Metabolic engineering of Corynebacterium glutamicum for L-serine production

Although L-serine proceeds in just three steps from the glycolytic intermediate 3-phosphoglycerate, and as much as 8% of the carbon assimilated from glucose is directed via L-serine formation, previous attempts to obtain a strain producing L-serine from glucose have not been successful. We functionally identified the genes serC and serB from Corynebacterium glutamicum, coding for phosphoserine aminotransferase and phosphoserine phosphatase, respectively. The overexpression of these genes, together with the third biosynthetic serA gene, serA(delta197), encoding an L-serine-insensitive 3-phosphoglycerate dehydrogenase, yielded only traces of L-serine, as did the overexpression of these genes in a strain with the L-serine dehydratase gene sdaA deleted. However, reduced expression of the serine hydroxymethyltransferase gene glyA, in combination with the overexpression of serA(delta197), serC, and serB, resulted in a transient accumulation of up to 16 mM L-serine in the culture medium. When sdaA was also deleted, the resulting strain, C. glutamicum delta sdaA::pK18mobglyA'(pEC-T18mob2serA(delta197)CB), accumulated up to 86 mM L-serine with a maximal specific productivity of 1.2 mmol h(-1) g (dry weight)(-1). This illustrates a high rate of L-serine formation and also utilization in the C. glutamicum wild type. Therefore, metabolic engineering of L-serine production from glucose can be achieved only by addressing the apparent key position of this amino acid in the central metabolism.     

Cometabolism of a nongrowth substrate: L-serine utilization by Corynebacterium glutamicum

Despite its key position in central metabolism, L-serine does not support the growth of Corynebacterium glutamicum. Nevertheless, during growth on glucose, L-serine is consumed at rates up to 19.4 +/- 4.0 nmol min(-1) (mg [dry weight])(-1), resulting in the complete consumption of 100 mM L-serine in the presence of 100 mM glucose and an increased growth yield of about 20%. Use of 13C-labeled L-serine and analysis of cellularly derived metabolites by nuclear magnetic resonance spectroscopy revealed that the carbon skeleton of L-serine is mainly converted to pyruvate-derived metabolites such as L-alanine. The sdaA gene was identified in the genome of C. glutamicum, and overexpression of sdaA resulted in (i) functional L-serine dehydratase (L-SerDH) activity, and therefore conversion of L-serine to pyruvate, and (ii) growth of the recombinant strain on L-serine as the single substrate. In contrast, deletion of sdaA decreased the L-serine cometabolism rate with glucose by 47% but still resulted in degradation of L-serine to pyruvate. Cystathionine beta-lyase was additionally found to convert L-serine to pyruvate, and the respective metC gene was induced 2.4-fold under high internal L-serine concentrations. Upon sdaA overexpression, the growth rate on glucose is reduced 36% from that of the wild type, illustrating that even with glucose as a single substrate, intracellular L-serine conversion to pyruvate might occur, although probably the weak affinity of L-SerDH (apparent Km, 11 mM) prevents substantial L-serine degradation.     

Functional analysis of L-serine O-acetyltransferase from Corynebacterium glutamicum

We report here the function of L-serine O-acetyltransferase (SAT) from the glutamic acid-producing bacterium Corynebacterium glutamicum. Based on the genome sequence of C. glutamicum and the NH(2)-terminal amino-acid sequence, the gene encoding SAT (cysE) was cloned and expressed in C. glutamicum. Deletion analysis of the 5'-noncoding region showed a putative -10 region ((-27)TTAAGT(-22) or (-26)TAAGTC(-21)) and a possible ribosome-binding site ((-12)AGA(-10)) just upstream from the start codon. We found that the SAT activity was sensitive to feedback inhibition by L-cysteine, and that SAT synthesis was repressed by L-methionine. Further, cysE-disrupted cells showed L-cysteine auxotrophy, indicating that C. glutamicum synthesizes L-cysteine from L-serine via O-acetyl-L-serine through the pathway involving SAT and O-acetyl-L-serine sulfhydrylase in the same manner as Escherichia coli.     

Increasing available NADH supply during succinic acid production by Corynebacterium glutamicum

A critical factor in the biotechnological production of succinic acid with Corynebacterium glutamicum is the sufficient supply of NADH. It is conceivable that cofactor availability and the proportion of cofactor in the active form may play an important role in dictating the succinic acid yield. PntAB genes from Escherichia coli can directly catalyze the reversible hydride transfer and adjust the dynamic balance between NADP(H) and NAD(H). Hence, we studied the physiological effect of coenzyme systems by expressing the membrane‐bound transhydrogenase pntAB genes. We have shown experimentally that the pntAB genes could function as an alternative source of NADH. In an anaerobic fermentation with C. glutamicum NC‐3‐pntAB, a 16% higher succinic acid yield and a 57% higher production from glucose were obtained by pntAB expression. Moreover, the formation of by‐products was significantly decreased. The concomitant increase in the consumption of intracellular NADPH from 0.6 to 1.2 mmol/g CDW and the increased NADH/NAD⁺ ratio resulted from introduction of pntAB, suggesting that the membrane‐bound transhydrogenase converted excess NADPH to NADH for succinic acid production. Finally, we explored whether the transhydrogenase had different effects on the succinic acid formation on different carbon sources. The succinic acid yield was increased in the presence of pntAB by 16% on glucose, 7% on sucrose, and without large influence on fructose and xylose. The results of this study demonstrated that the effectiveness of cofactor manipulation could be a promising strategy applied in metabolic engineering. © 2014 American Institute of Chemical Engineers Biotechnol. Prog., 31:12–19, 2015     

谷氨酸棒杆菌SYPS-062合成L-丝氨酸的代谢通量分析

以一株由自然界筛选获得的能够利用糖质原料直接产L-丝氨酸的谷氨酸棒杆菌Corynebacterium glutamicum SYPS-062为研究对象,考察了一碳单元循环中的辅因子—叶酸和维生素B12对菌株生长、蔗糖消耗及L-丝氨酸生成的影响,同时对处于对数生长期的菌株进行了代谢流量分析。结果发现,添加扰动因子叶酸和维生素B12对磷酸戊糖途径(HMP)碳流影响较大,碳源主要用于细胞生长及合成能量,而流向目的产物L-丝氨酸的碳流减少。同时在添加维生素B12时,增大了G3P节点的L-丝氨酸合成途径的分流比,但造成三羧酸循环(TCA)的流量不足,需要大量回补,从而限制了产物合成速率的进一步提高。     

Putrescine production by engineered Corynebacterium glutamicum

Here, we report the engineering of the industrially relevant Corynebacterium glutamicum for putrescine production. C. glutamicum grew well in the presence of up to 500 mM of putrescine. A reduction of the growth rate by 34% and of biomass formation by 39% was observed at 750 mM of putrescine. C. glutamicum was enabled to produce putrescine by heterologous expression of genes encoding enzymes of the arginine- and ornithine decarboxylase pathways from Escherichia coli. The results showed that the putrescine yield by recombinant C. glutamicum strains provided with the arginine-decarboxylase pathway was 40 times lower than the yield by strains provided with the ornithine decarboxylase pathway. The highest production efficiency was reached by overexpression of speC, encoding the ornithine decarboxylase from E. coli, in combination with chromosomal deletion of genes encoding the arginine repressor ArgR and the ornithine carbamoyltransferase ArgF. In shake-flask batch cultures this strain produced putrescine up to 6 g/L with a space time yield of 0.1 g/L/h. The overall product yield was about 24 mol% (0.12 g/g of glucose).     

Enhancing the carbon flux and NADPH supply to increase L-isoleucine production in Corynebacterium glutamicum

Our previous work has shown that L-isoleucine production in Corynebacterium glutamicum IWJ001 could be increased by overexpressing ilvA1 encoding a feedback-resistant threonine dehydratase, ilvBN1 encoding a feedback-resistant acetohydroxy acid synthase, lrp encoding the global regulator Lrp, brnFE encoding the two-component export system BrnFE, or ppnk1 encoding NAD kinase. The main purpose of this study is to further increase the L-isoleucine production in C. glutamicum IWJ001 by overexpressing the above genes in various combinations. Several C. glutamicum strains IWJ001/pDXW-8-ppnk1-lrp-brnFE, IWJ001/pDXW-8-ilvBN1-ilvA1-lrp-brnFE, IWJ001/pDXW-8-ilvBN1-ilvA1-ppnk1, and IWJ001/pDXW-8-ppnk1-ilvBN1-ilvA1-lrp-brnFE were constructed, and L-isoleucine production and activities of several key enzymes in these strains were analyzed. Compared with the control strain IWJ001/pDXW-8, L-isoleucine production increased in all of the four strains. IWJ001/pDXW-8-ilvBN1-ilvA1-ppnk1 showed the highest L-isoleucine production and produced 32.3 g/L L-isoleucine in 72 h fed batch fermentation. The results indicate that L-isoleucine production in C. glutamicum could be increased by enhancing the carbon flux and NADPH supply in the biosynthetic pathway.     

L-Tyrosine production by Polyauxotrophic Mutants of Corynebacterium glutamicum

Polyauxotrophic mutants of Corynebacterium glutamicum which have additional requirements to L-phenylalanine were derived from L-tyrosine producing strains of phenylalanine auxotrophs, C. glutamicum KY 9189 and C. glutamicum KY 10233, and screened for L-tyrosine production. The increase of L-tyrosine production was noted in many auxotrophic mutants derived from both strains. Especially some double auxotrophs which require phenylalanine and purine, phenylalanine and histidine, or phenylalanine and cysteine produced significantly higher amounts of L-tyrosine compared to the parents, A phenylalanine and purine double auxotrophic strain LM–96 produced L-tyrosine at a concentration of 15.1 mg per ml in the medium containing 20% sucrose. L-Tyrosine production by the strain decreased at high concentrations of L-phenylalanine.     

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.     

Carboxylic acid consumption and production by Corynebacterium glutamicum

Corynebacterium glutamicum is well-known as an industrial workhorse, most notably for its use in the bulk production of amino acids in the feed and food sector. Previous studies of the effect of gradients in scale-down reactors with complex media disclosed an accumulation of several carboxylic acids and a parallel decrease of growth and product accumulation. This study, therefore, addresses the impact of carboxylic acids, for example, acetate and l -lactate, on the cultivation of the cadaverine producing strain C. glutamicum DM1945Δact3:P_tuf-ldcC^opt and their potential role in scale up related performance losses. A fluctuating power input in shake flask and stirred tank cultivations with mineral salt was applied to mimic discontinuous oxygen availability. Results demonstrate, whenever sufficient oxygen was available, C. glutamicum recovered from previously occurring stressful conditions like an oxygen limiting phase. Reassimilation of acids was detected simultaneously. In cultures, which were supplemented with either acetate or l -lactate, a rapid cometabolization of both acids in presence of glucose was observed, showing conversion rates of 7.8 and 3.8 mmol g_{cell dry weight}⁻¹ hr⁻¹, respectively. Uptake of these acids was accompanied by increased oxygen consumption. Proteins related to oxidative stress response, glycogen synthesis, and the main carbon metabolism were found in altered concentrations under oscillatory cultivation conditions. (Proteomics data are available via ProteomeXchange with identifier PXD012760). Virtually no impact on growth or product formation was observed. We conclude that the reduced growth and product formation in scale-down cultivations when complex media was used is not caused by the accumulation of carboxylic acids.     

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.     

Engineering Corynebacterium glutamicum for isobutanol production

The production of isobutanol in microorganisms has recently been achieved by harnessing the highly active 2-keto acid pathways. Since these 2-keto acids are precursors of amino acids, we aimed to construct an isobutanol production platform in Corynebacterium glutamicum, a well-known amino-acid-producing microorganism. Analysis of this host’s sensitivity to isobutanol toxicity revealed that C. glutamicum shows an increased tolerance to isobutanol relative to Escherichia coli. Overexpression of alsS of Bacillus subtilis, ilvC and ilvD of C. glutamicum, kivd of Lactococcus lactis, and a native alcohol dehydrogenase, adhA, led to the production of 2.6 g/L isobutanol and 0.4 g/L 3-methyl-1-butanol in 48 h. In addition, other higher chain alcohols such as 1-propanol, 2-methyl-1-butanol, 1-butanol, and 2-phenylethanol were also detected as byproducts. Using longer-term batch cultures, isobutanol titers reached 4.0 g/L after 96 h with wild-type C. glutamicum as a host. Upon the inactivation of several genes to direct more carbon through the isobutanol pathway, we increased production by ∼25% to 4.9 g/L isobutanol in a ∆pyc∆ldh background. These results show promise in engineering C. glutamicum for higher chain alcohol production using the 2-keto acid pathways.     

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.     

L-Glutamate production by lysozyme-sensitive Corynebacterium glutamicum ltsA mutant strains

Background  

Infections of bacterial cultures by bacteriophages are serious problems in biotechnological laboratories. Apart from such infections, prophage induction in the host cells may also be dangerous. Escherichia coli is a commonly used host in biotechnological production, and many laboratory strains of this bacterium harbour lambdoid prophages. These prophages may be induced under certain conditions leading to phage lytic development. This is fatal for further cultivations as relatively low, though still significant, numbers of phages may be overlooked. Thus, subsequent cultures of non-lysogenic strains may be infected and destroyed by such phage.     

Effects of pyruvate kinase on the growth of Corynebacterium glutamicum and L-serine accumulation

Pyruvate kinase (PYK) is an important enzyme in the intermediary metabolism and has attracted much attention as a target for metabolic engineering of Corynebacterium glutamicum. Genome sequencing revealed that the 308 residue of PYK was mutated from methionine in model strain C. glutamicum ATCC14067 to isoleucine in L-serine-producing strain C. glutamicum SYPS-062. Consequently, a significantly lower PYK activity (77%) was noted in C. glutamicum SYPS-062, when compared with that in C. glutamicum ATCC14067. To confirm the role of this point mutation, pyk in both C. glutamicum SYPS-062 and C. glutamicum SYPS-062-33aΔSSAA was reversely mutated to restore the PYK enzyme activity, which led to a 33.1% and 28.8% decrease in L-serine titer, respectively. This is the first report to show that the (Met-308→Ile) mutation site of pyk is closely associated with its activity and apparently affected L-serine production. Furthermore, pyk was deleted in strain C. glutamicum SYPS-062-33aΔSSAA, and the resulting strain did not show alteration in growth rate and presented a 12% increase in L-serine production.     

Medium optimization for L-phenylalanine production by a tryptophan auxotroph of Corynebacterium glutamicum

Summary By screening 15,000 mutants, tyrosine auxotrophs T6, T7, and tryptophan auxotrophs P6, P8, were obtained. After primary production test, mutant P6 was chosen for further investigation. Fractional factorial design(FFD) and steepest ascent method(SAM) were used to optimize the medium component Mutant P6 had 17.1 g/l L-phenylalanine production when 0.44 g/l tryptophan was added. When Corynebacterium glutamicum P6 was cultivated in the optimum medium, L-phenylaianine production increased 22% as compared with the parent strain CCRC 18335, and the interference of tryptophan during the purification process was removed.     

Potential metabolic limitations in lysine production by Corynebacterium glutamicum as revealed by metabolic network analysis

Analysis of the metabolic network of lysine-producing Corynebacterium glutamicum showed that lysine yields are limited by the excess energy production in lysine biosynthesis. The most probable maximum yield is 0.47 mol/mol on glucose, when phosphoenolpyruvate carboxylase functions in an anaplerotic rection. When this function is fulfilled by the glyoxylate pathway, a maximum yield of 0.38 mol/mol is obtained.     

谷氨酸棒杆菌SYPS-062 L-丝氨酸脱水酶活性分析及其基因敲除对L-丝氨酸积累的影响

以谷氨酸棒杆菌(Corynebacterium glutamicum) SYPS-062基因组DNA为模板,扩增得到L-丝氨酸脱水酶(L-SerDH)的编码基因sdaA。将其克隆到表达载体pET-28a(+),并在E.coli BL21(DE3)中诱导表达,对纯化的L-SerDH进行了酶活测定,并与来自C.glutamicum ATCC13032的重组L-SerDH进行了比较,结果显示,两种不同菌株来源的重组L-SerDH降解L-丝氨酸的酶比活力差异并不显著。在此基础上敲除菌株SYPS-062 的sdaA基因,探讨该基因对C.glutamicum SYPS-062生长及产酸的影响。通过构建自杀型重组质粒pK18mobsacB-△sdaA,电击转入C.glutamicum SYPS-062中,以同源重组的方式获得了sdaA基因缺失突变株,并用PCR方法对突变株C.glutamicum SYPS-062△sdaA进行了验证。与出发菌株相比,突变菌株生长缓慢,单位菌体L-丝氨酸的产量(Y_P/X)提高了15.13%。     

Glutamic acid production with gel-entrapped Corynebacterium glutamicum

A glutamic acid producing microorganism (Corynebacterium glutamicum) is entrapped in a polyacrylamide gel. These immobilized microorganisms were used to produce glutamic acid in successive batches of fresh medium. Free microorganisms similarly used produced much less glutamic acid under similar conditions.