Feedback-Resistant Acetohydroxy Acid Synthase Increases Valine Production in Corynebacterium glutamicum

Acetohydroxy acid synthase (AHAS), which catalyzes the key reactions in the biosynthesis pathways of branched-chain amino acids (valine, isoleucine, and leucine), is regulated by the end products of these pathways. The whole Corynebacterium glutamicum ilvBNC operon, coding for acetohydroxy acid synthase (ilvBN) and aceto hydroxy acid isomeroreductase (ilvC), was cloned in the newly constructed Escherichia coli-C. glutamicum shuttle vector pECKA (5.4 kb, Km^r). By using site-directed mutagenesis, one to three amino acid alterations (mutations M8, M11, and M13) were introduced into the small (regulatory) AHAS subunit encoded by ilvN. The activity of AHAS and its inhibition by valine, isoleucine, and leucine were measured in strains carrying the ilvBNC operon with mutations on the plasmid or the ilvNM13 mutation within the chromosome. The enzyme containing the M13 mutation was feedback resistant to all three amino acids. Different combinations of branched-chain amino acids did not inhibit wild-type AHAS to a greater extent than was measured in the presence of 5 mM valine alone (about 57%). We infer from these results that there is a single binding (allosteric) site for all three amino acids in the enzyme molecule. The strains carrying the ilvNM13 mutation in the chromosome produced more valine than their wild-type counterparts. The plasmid-free C. glutamicum ΔilvA ΔpanB ilvNM13 strain formed 90 mM valine within 48 h of cultivation in minimal medium. The same strain harboring the plasmid pECKAilvBNC produced as much as 130 mM valine under the same conditions.     

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.     

Mechanism of l-Threonine and l-Lysine Production by Analog-resistant Mutants of Corynebactemum glutamicum

Homoserine dehydrogenases and aspartokinases in l-threonine- or l-threonine and l-lysine-producing mutants derived from Corynebacterium glutamicum KY 9159 (Met^?) were studied with respect to the sensitivity to the inhibition by end products, l-threonine and l-lysine. The activities of homoserine dehydrogenases in the mutants which produced l-threonine or l-threonine and l-lysine were slightly less susceptible to the inhibition by l-threonine than the activity in the parent strain, KY 9159. The aspartokinases in the threonine-producing mutants, KY 10484 and KY 10230, which were resistant to α-amino-β-hydroxylvaleric acid (AHV, a threonine analog) and more sensitive to thialysine (a lysine analog) than the parent, were sensitive to the concerted feedback inhibition by l-lysine and l-threonine by about the same degree as KY 9159. The aspartokinase in an AHV- and thialysine-resistant mutant, KY 10440, which was derived from KY 10484 and produced about 14 mg/ml of l-threonine in a medium containing 10% glucose was less susceptible to the concerted feedback inhibition than KY 10484 or KY 9159, although the activity was still under the feedback control. In the parent strain, l-threonine activated aspartokinase activity in the absence of ammonium sulfate, an activator of the enzyme, but partially inhibited the activity in the presence of the salt. On the other hand, the enzyme of KY 10440 was activated by l-threonine either in the presence or in the absence of the salt. In another AHV- and thialysine-resistant mutant, KY 10251, which was derived from KY 10230 and produced both 9 mg/ml of l-threonine and 5/5 mg/ml of l-lysine, l-threonine and l-lysine simultaneously added hardly inhibited the activity of aspartokinase.

Implications of these results are discussed in relation to l-threonine or l-lysine production, AHV or thialysine resistance and regulation of l-threonine biosynthesis in these mutants.     

l-Lysine production in continuous culture of an l-lysine hyperproducing mutant of Corynebacterium glutamicum

Summary l-Lysine production was studied in and volumetric productivity were 105 g/l and 5.6 g/l per hour, respectively. The latter corresponded to a 2.5-fold higher value than that of a fed-batch culture. Higher agitation or use of oxygen-enriched air was critical for high productivity. This indicates that oxygen supply greatly affects l-lysine productivity in continuous culture.     

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.     

谷氨酸棒杆菌TL1105的L-组氨酸生物合成途径分析

目的：对谷氨酸棒杆菌TL1105由葡萄糖生物合成L-组氨酸的代谢途径进行分析,以确定L-组氨酸合成的最佳途径和最大理论产率。方法：运用METATOOL软件对谷氨酸棒杆菌TL1105合成L-组氨酸进行途径分析。结果：确定了L-组氨酸合成的最佳途径,并确定最大理论产率为1．2;通过比较途径分析所获得的基础反应模型,确定了5-磷酸核糖焦磷酸是L-组氨酸合成途径的关键节点,并且确定了谷氨酸的大量合成是L-组氨酸合成的重要前提;添加谷氨酸,L-组氨酸的产量提高了39．2％。结论：以途径分析为指导,改变外界环境因子,L-组氨酸的产量得到显著的提高。     

不同来源的谷氨酸棒杆菌氨基脱氧分支酸合成酶的活性分析

分别以高产L-丝氨酸的谷氨酸棒杆菌(Corynebacterium glutamicum)SYPS-062与模式菌株谷氨酸棒杆菌(Corynebacterium glutamicum) ATCC 13032的基因组DNA为模板,运用PCR技术扩增出氨基脱氧分支酸合成酶(ADC synthase)的编码基因pabAB。实验结果表明：来源于SYPS-062和ATCC 13032的pabAB片段全长均为1863bp,编码620个氨基酸。两片段存在16个碱基的差异,引起了7个氨基酸的突变。将pabAB连接表达载体pET-28a(+),构建表达质粒pET-28a-pabAB,并转化E.coli BL21(DE3),在IPTG诱导下,E.coli BL21(DE3)(pET-28a-pabAB)高效表达分子量约为67kDa的可溶性蛋白。表达产物带有His-tag标记,选用Ni柱对表达产物进行纯化,纯化后酶活测定结果表明,来源于SYPS-062氨基脱氧分支酸合成酶的比酶活低于ATCC 13032达46.6%。     

Production of a novel polygalacturonic acid bioflocculant REA-11 by Corynebacterium glutamicum

The production of a novel polygalacturonic acid bioflocculant REA-11 from a newly isolated strain, Corynebacterium glutamicum CCTCC M201005, was investigated. Sucrose was chosen as a carbon source for REA-11 production. Complex nitrogen sources containing urea and an organic nitrogen compound enhanced both bacterial growth and REA-11 production, among which urea plus corn steep liquor was shown to be the most efficient combination. A cost-effective medium for REA-11 production mainly comprised 17 g/l sucrose, 0.45 g/l urea, and 5 ml/l corn steep liquor, under which conditions the flocculating activity reached 390 U/ml. The molar ratio of carbon to nitrogen (C/N) significantly affected REA-11 production, where a C/N ratio of 20:1 was shown to be the best. Interestingly, by simultaneously feeding sucrose and urea at a C/N ratio of 20:1 at 24 h of fermentation, REA-11 production (458 U/ml) was enhanced by 17% compared to the control. In a 10 l jar fermentor, lower dissolved oxygen tension was favorable for REA-11 production: a flocculating activity of 520 U/ml was achieved at a kappaLa of 100 h(-1). REA-11 raw product is relatively thermo-stable at acidic pH ranges of 3.0-6.5. Preliminary application studies showed that REA-11 had stronger flocculating activity to Kaolin clay suspension compared to chemical flocculants. In addition, the capability of decolorizing molasses wastewater indicates the industrial potential of this novel bioflocculant.     

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.     

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-Tyrosine Production by Analog-resistant Mutants Derived from a Phenylalanine Auxotroph of Corynebacterium glutamicum

Mutants resistant to various phenylalanine- or tyrosine-analogs were isolated from a phenylalanine auxotroph of Corynebacterium glutamicum KY 10233 by treatment with N- methyl-N′-nitro-N-nitrose guanidine (NTG) and screened for L-tyrosine production. A mutant, 98–Tx–71, which is resistant to 3-aminotyrosine, p-aminophenylalanine, p-fluoro-phenylalanine, and tyrosine hydroxamate was found to produce L-tyrosine at a concentration of 13.5 mg/ml in the cane molasses medium containing 10% of sugar calculated as glucose. A tyrosine-sensitive mutant, pr–20 which was derived from 98–Tx–71 produced L-tyrosine at a concentration of 17.6 mg/ml. L-Tyrosine formation in the strain pr–20 was found to be still inhibited by L-phenylalanine though it was not inhibited by L-tyrosine. The L-tyrosine formation in the mutant was repressed neither by L-phenylalanine nor by L-tyrosine.     

Production of l-valine from metabolically engineered Corynebacterium glutamicum

Applied Microbiology and Biotechnology - l-Valine is one of the three branched-chain amino acids (valine, leucine, and isoleucine) essential for animal health and important in metabolism;...     

A New Pathway for Poly(3-hydroxybutyrate) Production in Escherichia coli and Corynebacterium glutamicum by Functional Expression of a New Acetoacetyl-coenzyme A Synthase

A biosynthetic pathway for poly(3-hydroxybutyrate) [P(3HB)] was developed in Escherichia coli and Corynebacterium glutamicum by an acetoacetyl-coenzyme A (CoA) synthase (AACS) recently isolated from terpenoid-producing Streptomyces sp. strain CL190. Expression of AACS led to significant productions of P(3HB) in E. coli (10.5 wt %) and C. glutamicum (19.7 wt %).     

Production of minicellulosomes for the enhanced hydrolysis of cellulosic substrates by recombinant Corynebacterium glutamicum

Although cellulosic materials of plant origin are the most abundant utilizable biomass resource, the amino acid-producing organism Corynebacterium glutamicum can not utilize these materials. Here we report the engineering of a C. glutamicum strain expressing functional minicellulosomes containing chimeric endoglucanase E bound to miniCbpA from Clostridium cellulovorans that can hydrolyze cellulosic materials. The chimeric endoglucanase E consists of the endoglucanase E catalytic backbone of Clostridium thermocellum fused with the endoglucanase B dockerin domain of C. cellulovorans. The resulting strain degraded cellulose efficiently by substrate targeting via the carbohydrate binding module. The assembly of minicellulosomes increased the activity against carboxymethyl cellulose approximately 2.8-fold compared with that for the corresponding enzymes alone. This is the first report of the formation of Clostridium minicellulosomes by C. glutamicum. The development of C. glutamicum strain that is capable of more effective cellulose hydrolysis brings about a realization of consolidated bioprocessing for the utilization of cellulosic biomass.     

Fermentative Production of l-Proline with Auxotrophs of Corynebacterium glutamicum

Two auxotrophic mutants of Corynebacterium glutamicum were found to produce a large amount of l-proline in the culture medium. High concentration of MgSO₄ or MnSO₄ in the medium stimulated the l-proline production by an isoleucine auxotroph. Optimum concentration of l-isoleucine was 200 μg/ml, and the higher concentration of l-isoleucine reduced the l-proline production. The auxotroph produced 14.8 mg/ml of l-proline when cultured in a medium containing 12% glucose, 1.7% NH₄C1,0.6% MgSO₄·7H₂O, 0.06% MnSO₄·4H₂O and 200 μg/ml of l-isoleucine. The other mutant, whose growth responds to the bases of nucleic acids, produced 7 to 13 mg/ml of l-proline in a cane molasses (15%, as glucose concentration)-medium containing 2% of the acid-hydrolyzate of soybean meal. The l-proline production by this mutant increased to a level of 27 to 31 mg/ml when the growth was suppressed by the addition of 4% NH₄C1 to the medium, or by the addition of 2 mg/ml of polyoxyethylenestearylamine, a surfactant, to a culture at an appropriate stage of the fermentation.