Exploring the allosteric mechanism of dihydrodipicolinate synthase by reverse engineering of the allosteric inhibitor binding sites and its application for lysine production

Dihydrodipicolinate synthase (DHDPS, EC 4.2.1.52) catalyzes the first committed reaction of l-lysine biosynthesis in bacteria and plants and is allosterically regulated by l-lysine. In previous studies, DHDPSs from different species were proved to have different sensitivity to l-lysine inhibition. In this study, we investigated the key determinants of feedback regulation between two industrially important DHDPSs, the l-lysine-sensitive DHDPS from Escherichia coli and l-lysine-insensitive DHDPS from Corynebacterium glutamicum, by sequence and structure comparisons and site-directed mutation. Feedback inhibition of E. coli DHDPS was successfully alleviated after substitution of the residues around the inhibitor’s binding sites with those of C. glutamicum DHDPS. Interestingly, mutagenesis of the lysine binding sites of C. glutamicum DHDPS according to E. coli DHDPS did not recover the expected feedback inhibition but an activation of DHDPS by l-lysine, probably due to differences in the allosteic signal transduction in the DHDPS of these two organisms. Overexpression of l-lysine-insensitive E. coli DHDPS mutants in E. coli MG1655 resulted in an improvement of l-lysine production yield by 46 %.     

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

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

Quorum-sensing inhibitory compounds from extremophilic microorganisms isolated from a hypersaline cyanobacterial mat

In this study, extremely halophilic and moderately thermophilic microorganisms from a hypersaline microbial mat were screened for their ability to produce antibacterial, antidiatom, antialgal, and quorum-sensing (QS) inhibitory compounds. Five bacterial strains belonging to the genera Marinobacter and Halomonas and one archaeal strain belonging to the genus Haloterrigena were isolated from a microbial mat. The strains were able to grow at a maximum salinity of 22–25 % and a maximum temperature of 45–60 °C. Hexanes, dichloromethane, and butanol extracts from the strains inhibited the growth of at least one out of nine human pathogens. Only butanol extracts of supernatants of Halomonas sp. SK-1 inhibited growth of the microalga Dunaliella salina. Most extracts from isolates inhibited QS of the acyl homoserine lactone producer and reporter Chromobacterium violaceum CV017. Purification of QS inhibitory dichloromethane extracts of Marinobacter sp. SK-3 resulted in isolation of four related diketopiperazines (DKPs): cyclo(l-Pro-l-Phe), cyclo(l-Pro-l-Leu), cyclo(l-Pro-l-isoLeu), and cyclo(l-Pro-d-Phe). QS inhibitory properties of these DKPs were tested using C. violaceum CV017 and Escherichia coli-based QS reporters (pSB401 and pSB1075) deficient in AHL production. Cyclo(l-Pro-l-Phe) and cyclo(l-Pro-l-isoLeu) inhibited QS-dependent production of violacein by C. violaceum CV017. Cyclo(l-Pro-l-Phe), cyclo(l-Pro-l-Leu), and cyclo(l-Pro-l-isoLeu) reduced QS-dependent luminescence of the reporter E. coli pSB401 induced by 3-oxo-C6-HSL. Our study demonstrated the ability of halophilic and moderately thermophilic strains from a hypersaline microbial mat to produce biotechnologically relevant compounds that could be used as antifouling agents.     

Metabolic engineering Corynebacterium glutamicum for the l-lysine production by increasing the flux into l-lysine biosynthetic pathway

The experiments presented here were based on the conclusions of our previous results. In order to avoid introduction of expression plasmid and to balance the NADH/NAD ratio, the NADH biosynthetic enzyme, i.e., NAD-dependent glyceraldehyde-3-phosphate dehydrogenase (GADPH), was replaced by NADP-dependent GADPH, which was used to biosynthesize NADPH rather than NADH. The results indicated that the NADH/NAD ratio significantly decreased, and glucose consumption and l-lysine production drastically improved. Moreover, increasing the flux through l-lysine biosynthetic pathway and disruption of ilvN and hom, which involve in the branched amino acid and l-methionine biosynthesis, further improved l-lysine production by Corynebacterium glutamicum. Compared to the original strain C. glutamicum Lys5, the l-lysine production and glucose conversion efficiency (α) were enhanced to 81.0 ± 6.59 mM and 36.45 % by the resulting strain C. glutamicum Lys5-8 in shake flask. In addition, the by-products (i.e., l-threonine, l-methionine and l-valine) were significantly decreased as results of genetic modification in homoserine dehydrogenase (HSD) and acetohydroxyacid synthase (AHAS). In fed-batch fermentation, C. glutamicum Lys5-8 began to produce l-lysine at post-exponential growth phase and continuously increased over 36 h to a final titer of 896 ± 33.41 mM. The l-lysine productivity was 2.73 g l^?1 h^?1 and the α was 47.06 % after 48 h. However, the attenuation of MurE was not beneficial to increase the l-lysine production because of decreasing the cell growth. Based on the above-mentioned results, we get the following conclusions: cofactor NADPH, precursor, the flux through l-lysine biosynthetic pathway and DCW are beneficial to improve l-lysine production in C. glutamicum.     

Biotransformation of l-ornithine from l-arginine using whole-cell recombinant arginase

A recombinant arginase was generated for a whole-cell biotransformation system to convert l-arginine to l-ornithine in Escherichia coli. The gene ARG1 coding arginase from Bos taurus liver was synthesized and expressed in E. coli BL21 (DE3) via pETDuet-1. The recombinant arginase was used to catalyze l-arginine to l-ornithine and urea. The reaction was optimal at pH 9.5 and 37 °C. Manganese (10^?5 M) and Emulsifier OP-10 [0.033 % (v/v)] could promote arginase activity. In a scale up study, l-arginine conversion rate reached 98 % with a final concentration of 111.52 g l-ornithine/l.     

Enhancing the supply of oxaloacetate for l-glutamate production by pyc overexpression in different Corynebacterium glutamicum

During l-glutamate production, phosphoenolpyruvate carboxylase and pyruvate carboxylase (PCx) play important roles in supplying oxaloacetate to the tricarboxylic acid cycle. To explore the significance of PCx for l-glutamate overproduction, the pyc gene encoding PCx was amplified in Corynebacterium glutamicum GDK-9 triggered by biotin limitation and CN1021 triggered by a temperature shock, respectively. In the fed-batch cultures, GDK-9pXMJ19pyc exhibited 7.4 % lower l-alanine excretion and no improved l-glutamate production. In contrast, CN1021pXMJ19pyc finally exhibited 13 % lower l-alanine excretion and identical l-glutamate production, however, 8.5 % higher l-glutamate production was detected during a short period of the fermentation. It was indicated that pyc overexpression in l-glutamate producer strains, especially CN1021, increased the supply of oxaloacetate for l-glutamate synthesis and decreased byproduct excretion at the pyruvate node.     

Isolation of proline-based cyclic dipeptides from Bacillus sp. N strain associated with rhabitid entomopathogenic nematode and its antimicrobial properties

Entomopathogenic nematodes (EPN) are well-known as biological control agents and are found to have associated bacteria which can produce a wide range of bioactive secondary metabolites. We report herewith isolation of six proline containing cyclic dipeptides cyclo(d-Pro-l-Leu), cyclo(l-Pro-l-Met), cyclo(d-Pro-l-Phe), cyclo(l-Pro-l-Phe), cyclo(l-Pro-l-Tyr) and cyclo(l-Pro-d-Tyr) from ethyl acetate extract of the Luria Broth (LB) cell free culture filtrate of Bacillus sp. strain N associated with a new EPN Rhabditis sp. from sweet potato weevil grubs collected from Central Tuber Crops Research Institute farm. Antimicrobial studies of these 2,5-diketopiperazines (DKPs) against both medicinally and agriculturally important bacterium and fungi showed potent inhibitory values in the range of μg/mL. Cyclic dipeptides showed significantly higher activity than the commercial fungicide bavistin against agriculturally important fungi, viz., Fusarium oxysporum, Rhizoctonia solani, and Pencillium expansum. The highest activity of 2 μg/mL by cyclo(l-Pro-l-Phe) was recorded against P. expansum, a plant pathogen responsible for causing post harvest decay of stored apples and oranges. To our knowledge, this is the first report on the isolation of these DKPs from Rhabditis EPN bacterial strain Bacillus sp.     

Construction of an l-serine producing Escherichia coli via metabolic engineering

l-Serine is a nonessential amino acid, but plays a crucial role as a building block for cell growth. Currently, l-serine production is mainly dependent on enzymatic or cellular conversion. In this study, we constructed a recombinant Escherichia coli that can fermentatively produce l-serine from glucose. To accumulate l-serine, sdaA encoding the l-serine dehydratase, iclR encoding the isocitrate lyase regulator, and arcA encoding the aerobic respiration control protein were deleted in turn. In batch fermentation, the engineered E. coli strain YF-5 exhibited obvious l-serine accumulation but poor cell growth. To restore cell growth, aceB encoding the malate synthase was knocked out, and the engineered strain was then transformed with plasmid that overexpressed serA ^FR , serB, and serC genes. The resulting strain YF-7 produced 4.5 g/L l-serine in batch cultivation and 8.34 g/L l-serine in fed-batch cultivation.     

Characterization of a recombinant l-fucose isomerase from Caldicellulosiruptor saccharolyticus that isomerizes l-fucose, d-arabinose, d-altrose, and l-galactose

A recombinant l-fucose isomerase from Caldicellulosiruptor saccharolyticus was purified as a single 68 kDa band with an activity of 76 U mg^?1. The molecular mass of the native enzyme was 204 kDa as a trimer. The maximum activity for l-fucose isomerization was at pH 7 and 75°C in the presence of 1 mM Mn²⁺. Its half-life at 70°C was 6.1 h. For aldose substrates, the enzyme displayed activity in decreasing order for l-fucose, with a k _cat of 11,910 min^?1 and a K _m of 140 mM, d-arabinose, d-altrose, and l-galactose. These aldoses were converted to the ketoses l-fuculose, d-ribulose, d-psicose, and l-tagatose, respectively, with 24, 24, 85, 55% conversion yields after 3 h.     

Optimization of Biotransformation of l-Tyrosine to l-DOPA by Yarrowia lipolytica-NCIM 3472 Using Response Surface Methodology

l-DOPA (3,4-dihydroxyphenyl-l-alanine) is the most widely used drug for treatment of Parkinson’s disease. In this study Yarrowia lipolytica-NCIM 3472 biomass was used for transformation of l-tyrosine to l-DOPA. The process parameters were optimized using response surface methodology (RSM). The optimum values of the tested variables for the production of l-DOPA were: pH 7.31, temperature 42.9 °C, 2.31 g l^?1 cell mass and 1.488 g l^?1 l-tyrosine. The highest yield obtained with these optimum parameters along with recycling of the cells was 4.091 g l^?1. This optimization of process parameters using RSM resulted in 4.609-fold increase in the l-DOPA production. The statistical analysis showed that the model was significant. Also coefficient of determination (R²) was 0.9758, indicating a good agreement between the experimental and predicted values of l-DOPA production. The highest tyrosinase activity observed was 7,028 U mg^?1 tyrosine. l-DOPA production was confirmed by HPTLC and HPLC analysis. Thus, RSM approach effectively enhanced the potential of Y. lipolytica-NCIM 3472 as an alternative source to produce l-DOPA.     

Application of metabolic engineering for the biotechnological production of l-valine

The branched chain amino acid l-valine is an essential nutrient for higher organisms, such as animals and humans. Besides the pharmaceutical application in parenteral nutrition and as synthon for the chemical synthesis of e.g. herbicides or anti-viral drugs, l-valine is now emerging into the feed market, and significant increase of sales and world production is expected. In accordance, well-known microbial production bacteria, such as Escherichia coli and Corynebacterium glutamicum strains, have recently been metabolically engineered for efficient l-valine production under aerobic or anaerobic conditions, and the respective cultivation and production conditions have been optimized. This review summarizes the state of the art in l-valine biosynthesis and its regulation in E. coli and C. glutamicum with respect to optimal metabolic network for microbial l-valine production, genetic strain engineering and bioprocess development for l-valine production, and finally, it will shed light on emerging technologies that have the potential to accelerate strain and bioprocess engineering in the near future.     

Backbone and side-chain 1H, 15N and 13C assignment of apo- and imipenem-acylated l,d-transpeptidase from Bacillus subtilis

The d,d-transpeptidase activity of Penicillin Binding Proteins (PBPs) is essential to maintain cell wall integrity. PBPs catalyze the final step of the peptidoglycan synthesis by forming 4 → 3 cross-links between two peptide stems. Recently, a novel β-lactam resistance mechanism involving l,d-transpeptidases has been identified in Enterococcus faecium and Mycobacterium tuberculosis. In this resistance pathway, the classical 4 → 3 cross-links are replaced by 3 → 3 cross-links, whose formation are catalyzed by the l,d-transpeptidases. To date, only one class of the entire β-lactam family, the carbapenems, is able to inhibit the l,d-transpeptidase activity. Nevertheless, the specificity of this inactivation is still not understood. Hence, the study of this new transpeptidase family is of considerable interest in order to understand the mechanism of the l,d-transpeptidases inhibition by carbapenems. In this context, we present herein the backbone and side-chain ¹H, ¹⁵N and ¹³C NMR assignment of the l,d-transpeptidase from Bacillus subtilis (Ldt_Bs) in the apo and in the acylated form with a carbapenem, the imipenem.     

Cyclic dipeptides from rhabditid entomopathogenic nematode-associated Bacillus cereus have antimicrobial activities

The cell free culture filtrate of Bacillus cereus associated with an entomopathogenic nematode, Rhabditis (Oscheius) sp. exhibited strong antimicrobial activity. The ethyl acetate extract of the bacterial culture filtrate was purified by silica gel column chromatography to obtain four bioactive compounds. The structure and absolute stereochemistry of these compounds were determined based on extensive spectroscopic analyses (FABMS, ¹H NMR, ¹³C NMR, ¹H–¹H COSY, ¹H–¹³C HMBC) and Marfey’s method. The compounds were identified as cyclic dipeptides (CDPs): cyclo(l-Pro-l-Trp), cyclo(l-Leu-l-Val), cyclo(d-Pro-d-Met), and cyclo(d-Pro-d-Phe), respectively. Compounds recorded significant antibacterial activity against all the test bacteria (Staphylococcus epidermidis, Staphylococcus aureus, Klebsiella pneumoniae, Escherichia coli, Pseudomonas aeruginosa and methicillin-resistant S. aureus) except cyclo(l-Leu-l-Val). Cyclo(l-Leu-l-Val) recorded activity only against Gram positive bacteria. Best antibacterial activity was recorded by cyclo(l-Pro-l-Trp) against S. aureus (4 μg/ml). The four compounds were active against all the five fungi tested (Trichophyton rubrum, Aspergillus flavus, Candida albicans, Candida tropicalis and Cryptococcus neoformans) and the activity was compared with amphotericin B, the standard fungicide. The highest activity of 1 μg/ml by cyclo(l-Pro-l-Trp) was recorded against T. rubrum, a human pathogen responsible for causing athlete’s foot, jock itch, and ringworm. The activity of cyclo(l-Pro-l-Trp) against T. rubrum, C. neoformans and C. albicans were better than amphotericin B, the standard antifungal agent. To our knowledge, this is the first report of antifungal activity of CDPs against the human pathogenic fungi T. rubrum and C. neoformans. The four CDPs are nontoxic to healthy human cell line up to 200 μg/ml. We conclude that the bacterium associated with entomopathogenic nematode is promising sources of natural antimicrobial secondary metabolites, which may receive greater benefit as potential sources of new drugs in the pharmaceutical industry.     

l-Arabinose/d-galactose 1-dehydrogenase of Rhizobium leguminosarum bv. trifolii characterised and applied for bioconversion of l-arabinose to l-arabonate with Saccharomyces cerevisiae

Four potential dehydrogenases identified through literature and bioinformatic searches were tested for l-arabonate production from l-arabinose in the yeast Saccharomyces cerevisiae. The most efficient enzyme, annotated as a d-galactose 1-dehydrogenase from the pea root nodule bacterium Rhizobium leguminosarum bv. trifolii, was purified from S. cerevisiae as a homodimeric protein and characterised. We named the enzyme as a l-arabinose/d-galactose 1-dehydrogenase (EC 1.1.1.-), Rl AraDH. It belongs to the Gfo/Idh/MocA protein family, prefers NADP⁺ but uses also NAD⁺ as a cofactor, and showed highest catalytic efficiency (k _cat/K _m) towards l-arabinose, d-galactose and d-fucose. Based on nuclear magnetic resonance (NMR) and modelling studies, the enzyme prefers the α-pyranose form of l-arabinose, and the stable oxidation product detected is l-arabino-1,4-lactone which can, however, open slowly at neutral pH to a linear l-arabonate form. The pH optimum for the enzyme was pH 9, but use of a yeast-in-vivo-like buffer at pH 6.8 indicated that good catalytic efficiency could still be expected in vivo. Expression of the Rl AraDH dehydrogenase in S. cerevisiae, together with the galactose permease Gal2 for l-arabinose uptake, resulted in production of 18 g of l-arabonate per litre, at a rate of 248 mg of l-arabonate per litre per hour, with 86 % of the provided l-arabinose converted to l-arabonate. Expression of a lactonase-encoding gene from Caulobacter crescentus was not necessary for l-arabonate production in yeast.     

l-leucine, l-methionine, and l-phenylalanine share a Na+/K+-dependent amino acid transporter in shrimp hepatopancreas

Hepatopancreatic brush border membrane vesicles (BBMV), made from Atlantic White shrimp (Litopenaeus setiferus), were used to characterize the transport properties of ³H-l-leucine influx by these membrane systems and how other essential amino acids and the cations, sodium and potassium, interact with this transport system. ³H-l-leucine uptake by BBMV was pH-sensitive and occurred against transient transmembrane concentration gradients in both Na⁺- and K⁺-containing incubation media, suggesting that either cation was capable of providing a driving force for amino acid accumulation. ³H-l-leucine uptake in NaCl or KCl media were each three times greater in acidic pH (pH 5.5) than in alkaline pH (pH 8.5). The essential amino acid, l-methionine, at 20 mM significantly (p < 0.0001) inhibited the 2-min uptakes of 1 mM ³H-l-leucine in both Na⁺- and K⁺-containing incubation media. The residual ³H-l-leucine uptake in the two media were significantly greater than zero (p < 0.001), but not significantly different from each other (p > 0.05) and may represent an l-methionine- and cation-independent transport system. ³H-l-leucine influxes in both NaCl and KCl incubation media were hyperbolic functions of [l-leucine], following the carrier-mediated Michaelis–Menten equation. In NaCl, ³H-l-leucine influx displayed a low apparent K _M (high affinity) and low apparent J _max, while in KCl the transport exhibited a high apparent K _M (low affinity) and high apparent J _max. l-methionine or l-phenylalanine (7 and 20 mM) were competitive inhibitors of ³H-l-leucine influxes in both NaCl and KCl media, producing a significant (p < 0.01) increase in ³H-l-leucine influx K _M, but no significant response in ³H-l-leucine influx J _max. Potassium was a competitive inhibitor of sodium co-transport with ³H-l-leucine, significantly (p < 0.01) increasing ³H-l-leucine influx K _M in the presence of sodium, but having negligible effect on ³H-l-leucine influx J _max in the same medium. These results suggest that shrimp BBMV transport ³H-l-leucine by a single l-methionine- and l-phenylalanine-shared carrier system that is enhanced by acidic pH and can be stimulated by either Na⁺ or K⁺ acting as co-transport drivers binding to shared activator sites.     

Modification of glycolysis and its effect on the production of l-threonine in Escherichia coli

High concentrations of acetate, the main by-product of Escherichia coli (E. coli) high cell density culture, inhibit bacterial growth and l-threonine production. Since metabolic overflux causes acetate accumulation, we attempted to reduce acetate production by redirecting glycolysis flux to the pentose phosphate pathway by deleting the genes encoding phosphofructokinase (pfk) and/or pyruvate kinase (pyk) in an l-threonine-producing strain of E. coli, THRD. pykF, pykA, pfkA, and pfkB deletion mutants produced less acetate (9.44 ± 0.83, 3.86 ± 0.88, 0.30 ± 0.25, and 6.99 ± 0.85 g/l, respectively) than wild-type THRD cultures (19.75 ± 0.93 g/l). THRDΔpykF and THRDΔpykA produced 11.05 and 5.35 % more l-threonine, and achieved a 10.91 and 5.60 % higher yield on glucose, respectively. While THRDΔpfkA grew more slowly and produced less l-threonine than THRD, THRDΔpfkB produced levels of l-threonine (102.28 ± 2.80 g/l) and a yield on glucose (0.34 g/g) similar to that of THRD. The dual deletion mutant THRDΔpfkBΔpykF also achieved low acetate (7.42 ± 0.81 g/l) and high l-threonine yields (111.37 ± 2.71 g/l). The level of NADPH in THRDΔpfkA cultures was depressed, whereas all other mutants produced more NADPH than THRD did. These results demonstrated that modification of glycolysis in E. coli THRD reduced acetate production and increased accumulation of l-threonine.     

Metabolic engineering of Escherichia coli for biosynthesis of d-galactonate

d-galactose is an attractive substrate for bioconversion. Herein, Escherichia coli was metabolically engineered to convert d-galactose into d-galactonate, a valuable compound in the polymer and cosmetic industries. d-galactonate productions by engineered E. coli strains were observed in shake flask cultivations containing 2 g L^?1 d-galactose. Engineered E. coli expressing gld coding for galactose dehydrogenase from Pseudomonas syringae was able to produce 0.17 g L^?1 d-galactonate. Inherent metabolic pathways for assimilating both d-galactose and d-galactonate were blocked to enhance the production of d-galactonate. This approach finally led to a 7.3-fold increase with d-galactonate concentration of 1.24 g L^?1 and yield of 62.0 %. Batch fermentation in 20 g L^?1 d-galactose of E. coli ?galK?dgoK mutant expressing the gld resulted in 17.6 g L^?1 of d-galactonate accumulation and highest yield of 88.1 %. Metabolic engineering strategy developed in this study could be useful for industrial production of d-galactonate.     

Implication of gluconate kinase activity in l-ornithine biosynthesis in Corynebacterium glutamicum

With the purpose of generating a microbial strain for l-ornithine production in Corynebacterium glutamicum, genes involved in the central carbon metabolism were inactivated so as to modulate the intracellular level of NADPH, and to evaluate their effects on l-ornithine production in C. glutamicum. Upon inactivation of the 6-phosphoglucoisomerase gene (pgi) in a C. glutamicum strain, the concomitant increase in intracellular NADPH concentrations from 2.55 to 5.75?mmol?g^?1 (dry cell weight) was accompanied by reduced growth rate and l-ornithine production, suggesting that l-ornithine production is not solely limited by NADPH availability. In contrast, inactivation of the gluconate kinase gene (gntK) led to a 51.8?% increase in intracellular NADPH concentration, which resulted in a 49.9?% increase in l-ornithine production. These results indicate that excess NADPH is not necessarily rate-limiting, but is required for increased l-ornithine production in C. glutamicum.     

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.     

l-Valine production with minimization of by-products’ synthesis in Corynebacterium glutamicum and Brevibacterium flavum

Corynebacterium glutamicum ATCC13032 and Brevibacterium flavum JV16 were engineered for l-valine production by over-expressing ilvEBN ^r C genes at 31?°C in 72?h fermentation. Different strategies were carried out to reduce the by-products’ accumulation in l-valine fermentation and also to increase the availability of precursor for l-valine biosynthesis. The native promoter of ilvA of C. glutamicum was replaced with a weak promoter MPilvA (P-ilvAM1CG) to reduce the biosynthetic rate of l-isoleucine. Effect of different relative dissolved oxygen on l-valine production and by-products’ formation was recorded, indicating that 15?% saturation may be the most appropriate relative dissolved oxygen for l-valine fermentation with almost no l-lactic acid and l-glutamate formed. To minimize l-alanine accumulation, alaT and/or avtA was inactivated in C. glutamicum and B. flavum, respectively. Compared to high concentration of l-alanine accumulated by alaT inactivated strains harboring ilvEBN ^r C genes, l-alanine concentration was reduced to 0.18?g/L by C. glutamicum ATCC13032MPilvA△avtA pDXW-8-ilvEBN ^r C, and 0.22?g/L by B. flavum JV16avtA::Cm pDXW-8-ilvEBN ^r C. Meanwhile, l-valine production and conversion efficiency were enhanced to 31.15?g/L and 0.173?g/g by C. glutamicum ATCC13032MPilvA△avtA pDXW-8-ilvEBN ^r C, 38.82?g/L and 0.252?g/g by B. flavum JV16avtA::Cm pDXW-8-ilvEBN ^r C. This study provides combined strategies to improve l-valine yield by minimization of by-products’ production.