Metabolic analysis of glutamate production by Corynebacterium glutamicum

The dynamic behavior of the metabolism of Corynebacterium glutamicum during L-glutamic acid fermentation, was evaluated by quantitative analysis of the evolution of intracellular metabolites and key enzyme concentrations. Glutamate production was induced by an increase of the temperature and a final concentration of 80 g/l was attained. During the production phase, various other compounds, notably lactate, trehalose, and DHA were secreted to the medium. Intracellular metabolites analysis showed important variations of glycolytic intermediates and NADH, NAD coenzymes levels throughout the production phase. Two phenomena occur during the production phase which potentially provoke a decrease in the glutamate yield: Both the intracellular concentrations of glycolytic intermediates and the NADH/NAD ratio increase significantly during the period in which the overall metabolic rates decline. This correlates with the decrease in glutamate yield due in part to the production of lactate and also to the period of the fermentation in which growth no longer occurred.     

Continuous conversion of glutamine to glutamate by immobilized glutaminase-producing yeast

Yeast cells with a salt-tolerant and thermostable glutaminase were immobilized in silica gel (S gel) and/or alginate-silica complex gel (AS gel). The inhibition rate of the conversion rate of immobilized cells by NaCl were lower than that of free cells. The glutaminases of immobilized cells and free cells were not inactivated by heat treatment at 60°C for 1 h. The half-lives of glutaminase in AS gel were 310 d at 40°C, 40 d at 45°C, and 14 d at 50°C at a constant space velocity (SV) of 0.64. The half-life of the glutaminase activity in cells immobilized in AS gel was longer than that in S gel. By passing a filtrate of wheat gluten hydrolyzed by proteolytic enzymes through the column containing the cells immobilized in AS gel at SV of 0.20, 10 mg/ml of glutamate was continuously produced.     

Conversion of Citrate to Extracellular Glutamate by Penicillin-treated Resting Cells of Corynebacterium glutamicum

Triggering of glutamate excretion by penicillin is thought to occur by increasing cell permeability. It seemed odd that glucose-grown resting cells, after penicillin treatment, would not convert citrate to extracellular glutamate especially since citrate had been reported to be a substrate for the glutamate fermentation. Citrate was not even taken up by such cells. Upon addition of at least 2 percent glucose, citrate was converted to extracellular glutamate. Both glucose and citrate were used simultaneously and citrate metabolism continued even after sugar was exhausted. It was suspected that glucose was required as energy source for induction of a citrate-transport system. Resting cells pregrown in glucose plus citrate, were indeed found to take up citrate and convert it to extracellular glutamate even in the absence of sugar. In line with the induction hypothesis, chloramphenicol inhibited the metabolism of citrate by glucose-grown resting cells but had no such effect on the citrate-adapted cells. The antibiotic did not inhibit glucose utilization by citrate-adapted or unadapted resting cells.     

Transport of glutamine and glutamate in kidney mitochondria in relation to glutamine deamidation

1. In the absence of added ADP glutamine is transformed by pig kidney mitochondria to ammonium glutamate, which appears in the external medium. This reaction is stimulated only slightly by the addition of ADP, but under these conditions about 20% of the glutamate is oxidized to aspartate. 2. Externally added glutamate is oxidized to aspartate, and at about the same rate as glutamine. 3. The net rates of glutamine and glutamate influx into the intramitochondrial compartment are very slow. 4. The phosphate-dependent glutaminase activity of intact mitochondria is stimulated by the provision of energy. 5. The provision of energy also decreases the concentration of glutamate and increases the concentration of glutamine in the intramitochondrial compartment. These energy-linked changes in the glutamine and glutamate concentrations are of equal magnitude. 6. It is suggested that transport of glutamine and glutamate across the inner membrane of kidney mitochondria occurs by an obligatory exchange between the two metabolites, and is electrogenic. The existence of an electrogenic glutamine-glutamate anti-porter is proposed.     

Carrier-mediated glutamate secretion by Corynebacterium glutamicum under biotin limitation.

Previous studies have demonstrated the involvement of a carrier system in glutamate secretion by Corynebacterium glutamicum under biotin limitation (Hoischen, C. and Kr?mer, R. (1989) Arch. Microbiol. 151, 342-347). In a detailed analysis of the export process we found secretion to be independent of secondary forces: (i) glutamate was secreted at high rate even when external glutamate exceeded the internal concentration, (ii) movement of neither protons nor potassium or chloride ions was found to be coupled to glutamate secretion, and (iii) secretion continued unaffected after breakdown of the membrane potential. Instead, under conditions leading to variation of glutamate secretion activity, a correlation of secretion rate and the intracellular ATP-pool was observed. Thus, ATP or a related high-energy metabolite is thought to be involved in the activity of the glutamate secretion system.     

The enzymic estimation of glutamate and glutamine

A method of estimating glutamic acid is described, based on its dehydrogenation by glutamate dehydrogenase coupled, by means of N-methylphenazine methosulphate, to the reduction of tetrazolium salts. The method is suitable for the estimation of 0-0.3mumole of glutamic acid. The response is linear, but not stoicheiometric: possible reasons for this are discussed. If suitable precautions are taken, the use of a partially purified preparation of glutaminase makes it possible to estimate glutamine also.     

Gene expression of Corynebacterium glutamicum in response to the conditions inducing glutamate overproduction

AIM: The ultimate aim is to elucidate the molecular mechanisms for glutamate overproduction by Corynebacterium glutamicum. METHODS AND RESULTS: Gene expression in response to the conditions inducing glutamate overproduction was investigated by using a DNA microarray technique. Most genes involved in the EMP pathway, the PPP, and the TCA cycle were downregulated, while five genes that were highly upregulated (NCgl0917, NCgl2944, NCgl2945, NCgl2946, and NCgl2975) were identified under all the three conditions for overproduction that are studied here. Gene products of NCgl2944, NCgl2945, and NCgl2946 were highly homologous to each other, did not resemble any other protein, and have remained uncharacterized thus far. The product of NCgl0917 showed a similarity to a few hypothetical and uncharacterized proteins. NCgl2975 was homologous to metal-binding proteins. CONCLUSIONS: The decrease in the activity of 2-oxoglutarate dehydrogenase complex, a key enzyme that is downregulated during glutamate overproduction, can be mainly attributed to the downregulation of odhA and sucB. Five highly upregulated genes were also identified. SIGNIFICANCE AND IMPACT OF THE STUDY: Although fermentative production of glutamate has been carried out for more than 45 years, information on the molecular mechanisms of glutamate overproduction is still limited. This study further elucidates these mechanisms.     

Regulation of mitochondrial glutamine/glutamate metabolism by glutamate transport: studies with (15)N

We focused on the role of plasma membrane glutamate uptake in modulating the intracellular glutaminase (GA) and glutamate dehydrogenase (GDH) flux and in determining the fate of the intracellular glutamate in the proximal tubule-like LLC-PK(1)-F(+) cell line. We used high-affinity glutamate transport inhibitors D-aspartate (D-Asp) and DL-threo-beta-hydroxyaspartate (THA) to block extracellular uptake and then used [(15)N]glutamate or [2-(15)N]glutamine to follow the metabolic fate and distribution of glutamine and glutamate. In monolayers incubated with [2-(15)N]glutamine (99 atom %excess), glutamine and glutamate equilibrated throughout the intra- and extracellular compartments. In the presence of 5 mM D-Asp and 0.5 mM THA, glutamine distribution remained unchanged, but the intracellular glutamate enrichment decreased by 33% (P < 0.05) as the extracellular enrichment increased by 39% (P < 0.005). With glutamate uptake blocked, intracellular glutamate concentration decreased by 37% (P < 0.0001), in contrast to intracellular glutamine concentration, which remained unchanged. Both glutamine disappearance from the media and the estimated intracellular GA flux increased with the fall in the intracellular glutamate concentration. The labeled glutamate and NH formed from [2-(15)N]glutamine and recovered in the media increased 12- and 3-fold, respectively, consistent with accelerated GA and GDH flux. However, labeled alanine formation was reduced by 37%, indicating inhibition of transamination. Although both D-Asp and THA alone accelerated the GA and GDH flux, only THA inhibited transamination. These results are consistent with glutamate transport both regulating and being regulated by glutamine and glutamate metabolism in epithelial cells.     

Limited proteolysis of glutamine synthetase is inhibited by glutamate and by feedback inhibitors.

Limited proteolysis of glutamine synthetase from Escherichia coli has been studied under nondenaturing conditions (pH 7.6, 20 degrees C). Trypsin cleaves the polypeptide chain of glutamine synthetase into two principal fragments, Mr = about 32,000 and 18,000. The covalently bound AMP group is attached to the larger fragment and its presence does not affect cleavage. Although the cleaved polypeptide chain does not dissociate under nondenaturing conditions, catalytic activity is lost. Chymotrypsin and Staphylococcus aureus protease produce similar cleavages in glutamine synthetase. The substrate L-glutamate retards tryptic as well as chymotryptic digestion. Tryptic digestion is also retarded by some of the feedback inhibitors of glutamine synthetase including CTP, L-alanine, L-serine, L-histidine, and glucosamine 6-phosphate. An implication of these findings is that there is a region of the glutamine synthetase polypeptide chain that is particularly susceptible to proteolysis. Either the glutamate and inhibitor sites are formed partly by this suceptible peptide or the binding of glutamate and some inhibitors induces conformational changes within the E. coli glutamine synthetase molecule in the region of the susceptible peptide.     

Production of glutamine by micro-gel bead-immobilized Corynebacterium glutamicum 9703-T cells in a stirred tank reactor

The effectiveness of using micro-gel bead-immobilized cells for aerobic processes was investigated. Glutamine production by Corynebacterium glutamicum, 9703-T, cells was used as an example. The cells were immobilized in Sr-alginate micro-gel beads 500 m in diameter and used for fermentation processes in a stirred tank reactor with a modified impeller at 400 min^–1. Continuous production of glutamine was carried out for more than 220 h in this reactor and no gel breakage was observed. As a result of the high oxygen transfer capacity of this system, the glutamine yield from glucose was more than three times higher, while the organic acid accumulation was more than 24 times lower than those obtained with 3.0 mm-gel bead-immobilized cells in an airlift fermentor under similar experimental conditions. During the continuous fermentations there was evolution and proliferation of non-glutamine producing strains which led to a gradual decrease in the productivity of the systems. Although a modified production medium which suppresses cell growth during the production phase was effective in maintaining the productivity, the stability of the whole system was shortened due to high cell deactivation rate in such a medium.List of Symbols C kg/m³ glutamine concentration - C _A mol/m ³ local oxygen concentration inside the gel beads - C _AS mol/m ³ oxygen concentration at the surface of the gel beads - De m²/h effective diffusion coefficient of oxygen in the gel bead - DO mol/m³ dissolved oxygen concentration - F dm³/h medium flow rate - K h^–1 glutamine decomposition rate constant - Km mol/m³ Michaelis Menten constant - QO _2max mol/(kg · h) maximum specific respiration rate - R m radius of the gel beads - r m radial distance - t h time - V _C dm ³ volume of the gel beads - V _L dm ³ liquid volume in the reactor - Vm mol/(m³ · h) maximum respiration rate - X kg/m³ cell concentration - x r/R - y C _A /C_AS - h^–1 cell deactivation rate constant - Thiele modulus defined by R(Vm/De Km) ^1/2 - C _AS /Km - _C kg/(m³-gel · h) specific glutamine formation rate - _c dm³-gel/dm³ V _C /V _L      

Conversion of L-Hydroxyproline to glutamate by extracts of strains of Pseudomonas convexa and Pseudomonas fluorescens

Summary Three strains of Pseudomonas convexa and three strains of Pseudomonas fluorescens were found able to utilize L-hydroxyproline as sole source of carbon and nitrogen. Sonic extracts of these organisms converted L-hydroxyproline to glutamic acid.     

Glutamate excretion by Corynebacterium glutamicum: a study of glutamate accumulation during a fermentation course

Summary Corynebacterium glutamicum was used in fed-batch fermentation for glutamate production. Both intracellular and extracellular concentrations were determined which allowed us to study the repartition of the amino acid according to the culture conditions and in the presence or absence of surfactants. A decrease in cell volume was observed after addition of surfactants during the exponential phase of growth; glutamate accumulates in the cell, whereas in standard industrial conditions the glutamate concentration in the medium during the production phase can be 30-fold higher than that found inside the cell. The level of excretion is compatible with industrial production.     

Ammonia assimilation in Corynebacterium glutamicum and a glutamate dehydrogenase-deficient mutant

In the wild-type of Corynebacterium glutamicum, the specific activity of glutamate dehydrogenase (GDH) remained constant at 1.3 U (mg protein)–1 when raising the ammonia (NH4) concentration in the growth medium from 1 to 90 mM. In contrast, the glutamine synthetase (GS) and glutamate synthase (GOGAT) activities decreased from 1.1 U (mg protein)–1 and 42 mU (mg protein)–1, respectively, to less than 10 % of these values at NH4 concentrations > 10 mM suggesting that under these conditions the GDH reaction is the primary NH4 assimilation pathway. Consistent with this suggestion, a GDH-deficient C. glutamicum mutant showed slower growth at NH4 concentrations 10 mM and, in contrast to the wild-type, did not grow in the presence of the GS inhibitor methionine sulfoximine. © Rapid Science Ltd. 1998     

Evidence for an efflux carrier system involved in the secretion of glutamate by Corynebacterium glutamicum

Corynebacterium glutamicum effectively secretes L-glutamate when growing under biotin limitation. The secretion of glutamate was studied with respect to kinetic and energetic parameters: rate of glutamate uptake and efflux, specificity of transport, dependence of efflux on the energy state of the cell, concentration gradient of glutamate and ions, and membrane potential. By comparing these parameters when measured in biotin-limited, i.e. producer cells, and biotin-supplemented, i.e. non-producer cells, respectively, the following conclusions could be drawn: 1. The efflux of L-glutamate in C. glutamicum cannot be explained by passive permeation of this amino acid through the plasma membrane, as it has been assumed in the generally accepted model of glutamate secretion in biotin-limited cells. 2. It is unlikely that the efflux of glutamate occurs via an inversion of the glutamate uptake system. 3. Based on our results concerning the specificity and the kinetics of glutamate transport as well as the observed regulation phenomena, we conclude that secretion of glutamate in C. glutamicum occurs by a special efflux carrier system.Abbreviations dw dry weight - OD optical density - TPP tetraphenyl phosphonium bromide