Modelling L-glutamic acid production with Corynebacterium glutamicum under biotin limitation

The production of L-glutamic acid with Corynebacterium glutamicum under biotin limitation was studied. Assuming a formal type of cell maturation, an adequate formal kinetic model was developed. This model includes growth, dependent on biotin, and uses the same retention term for describing the lag phase and cell maturation. Special attention was paid to the graphical interpretation of the performance between the variables, which is relevant for kinetics. Comparison between experiments and the model resulted in different degrees of agreement. However, the main trend of the experimental patterns of the complex bioprocess can clearly be mirrored in this model.     

Modelling of the L-glutamic acid production with Corynebacterium glutamicum under biotin limitation

Production of L-glutamic acid with Corynebacterium glutamicum, under biotin limitation was studied. On the base of formal kinetic approach, a mathematical model was developed, which included formal growth inhibition with product, and production repression with substrate. For the testing of computer simulations experiments were carried out and the results have been compared.     

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.     

Improved L-lysine yield with Corynebacterium glutamicum: use of dapA resulting in increased flux combined with growth limitation

The amino acid L-lysine is produced on a large scale using mutants of Corynebacterium glutamicum. However, as yet recombinant DNA techniques have not succeed in improving strains selected for decades by classic mutagenesis for high productivity. We here report that seven biosynthetic enzymes were assayed and oversynthesis of the dihydrodipicolinate synthase resulted in an increase of lysine accumulation from 220 mM to 270 mM. The synthase, encoded by dapA, is located at the branch point of metabolite distribution to either lysine or threonine and competes with homoserine dehydrogenase for the common substrate aspartate semialdehyde. When graded dapA expression was used, as well as quantification of enzyme activities, intracellular metabolite concentrations and flux rates, a global response of the carbon metabolism to the synthase activity became apparent: the increased flux towards lysine was accompanied by a decreased flux towards threonine. This resulted in a decreased growth rate, but increased intracellular levels of pyruvate-derived valine and alanine. Therefore, modulating the flux at the branch point results in an intrinsically introduced growth limitation with increased intracellular precursor supply for lysine synthesis. This does not only achieve an increase in lysine yield but this example of an intracellularly introduced growth limitation is proposed as a new general means of increasing flux for industrial metabolite overproduction. Received: 8 August 1997 / Received revision: 2 October 1997 / Accepted: 14 October 1997     

Increased expression of pyruvate carboxylase and biotin protein ligase increases lysine production in a biotin prototrophic Corynebacterium glutamicum strain

Corynebacterium glutamicum, a Gram‐positive bacterium used for the production of various biochemicals, is naturally a biotin auxotroph. We introduced the biotin genes from Bacillus subtilis on a plasmid, pBIO, into a lysine‐producing derivative (termed AHP‐3) that has been described previously, and achieved biotin prototrophy. We found that AHP‐3, containing pBIO, was able to produce lysine in a medium lacking biotin and that the lysine yield on glucose was similar to what is obtained when using a medium containing biotin. However, there was a decrease in specific growth rate of 20% when the strain was cultivated without biotin, indicating a suboptimal intracellular concentration of biotin. In an attempt to locate the potential bottleneck, we added pimelic acid, an early biotin precursor, and found that growth rate could be restored fully, which demonstrates that the bottleneck is in pimeloyl‐CoA (or pimeloyl‐Acyl Carrier Protein [ACP]) formation. Pyruvate carboxylase (pycA), a biotin‐dependent enzyme needed for lysine biosynthesis and biotin ligase (birA), which is responsible for attaching biotin to pyruvate carboxylase, were overexpressed by replacing the native promoters with the strong superoxide dismutase (sod) promoter, to see whether growth could be restored. Neither pycA nor birA overexpression, whether alone or in combination, had an effect on specific growth rate, but they did have a positive effect on lysine yield, which increased by 55% in the strain overexpressing both enzymes.     

Secretion of human epidermal growth factor by Corynebacterium glutamicum

AIMS: To examine the secretion of human epidermal growth factor (hEGF) by Corynebacterium glutamicum. METHODS AND RESULTS: We recently showed that a novel protein-secretion system in C. glutamicum could produce Streptomyces mobaraensis transglutaminase. In the present study, the industrially important protein hEGF was secreted into the culture medium in a fully active form by C. glutamicum and accumulated at a rate of up to 156 mg l(-1) day(-1). CONCLUSIONS: These results demonstrated that the hEGF protein could be secreted in an active form by C. glutamicum. SIGNIFICANCE AND IMPACT OF THE STUDY: Our data confirmed that the pharmaceutically important human protein hEGF could be efficiently secreted in an active form by the C. glutamicum protein-expression system. Moreover, we demonstrated that this bacterium has potential as a host for the industrial-scale production of human proteins.     

Effect of oxygen limitation on cellular L-lysine pool and lipid spectrum of Corynebacterium glutamicum

Summary During submerged cultivation of L-lysine producing Corynebacterium glutamicum 9366, oxygen limitation caused a three-fold increase in the intracellular pool of L-lysine while its excretion into the medium cased. At the same time, the phospholipid content of cells increased markedly whereas the proportion of oleic acid in the fatty acids of phospholipids decreased.     

A Corynebacterium glutamicum gene encoding a two-domain protein similar to biotin carboxylases and biotin-carboxyl-carrier proteins

Following the analysis of transposon Tn5432-induced mutants of Corynebacterium glutamicum ATCC 13032, a gene encoding a protein with a biotin-binding motif was cloned. The DNA sequence of this gene revealed an open reading frame encoding 591 amino acids with a calculated mol. mass of 63.4 kDa. The protein is composed of two domains, an N-terminal biotin carboxylase and a C-terminal biotin-carboxyl-carrier protein, that are highly similar to corresponding subunits from prokaryotic and eukaryotic biotin enzymes. Over 70% identity was found to a protein from Mycobacterium leprae proposed to be part of an acyl-CoA carboxylase. Since it was not possible to inactivate the C. glutamicum gene, the gene most likely encodes a subunit of the essential acetyl-CoA carboxylase, which catalyzes the committed step in fatty acid synthesis. Received: 2 December 1995 / Accepted: 20 May 1996     

Xylitol production by recombinant Corynebacterium glutamicum under oxygen deprivation

Wild-type Corynebacterium glutamicum produced 0.6 g l⁻¹ xylitol from xylose at a productivity of 0.01 g l⁻¹ h⁻¹ under oxygen deprivation. To increase this productivity, the pentose transporter gene (araE) from C. glutamicum ATCC31831 was integrated into the C. glutamicum R chromosome. Consequent disruption of its lactate dehydrogenase gene (ldhA), and expression of single-site mutant xylose reductase from Candida tenuis (CtXR (K274R)) resulted in recombinant C. glutamicum strain CtXR4 that produced 26.5 g l⁻¹ xylitol at 3.1 g l⁻¹ h⁻¹. To eliminate possible formation of toxic intracellular xylitol phosphate, genes encoding xylulokinase (XylB) and phosphoenolpyruvate-dependent fructose phosphotransferase (PTS^fru) were disrupted to yield strain CtXR7. The productivity of strain CtXR7 increased 1.6-fold over that of strain CtXR4. A fed-batch 21-h CtXR7 culture in mineral salts medium under oxygen deprivation yielded 166 g l⁻¹ xylitol at 7.9 g l⁻¹ h⁻¹, representing the highest bacterial xylitol productivity reported to date.     

Production of organic acids by Corynebacterium glutamicum under oxygen deprivation

Under oxygen deprivation, aerobic Corynebacterium glutamicum produce organic acids from glucose at high yields in mineral medium even though their proliferation is arrested. To develop a new, high-productivity bioprocess based on these unique features, characteristics of organic acid production by C. glutamicum under oxygen deprivation were investigated. The main organic acids produced from glucose under these conditions were lactic acid and succinic acid. Addition of bicarbonate, which is a co-substrate for anaplerotic enzymes, increased the glucose consumption rate, leading to increased organic acid production rates. With increasing concentration of bicarbonate, the yield of succinic acid increased, whereas that of lactic acid decreased. There was a direct correlation between cell concentration and organic acid production rates even at elevated cell densities, and productivities of lactic acid and succinic acid were 42.9 g l⁻¹ h⁻¹ and 11.7 g l⁻¹ h⁻¹, respectively, at a cell concentration of 60 g dry cell l⁻¹. This cell-recycling continuous reaction demonstrated that rates of organic acid production by C. glutamicum could be maintained for at least 360 h.     

Evolutionary engineering of Corynebacterium glutamicum

A unique feature of biotechnology is that we can harness the power of evolution to improve process performance. Rational engineering of microbial strains has led to the establishment of a variety of successful bioprocesses, but it is hampered by the overwhelming complexity of biological systems. Evolutionary engineering represents a straightforward approach for fitness‐linked phenotypes (e.g., growth or stress tolerance) and is successfully applied to select for strains with improved properties for particular industrial applications. In recent years, synthetic evolution strategies have enabled selection for increased small molecule production by linking metabolic productivity to growth as a selectable trait. This review summarizes the evolutionary engineering strategies performed with the industrial platform organism Corynebacterium glutamicum. An increasing number of recent studies highlight the potential of adaptive laboratory evolution (ALE) to improve growth or stress resistance, implement the utilization of alternative carbon sources, or improve small molecule production. Advances in next‐generation sequencing and automation technologies will foster the application of ALE strategies to streamline microbial strains for bioproduction and enhance our understanding of biological systems.     

外源精氨酸对谷氨酸棒杆菌在高葡萄糖胁迫下生长和发酵特性的影响

【目的】探究外源添加不同氨基酸和相容性溶质对谷氨酸棒杆菌(Corynebacterium glutamicum)在高糖胁迫环境下生长的影响及可能的作用机理。【方法】通过在培养基中外源添加各种氨基酸和相容性溶质,研究其对谷氨酸棒杆菌在高葡萄糖和高蔗糖胁迫下生长的影响,并分析添加精氨酸对高葡萄糖胁迫下菌株糖转运和代谢途径中关键酶转录水平的影响,以及对菌株发酵产氨基酸的影响。进一步探究了碱性氨基酸在其它棒状杆菌属中抵御高葡萄糖胁迫的潜在作用。【结果】在高葡萄糖胁迫条件下,外源添加赖氨酸、精氨酸和组氨酸后谷氨酸棒杆菌的生物量分别提高54.7%、50.0%和37.6%;而在高蔗糖胁迫条件下,添加脯氨酸和四氢嘧啶后菌株生物量增加20%以上。进一步研究表明,在高葡萄糖胁迫下,外源添加精氨酸后谷氨酸棒杆菌的葡萄糖利用速率提高约2.5倍,谷氨酸的发酵产量也增加了127.5%。此外,碱性氨基酸对其它4种棒状杆菌也具有一定的渗透保护效应。【结论】精氨酸对谷氨酸棒杆菌在高葡萄糖胁迫下具有良好的渗透保护作用,可能归因于其能促进葡萄糖的转运和代谢能力,同时发现碱性氨基酸的渗透保护效应对棒状杆菌属具有一定的普遍性。     

Detoxification of furfural in Corynebacterium glutamicum under aerobic and anaerobic conditions

The toxic fermentation inhibitors in lignocellulosic hydrolysates raise serious problems for the microbial production of fuels and chemicals. Furfural is considered to be one of the most toxic compounds among these inhibitors. Here, we describe the detoxification of furfural in Corynebacterium glutamicum ATCC13032 under both aerobic and anaerobic conditions. Under aerobic culture conditions, furfuryl alcohol and 2-furoic acid were produced as detoxification products of furfural. The ratio of the products varied depending on the initial furfural concentration. Neither furfuryl alcohol nor 2-furoic acid showed any toxic effect on cell growth, and both compounds were determined to be the end products of furfural degradation. Interestingly, unlike under aerobic conditions, most of the furfural was converted to furfuryl alcohol under anaerobic conditions, without affecting the glucose consumption rate. Both the NADH/NAD⁺ and NADPH/NADP⁺ ratio decreased in the accordance with furfural concentration under both aerobic and anaerobic conditions. These results indicate the presence of a single or multiple endogenous enzymes with broad and high affinity for furfural and co-factors in C. glutamicum ATCC13032.     

Metabolic activity of Corynebacterium glutamicum grown on l-lactic acid under stress

Respiration measurement in shake flasks is introduced as a new method to characterize the metabolic activity of microorganisms during and after stress exposure. The major advantage of the new method is the possibility to determine the metabolic activity independent of manual sampling without the necessity to change the culture vessel or the cultivation medium. This excludes stress factors, which may be induced by transferring the microorganisms to plates or respirometers. The negative influence, which interruptions of the shaker during sampling times may have on the growth of microorganisms was demonstrated. The applicability of the method was verified by characterizing the behavior of Corynebacterium glutamicum grown on the carbon source l-lactic acid under stress factors such as carbon starvation, anaerobic conditions, lactic acid, osmolarity, and pH. The following conditions had no effect on the metabolic activity of C. glutamicum: a carbon starvation of up to 19 h, anaerobic conditions, lactic acid concentrations up to 10 g/l, 3-(N-morpholino) propanesulfonic acid buffer concentrations up to 42 g/l, or pH from 6.4 to 7.4. Lactic-acid concentrations from 10 to 30 g/l lead to a decrease of the growth rate and the biomass substrate yield without effecting the oxygen substrate conversion. Without adaptation, the organism did not grow at pH≤5 or ≥9.