Engineering of Corynebacterium glutamicum for High-Yield l-Valine Production under Oxygen Deprivation Conditions

We previously demonstrated efficient l-valine production by metabolically engineered Corynebacterium glutamicum under oxygen deprivation. To achieve the high productivity, a NADH/NADPH cofactor imbalance during the synthesis of l-valine was overcome by engineering NAD-preferring mutant acetohydroxy acid isomeroreductase (AHAIR) and using NAD-specific leucine dehydrogenase from Lysinibacillus sphaericus. Lactate as a by-product was largely eliminated by disrupting the lactate dehydrogenase gene ldhA. Nonetheless, a few other by-products, particularly succinate, were still produced and acted to suppress the l-valine yield. Eliminating these by-products therefore was deemed key to improving the l-valine yield. By additionally disrupting the phosphoenolpyruvate carboxylase gene ppc, succinate production was effectively suppressed, but both glucose consumption and l-valine production dropped considerably due to the severely elevated intracellular NADH/NAD⁺ ratio. In contrast, this perturbed intracellular redox state was more than compensated for by deletion of three genes associated with NADH-producing acetate synthesis and overexpression of five glycolytic genes, including gapA, encoding NADH-inhibited glyceraldehyde-3-phosphate dehydrogenase. Inserting feedback-resistant mutant acetohydroxy acid synthase and NAD-preferring mutant AHAIR in the chromosome resulted in higher l-valine yield and productivity. Deleting the alanine transaminase gene avtA suppressed alanine production. The resultant strain produced 1,280 mM l-valine at a yield of 88% mol mol of glucose⁻¹ after 24 h under oxygen deprivation, a vastly improved yield over our previous best.     

Platform Engineering of Corynebacterium glutamicum with Reduced Pyruvate Dehydrogenase Complex Activity for Improved Production of l-Lysine,l-Valine,and 2-Ketoisovalerate

Exchange of the native Corynebacterium glutamicum promoter of the aceE gene, encoding the E1p subunit of the pyruvate dehydrogenase complex (PDHC), with mutated dapA promoter variants led to a series of C. glutamicum strains with gradually reduced growth rates and PDHC activities. Upon overexpression of the l-valine biosynthetic genes ilvBNCE, all strains produced l-valine. Among these strains, C. glutamicum aceE A16 (pJC4 ilvBNCE) showed the highest biomass and product yields, and thus it was further improved by additional deletion of the pqo and ppc genes, encoding pyruvate:quinone oxidoreductase and phosphoenolpyruvate carboxylase, respectively. In fed-batch fermentations at high cell densities, C. glutamicum aceE A16 Δpqo Δppc (pJC4 ilvBNCE) produced up to 738 mM (i.e., 86.5 g/liter) l-valine with an overall yield (Y_P/S) of 0.36 mol per mol of glucose and a volumetric productivity (Q_P) of 13.6 mM per h [1.6 g/(liter × h)]. Additional inactivation of the transaminase B gene (ilvE) and overexpression of ilvBNCD instead of ilvBNCE transformed the l-valine-producing strain into a 2-ketoisovalerate producer, excreting up to 303 mM (35 g/liter) 2-ketoisovalerate with a Y_P/S of 0.24 mol per mol of glucose and a Q_P of 6.9 mM per h [0.8 g/(liter × h)]. The replacement of the aceE promoter by the dapA-A16 promoter in the two C. glutamicum l-lysine producers DM1800 and DM1933 improved the production by 100% and 44%, respectively. These results demonstrate that C. glutamicum strains with reduced PDHC activity are an excellent platform for the production of pyruvate-derived products.     

Engineering of a Glycerol Utilization Pathway for Amino Acid Production by Corynebacterium glutamicum

The amino acid-producing organism Corynebacterium glutamicum cannot utilize glycerol, a stoichiometric by-product of biodiesel production. By heterologous expression of Escherichia coli glycerol utilization genes, C. glutamicum was engineered to grow on glycerol. While expression of the E. coli genes for glycerol kinase (glpK) and glycerol 3-phosphate dehydrogenase (glpD) was sufficient for growth on glycerol as the sole carbon and energy source, additional expression of the aquaglyceroporin gene glpF from E. coli increased growth rate and biomass formation. Glutamate production from glycerol was enabled by plasmid-borne expression of E. coli glpF, glpK, and glpD in C. glutamicum wild type. In addition, a lysine-producing C. glutamicum strain expressing E. coli glpF, glpK, and glpD was able to produce lysine from glycerol as the sole carbon substrate as well as from glycerol-glucose mixtures.     

DAHP Synthetase and Its Control in Corynebacterium glutamicum

Properties of 3-deoxy-D-arabinoheptulosonate-7-phosphate (DAHP) synthetase from Corynebacterium glutamicum were examined using the cell free extract. The optimum pH for the reaction was broad ranging from 5.5 to 7.0 and the optimum temperature was 37°C. Co²⁺ inhibited the enzyme activity at 20°C, whereas Co²⁺ apparently stimulated the enzyme activity at 37°C because the ion protected the enzyme from inactivation at 37°C. Co²⁺ reversed the inhibition of the enzyme activity by EDTA. The activity of DAHP synthetase was feedback inhibited only weakly by l-phenylalanine, l-tyrosine or l-tryptophan alone, but was strongly inhibited synergistically by l-phenylalanine and l-tyrosine. l-Tryptophan enhanced the inhibition by the pair of l-tyrosine and l-phenylalanine. Maximal inhibition was near 90 % in the simultaneous presence of the three amino acids. Sensitivity of the enzyme to the inhibitors was lost during the purification process of the enzyme or during the reaction at 37°C. Especially sensitivity to l-tryptophan was easily lost. Co²⁺ protected the enzyme from the desensitization. Mutants resistant to p-fluorophenylalanine plus l-tyrosine (or 3-aminotyrosine) had DAHP synthetase which was released from the feedback inhibition by the three amino acids. The formation of the enzyme was not affected by aromatic amino acids.     

利用蛋白质序列模式识别改善谷氨酸棒杆菌基因组注释

即使细菌基因组的基因结构较为简单,但在注释过程中也可能出现基因遗漏的现象。当潜在基因在高质量数据库中没有显著同源序列时,基于知识库的基因预测方法就会遇到困难。本文希望通过系统扫描基因组所有可能ORF的蛋白质序列模式来搜索遗漏基因。为验证该方法的可行性,作者系统分析了重要的工业发酵微生物谷氨酸棒杆菌的基因组,发现了25个候选疑似基因。它们具有显著的蛋白质序列模式,但在Swiss-Prot中元显著同源序列,并且在GenBank中仍未注释。深入分析发现,25个候选疑似基因中19个为可能基因,3个为可能假基因,3个为疑似基因序列。这些结果说明本文的分析方法可以有效地用于无显著同源序列基因的搜索。     

l-Valine biosynthesis during batch and fed-batch cultivations of Corynebacterium glutamicum: Relationship between changes in bacterial growth rate and intracellular metabolism

A transition in the bacterial growth rate to below maximum was found to be an optimum parameter of cellular physiology to increase the activity of acetohydroxy acid synthase, a regulatory enzyme in l-valine synthesis, and amino acid overproduction by Corynebacterium glutamicum ATCC 13032 recombinants under batch and fed-batch cultivation conditions. An increase in l-valine synthesis under transient situations when cellular growth rate was downregulated was correlated to a decrease in the activity of aconitase, a key enzyme in the tricarboxylic acid cycle (TCA) of C. glutamicum, and, in contrast, to an increase in the activity of glucose-6-phosphate dehydrogenase, a key enzyme in the pentose phosphate pathway (PPP). The increase in amino acid synthesis was also directly related to a drastic increase in intracellular pyruvate concentration. Thus, an increase in intracellular pyruvate availability and NADPH₂ generation by PPP could be the metabolic origins of the increased l-valine overproduction by growth restrained C. glutamicum cell culture.     

Utilization of soluble starch by a recombinant Corynebacterium glutamicum strain: growth and lysine production

Corynebacterium glutamicum, well known for the industrial production of amino acids, grows aerobically on a variety of mono- and disaccharides and on alcohols and organic acids as single or combined sources of carbon and energy. Members of the genera Corynebacterium and Brevibacterium were here tested for their ability to use the homopolysaccharide starch as a substrate for growth. None of the 24 type strains tested showed growth on or degradation of this substrate, indicating that none of the strains synthesized and secreted starch-degrading enzymes. Introducing the Streptomyces griseus amy gene on an expression vector into the lysine-producer C. glutamicum DM1730, we constructed a C. glutamicum strain synthesizing and secreting alpha-amylase into the culture broth. Although some high-molecular-weight degradation products remained in the culture broth, this recombinant strain effectively used soluble starch as carbon and energy substrate for growth and also for lysine production. Thus, employment of our construct allows avoidance of the cost-intensive enzymatic hydrolysis of the starch, which commercially is used as a substrate in industrial amino acid fermentations.     

Improvement of the redox balance increases L-valine production by Corynebacterium glutamicum under oxygen deprivation conditions

Production of L-valine under oxygen deprivation conditions by Corynebacterium glutamicum lacking the lactate dehydrogenase gene ldhA and overexpressing the L-valine biosynthesis genes ilvBNCDE was repressed. This was attributed to imbalanced cofactor production and consumption in the overall L-valine synthesis pathway: two moles of NADH was generated and two moles of NADPH was consumed per mole of L-valine produced from one mole of glucose. In order to solve this cofactor imbalance, the coenzyme requirement for L-valine synthesis was converted from NADPH to NADH via modification of acetohydroxy acid isomeroreductase encoded by ilvC and introduction of Lysinibacillus sphaericus leucine dehydrogenase in place of endogenous transaminase B, encoded by ilvE. The intracellular NADH/NAD(+) ratio significantly decreased, and glucose consumption and L-valine production drastically improved. Moreover, L-valine yield increased and succinate formation decreased concomitantly with the decreased intracellular redox state. These observations suggest that the intracellular NADH/NAD(+) ratio, i.e., reoxidation of NADH, is the primary rate-limiting factor for L-valine production under oxygen deprivation conditions. The L-valine productivity and yield were even better and by-products derived from pyruvate further decreased as a result of a feedback resistance-inducing mutation in the acetohydroxy acid synthase encoded by ilvBN. The resultant strain produced 1,470 mM L-valine after 24 h with a yield of 0.63 mol mol of glucose(-1), and the L-valine productivity reached 1,940 mM after 48 h.     

Utilization of PEI-modified Corynebacterium glutamicum biomass for the recovery of Pd(II) in hydrochloric solution

A new type of biosorbent was developed for binding anionic precious metals through cross-linking waste biomass Corynebacterium glutamicum with polyethylenimine (PEI). This biomass was evaluated for the removal and recovery of palladium and compared to commercial adsorbents, such as Amberjet 4200 Cl, Lewatit Monoplus TP 214, SPC-100, and SPS-200. The kinetic experiments revealed that the sorption equilibrium was reached with 30 min for the PEI-modified biomass. The maximum uptake of the biosorbent was 176.8 mg/g, which was calculated using the Langmuir model. The Pd(II) maximum uptake exhibited the following order: Amberjet 4200 Cl > Lewatit Monoplus TP 214 > PEI-modified biomass > SPC-100 > SPS-200. Acidified thiourea in 1.0 M HCl was used to desorb Pd(II) from all of the sorbents examined.     

Isolation of restriction deficient mutant for Corynebacterium glutamicum by electroporation

Summary A simple electroporation method for isolating restriction deficient mutants from Corynebacterium glutamicum has been developed. This procedure will also be useful for isolations of restriction deficient mutants of other microorganisms.