetic bacterial operon was able to 11β-hydroxylate several steroids as substrates. This is a new example to show that the industrial strain C. glutamicum can be used as a suitable chassis to perform steroid biotransformation expressing eukaryotic cytochromes.     

Subunit–subunit interactions are weakened in mutant forms of acetohydroxy acid synthase insensitive to valine inhibition

In acetohydroxy acid synthase from Streptomyces cinnamonensis mutants affected in valine regulation, the impact of mutations on interactions between the catalytic and the regulatory subunits was examined using yeast two-hybrid system. Mutations in the catalytic and the regulatory subunits were projected into homology models of the respective proteins. Two changes in the catalytic subunit, E139A (α domain) and ΔQ217 (β domain), both located on the surface of the catalytic subunit dimer, lowered the interaction with the regulatory subunit. Three consecutive changes in the N-terminal part of the regulatory subunit were examined. Changes G16D and V17D in a loop and adjacent α-helix of ACT domain affected the interaction considerably, indicating that this region might be in contact with the catalytic subunit during allosteric regulation. In contrast, the adjacent mutation L18F did not influence the interaction at all. Thus, L18 might participate in valine binding or conformational change transfer within the regulatory subunits. Shortening of the regulatory subunit to 107 residues reduced the interaction essentially, suggesting that the C-terminal part of the regulatory subunit is also important for the catalytic subunit binding.