Metabolic reprogramming and biosensor-assisted mutagenesis screening for high-level production of L-arginine in Escherichia coli.

L-arginine is a value-added amino acid with promising applications in the pharmaceutical and nutraceutical industries. Further unleashing the potential of microbial cell factories to make L-arginine production more competitive remains challenging due to the sophisticated intracellular interaction networks and the insufficient knowledge of global metabolic regulation. Here, we combined multilevel rational metabolic engineering with biosensor-assisted mutagenesis screening to exploit the L-arginine production potential of Escherichia coli. First, multiple metabolic pathways were systematically reprogrammed to redirect the metabolic flux into L-arginine synthesis, including the L-arginine biosynthesis, TCA cycle, and L-arginine export. Specifically, a toggle switch responding to special cellular physiological conditions was designed to dynamically control the expression of sucA and pull more carbon flux from the TCA cycle toward L-arginine biosynthesis. Subsequently, a biosensor-assisted high-throughput screening platform was designed and applied to further exploit the L-arginine production potential. The best-engineered ARG28 strain produced 132 g/L L-arginine in a 5-L bioreactor with a yield of 0.51 g/g glucose and productivity of 2.75 g/(L ⋅ h), which were the highest values reported so far. Through whole genome sequencing and reverse engineering, Frc frameshift mutant, PqiB A78P mutant, and RpoB P564T mutant were revealed for enhancing the L-arginine biosynthesis. Our study exhibited the power of coupling rational metabolic reprogramming and biosensor-assisted mutagenesis screening to unleash the cellular potential for value-added metabolite production.

The implication of viability and pathogenicity by truncated lipopolysaccharide in Yersinia enterocolitica.

The fast envelope stress responses play a key role in the transmission and pathogenesis of Yersinia enterocolitica, one of the most common foodborne pathogens. Our previous study showed that deletion of the waaF gene, essential for the biosynthesis of lipopolysaccharide (LPS) core polysaccharides, led to the formation of a truncated LPS structure and induced cell envelope stress. This envelope stress may disturb the intracellular signal transduction, thereby affecting the physiological functions of Y. enterocolitica. In this study, truncated LPS caused by waaF deletion was used as a model of envelope stress in Y. enterocolitica. We investigated the mechanisms of envelope stress responses and the cellular functions affected by truncated LPS. Transcriptome analysis and phenotypic validation showed that LPS truncation reduced flagellar assembly, bacterial chemotaxis, and inositol phosphate metabolism, presenting lower pathogenicity and viability both in vivo and in vitro environments. Further 4D label-free phosphorylation analysis confirmed that truncated LPS perturbed multiple intracellular signal transduction pathways. Specifically, a comprehensive discussion was conducted on the mechanisms by which chemotactic signal transduction and Rcs system contribute to the inhibition of chemotaxis. Finally, the pathogenicity of Y. enterocolitica with truncated LPS was evaluated in vitro using IPEC-J2 cells as models, and it was found that truncated LPS exhibited reduced adhesion, invasion, and toxicity of Y. enterocolitica to IPEC-J2 cells. Our research provides an understanding of LPS in the regulation of Y. enterocolitica viability and pathogenicity and, thus, opening new avenues to develop novel food safety strategies or drugs to prevent and control Y. enterocolitica infections. KEY POINTS: • Truncated LPS reduces flagellar assembly, chemotaxis, and inositol phosphate metabolism in Y. enterocolitica. • Truncated LPS reduces adhesion, invasion, and toxicity of Y. enterocolitica to IPEC-J2 cells. • Truncated LPS regulates intracellular signal transduction of Y. enterocolitica.

Metabolic engineering of Escherichia coli for efficient osmotic stress-free production of compatible solute hydroxyectoine.

Compatible solutes are key for the ability of halophilic bacteria to resist high osmotic stress. They have received wide attention from researchers for their excellent osmotic protection properties. Hydroxyectoine is a particularly important compatible solute, but its production by microbes faces several challenges, including low titer/yield, the presence of the byproduct ectoine, and the requirement of high salinity. Here, we aimed to metabolically engineer Escherichia coli to efficiently produce hydroxyectoine in the absence of osmotic stress without accumulating the byproduct ectoine. First, combinatorial optimization of the expression strength of key genes in the ectoine synthesis module and hydroxyectoine synthesis module was conducted. After optimization of the expression of these genes, 12.12 g/L hydroxyectoine and 0.24 g/L ectoine were obtained at 36 h in shake-flask fermentation with the addition of the co-substrate α-ketoglutarate. Further optimization of the addition of α-ketoglutarate achieved the sole production of hydroxyectoine (i.e., no ectoine accumulation), indicating that the supply of α-ketoglutarate is critically important for sole hydroxyectoine production. Finally, quorum sensing-based auto-regulation of intracellular α-ketoglutarate pool was implemented as an alternative to α-ketoglutarate addition by coupling the expression of sucA with the esaI/esaR circuit, which led to 14.93 g/L hydroxyectoine with a unit cell yield of 1.678 g/g and no ectoine accumulation in the absence of osmotic stress. This is the highest reported titer of sole hydroxyectoine production under salinity-free fermentation to date.

Reconstructing a recycling and nonauxotroph biosynthetic pathway in Escherichia coli toward highly efficient production of L-citrulline.

L-citrulline is a high-value amino acid with promising application in medicinal and food industries. Construction of highly efficient microbial cell factories for L-citrulline production is still an open issue due to complex metabolic flux distribution and L-arginine auxotrophy. In this study, we constructed a nonauxotrophic cell factory in Escherichia coli for high-titer L-citrulline production by coupling modular engineering strategies with dynamic pathway regulation. First, the biosynthetic pathway of L-citrulline was enhanced after blockage of the degradation pathway and introduction of heterologous biosynthetic genes from Corynebacterium glutamicum. Specifically, a superior recycling biosynthetic pathway was designed to replace the native linear pathway by deleting native acetylornithine deacetylase. Next, the carbamoyl phosphate and L-glutamate biosynthetic modules, the NADPH generation module, and the efflux module were modified to increase L-citrulline titer further. Finally, a toggle switch that responded to cell density was designed to dynamically control the expression of the argG gene and reconstruct a nonauxotrophic pathway. Without extra supplement of L-arginine during fermentation, the final CIT24 strain produced 82.1 g/L L-citrulline in a 5-L bioreactor with a yield of 0.34 g/g glucose and a productivity of 1.71 g/(L ⋅ h), which were the highest values reported by microbial fermentation. Our study not only demonstrated the successful design of cell factory for high-level L-citrulline production but also provided references of coupling the rational module engineering strategies and dynamic regulation strategies to produce high-value intermediate metabolites.

Flux redistribution of central carbon metabolism for efficient production of l-tryptophan in Escherichia coli.

Microbial production of l-tryptophan (l-trp) has received considerable attention because of its diverse applications in food additives and pharmaceuticals. Overexpression of rate-limiting enzymes and blockage of competing pathways can effectively promote microbial production of l-trp. However, the biosynthetic process remains suboptimal due to imbalanced flux distribution between central carbon and tryptophan metabolism, presenting a major challenge to further improvement of l-trp yield. In this study, we redistributed central carbon metabolism to improve phosphoenolpyruvate (PEP) and erythrose-4-phosphate (E4P) pools in an l-trp producing strain of Escherichia coli for efficient l-trp synthesis. To do this, a phosphoketolase from Bifidobacterium adolescentis was introduced to strengthen E4P formation, and the l-trp titer and yield increased to 10.8 g/L and 0.148 g/g glucose, respectively. Next, the phosphotransferase system was substituted with PEP-independent glucose transport, meditated by a glucose facilitator from Zymomonas mobilis and native glucokinase. This modification improved l-trp yield to 0.164 g/g glucose, concomitant with 58% and 40% decreases of acetate and lactate accumulation, respectively. Then, to channel more central carbon flux to the tryptophan biosynthetic pathway, several metabolic engineering strategies were applied to rewire the PEP-pyruvate-oxaloacetate node. Finally, the constructed strain SX11 produced 41.7 g/L l-trp with an overall yield of 0.227 g/g glucose after 40 h fed-batch fermentation in 5-L bioreactor. This is the highest overall yield of l-trp ever reported from a rationally engineered strain. Our results suggest the flux redistribution of central carbon metabolism to maintain sufficient supply of PEP and E4P is a promising strategy for efficient l-trp biosynthesis, and this strategy would likely also increase the production of other aromatic amino acids and derivatives.

High-yield production of L-valine in engineered Escherichia coli by a novel two-stage fermentation.

L-valine is an essential amino acid and an important amino acid in the food and feed industry. The relatively low titer and low fermentation yield currently limit the large-scale application of L-valine. Here, we constructed a chromosomally engineered Escherichia coli to efficiently produce L-valine. First, the synthetic pathway of L-valine was enhanced by heterologous introduction of a feedback-resistant acetolactate acid synthase from Bacillus subtilis and overexpression of other two enzymes in the L-valine synthetic pathway. For efficient efflux of L-valine, an exporter from Corynebacterium glutamicum was subsequently introduced. Next, the precursor pyruvate pool was increased by knockout of GTP pyrophosphokinase and introduction of a ppGpp 3'-pyrophosphohydrolase mutant to facilitate the glucose uptake process. Finally, in order to improve the redox cofactor balance, acetohydroxy acid isomeroreductase was replaced by a NADH-preferring mutant, and branched-chain amino acid aminotransferase was replaced by leucine dehydrogenase from Bacillus subtilis. Redox cofactor balance enabled the strain to synthesize L-valine under oxygen-limiting condition, significantly increasing the yield in the presence of glucose. Two-stage fed-batch fermentation of the final strain in a 5 L bioreactor produced 84 g/L L-valine with a yield and productivity of 0.41 g/g glucose and 2.33 g/L/h, respectively. To the best of our knowledge, this is the highest L-valine titer and yield ever reported in E. coli. The systems metabolic engineering strategy described here will be useful for future engineering of E. coli strains for the industrial production of L-valine and related products.

Efficient fermentative production of L-theanine by Corynebacterium glutamicum.

L-Theanine is a unique non-protein amino acid found in tea plants that has been shown to possess numerous functional properties relevant to food science and human nutrition. L-Theanine has been commercially developed as a valuable additive for use in food and beverages, and its market is expected to expand substantially if the production cost can be lowered. Although the enzymatic approach holds considerable potential for use in L-theanine production, demand exists for developing more tractable methods (than those currently available) that can be implemented under mild conditions and will reduce operational procedures and cost. Here, we sought to engineer fermentative production of L-theanine in Corynebacterium glutamicum, an industrially safe host. For L-theanine synthesis, we used γ-glutamylmethylamide synthetase (GMAS), which catalyzes the ATP-dependent ligation of L-glutamate and ethylamine. First, distinct GMASs were expressed in C. glutamicum wild-type ATCC 13032 strain and GDK-9, an L-glutamate overproducing strain, to produce L-theanine upon ethylamine addition to the hosts. Second, the L-glutamate exporter in host cells was disrupted, which markedly increased the L-theanine titer in GDK-9 cells and almost eliminated the accumulation of L-glutamate in the culture medium. Third, a chromosomally gmasMm-integrated L-alanine producer was constructed and used, attempting to synthesize ethylamine endogenously by expressing plant-derived L-serine/L-alanine decarboxylases; however, these enzymes showed no L-alanine decarboxylase activity under our experimental conditions. The optimal engineered strain that we ultimately created produced ~ 42 g/L L-theanine, with a yield of 19.6%, in a 5-L fermentor. This is the first report of fermentative production of L-theanine achieved using ethylamine supplementation.

Comparative metabolomic analysis reveals different evolutionary mechanisms for branched-chain amino acids production.

Evolution is a powerful tool for the breeding of microorganisms, while the connection between the changes of intracellular metabolism and different evolution directions is still unclear, which once clarified, will greatly expand the application of evolutionary engineering. We aim to clarify the correlation between metabolism changes and evolution directions in two Corynebacterium glutamicum strains for L-valine and L-leucine overproducing originated from the same parental strain by repeated random mutagenesis and selection. GC-MS metabolomics was performed to identify and quantify intracellular metabolites of the evolved and wild-type C. glutamicum strains. Time-series comparison of the fermentation processes was performed. The metabolism differences of three strains mainly exist in central carbon metabolism and the stress-resisting modes. C. glutamicum XV developed an overall "pyruvate-saving" mode for L-valine synthesis, and adopted a trehalose accumulating strategy to resist environmental stresses. C. glutamicum CP depended on an enhanced "pyruvate-producing" mode, together with certain "pyruvate-saving" strategies, for efficient L-leucine synthesis, and accumulated proline, my-inositol, and inositol as the stress-resisting measure. These elaborate regulation strategies could be used in future metabolic engineering, making evolution more informative and applicable.

Two-stage carbon distribution and cofactor generation for improving l-threonine production of Escherichia coli.

L-Threonine, a kind of essential amino acid, has numerous applications in food, pharmaceutical, and aquaculture industries. Fermentative l-threonine production from glucose has been achieved in Escherichia coli. However, there are still several limiting factors hindering further improvement of l-threonine productivity, such as the conflict between cell growth and production, byproduct accumulation, and insufficient availability of cofactors (adenosine triphosphate, NADH, and NADPH). Here, a metabolic modification strategy of two-stage carbon distribution and cofactor generation was proposed to address the above challenges in E. coli THRD, an l-threonine producing strain. The glycolytic fluxes towards tricarboxylic acid cycle were increased in growth stage through heterologous expression of pyruvate carboxylase, phosphoenolpyruvate carboxykinase, and citrate synthase, leading to improved glucose utilization and growth performance. In the production stage, the carbon flux was redirected into l-threonine synthetic pathway via a synthetic genetic circuit. Meanwhile, to sustain the transaminase reaction for l-threonine production, we developed an l-glutamate and NADPH generation system through overexpression of glutamate dehydrogenase, formate dehydrogenase, and pyridine nucleotide transhydrogenase. This strategy not only exhibited 2.02- and 1.21-fold increase in l-threonine production in shake flask and bioreactor fermentation, respectively, but had potential to be applied in the production of many other desired oxaloacetate derivatives, especially those involving cofactor reactions.

Multiple-step chromosomal integration of divided segments from a large DNA fragment via CRISPR/Cas9 in Escherichia coli.

Although CRISPR/Cas9-mediated gene editing technology has developed vastly in Escherichia coli, the chromosomal integration of large DNA fragment is still challenging compared with gene deletion and small fragment integration. Moreover, to guarantee sufficient Cas9-induced double-strand breaks, it is usually necessary to design several gRNAs to select the appropriate one. Accordingly, we established a practical daily routine in the laboratory work, involving multiple-step chromosomal integration of the divided segments from a large DNA fragment. First, we introduced and optimized the protospacers from Streptococcus pyogenes in E. coli W3110. Next, the appropriate fragment size for each round of integration was optimized to be within 3-4 kb. Taking advantage of the optimized protospacer/gRNA pairs, a DNA fragment with a total size of 15.4 kb, containing several key genes for uridine biosynthesis, was integrated into W3110 chromosome, which produced 5.6 g/L uridine in shake flask fermentation. Using this strategy, DNA fragments of virtually any length can be integrated into a suitable genomic site, and two gRNAs can be alternatively used, avoiding the tedious construction of gRNA-expressing plasmids. This study thus presents a useful strategy for large DNA fragment integration into the E. coli chromosome, which can be easily adapted for use in other bacteria.

Metabolic engineering of Escherichia coli for high-yield uridine production.

Uridine is a kind of pyrimidine nucleoside that has been widely applied in the pharmaceutical industry. Although microbial fermentation is a promising method for industrial production of uridine, an efficient microbial cell factory is still lacking. In this study, we constructed a metabolically engineered Escherichia coli capable of high-yield uridine production. First, we developed a CRISPR/Cas9-mediated chromosomal integration strategy to integrate large DNA into the E. coli chromosome, and a 9.7 kb DNA fragment including eight genes in the pyrimidine operon of Bacillus subtilis F126 was integrated into the yghX locus of E. coli W3110. The resultant strain produced 3.3 g/L uridine and 4.5 g/L uracil in shake flask culture for 32 h. Subsequently, five genes involved in uridine catabolism were knocked out, and the uridine titer increased to 7.8 g/L. As carbamyl phosphate, aspartate, and 5'-phosphoribosyl pyrophosphate are important precursors for uridine synthesis, we further modified several metabolism-related genes and synergistically improved the supply of these precursors, leading to a 76.9% increase in uridine production. Finally, nupC and nupG encoding nucleoside transport proteins were deleted, and the extracellular uridine accumulation increased to 14.5 g/L. After 64 h of fed-batch fermentation, the final engineered strain UR6 produced 70.3 g/L uridine with a yield and productivity of 0.259 g/g glucose and 1.1 g/L/h, respectively. To the best of our knowledge, this is the highest uridine titer and productivity ever reported for the fermentative production of uridine.

High production of 4-hydroxyisoleucine in Corynebacterium glutamicum by multistep metabolic engineering.

4-Hydroxyisoleucine (4-HIL) exhibits a unique glucose-dependent insulinotropic activity and is a promising candidate for the treatment of diabetes. Direct fermentation of 4-HIL has been recently studied; however, the expected titre and yield were not achieved. In this study, we initially developed a pathway for the synthesis of 4-HIL in an L-isoleucine producer, C. glutamicum YI, but insufficient supply of α-ketoglutarate was a bottleneck for a strong production. Six genes involved in oxaloacetate and α-ketoglutarate branches were overexpressed or deleted, which increased the production of 4-HIL to 5.12 g/L but a considerable amount of L-isoleucine still accumulated in the culture. We then dynamically modulated the activity of the α-ketoglutarate dehydrogenase complex (ODHC) by employing L-isoleucine-responsive transcription or attenuation strategies. The best-engineered strain, HIL18, produced 34.21 g/L 4-HIL with a negligible accumulation of byproducts, including approximately 0.6 g/L L-isoleucine. This study achieved the highest production and yield of 4-HIL, and optimizing the TCA cycle by dynamically modulating the activity of ODHA can be a powerful strategy to balance the carbon flux and achieve efficient production of α-ketoglutarate and derivatives.

Identification and application of a growth-regulated promoter for improving L-valine production in Corynebacterium glutamicum.

BACKGROUND: Promoters are commonly used to regulate the expression of specific target genes or operons. Although a series of promoters have been developed in Corynebacterium glutamicum, more precise and unique expression patterns are needed that the current selection of promoters cannot produce. RNA-Seq technology is a powerful tool for helping us to screen out promoters with expected transcriptional strengths. RESULTS: The promoter PCP_2836 of an aldehyde dehydrogenase coding gene from Corynebacterium glutamicum CP was identified via RNA-seq and RT-PCR as a growth-regulated promoter. Comparing with the strong constitutive promoter Ptuf, the transcriptional strength of PCP_2836 showed a significant decrease that from about 75 to 8% in the stationary phase. By replacing the native promoters of the aceE and gltA genes with PCP_2836 in the C. glutamicum ATCC 13032-derived L-valine-producing strain AN02, the relative transcriptional levels of the aceE and gltA genes decreased from 1.2 and 1.1 to 0.35 and 0.3, and the activity of their translation products decreased to 43% and 35%, respectively. After 28 h flask fermentation, the final cell density of the obtained strains, GRaceE and GRgltA, exhibited a 7-10% decrease. However, L-valine production increased by 23.9% and 27.3%, and the yield of substrate to product increased 43.8% and 62.5%, respectively. In addition, in the stationary phase, the intracellular citrate levels in GRaceE and GRgltA decreased to 27.0% and 33.6% of AN02, and their intracellular oxaloacetate levels increased to 2.7 and 3.0 times that of AN02, respectively. CONCLUSIONS: The PCP_2836 promoter displayed a significant difference on its transcriptional strength in different cell growth phases. With using PCP_2836 to replace the native promoters of aceE and gltA genes, both the transcriptional levels of the aceE and gltA genes and the activity of their translation products demonstrated a significant decrease in the stationary phase. Thus, the availability of pyruvate was significantly increased for the synthesis of L-valine without any apparent irreversible negative impacts on cell growth. Use of this promoter can enhance the selectivity and control of gene expression and could serve as a useful research tool for metabolic engineering.

Metabolic engineering of Bacillus subtilis for the co-production of uridine and acetoin.

In this study, a uridine and acetoin co-production pathway was designed and engineered in Bacillus subtilis for the first time. A positive correlation between acetoin and uridine production was observed and investigated. By disrupting acetoin reductase/2,3-butanediol dehydrogenasegenebdhA, the acetoin and uridine yield was increased while 2,3-butanediol formation was markedly reduced. Subsequent overexpression of the alsSD operon further improved acetoin yield and abolished acetate formation. After optimization of fermentation medium, key supplementation strategies of yeast extract and soybean meal hydrolysate were identified and applied to improve the co-production of uridine and acetoin. With a consumption of 290.33 g/L glycerol, the recombinant strain can accumulate 40.62 g/L uridine and 60.48 g/L acetoin during 48 h of fed-batch fermentation. The results indicate that simultaneous production of uridine and acetoin is an efficient strategy for balancing the carbon metabolism in engineered Bacillus subtilis. More importantly, co-production of value-added products is a possible way to improve the economics of uridine fermentation.

Pathway construction and metabolic engineering for fermentative production of ectoine in Escherichia coli.

Ectoine is a protective agent and stabilizer whose synthesis pathway exclusively exists in select moderate halophiles. A novel established process called "bacterial milking" efficiently synthesized ectoine in moderate halophiles, however, this method places high demands on equipment and is cost prohibitive. In this study, we constructed an ectoine producing strain by introducing the ectoine synthesis pathway into Escherichia coli and improved its production capacity. Firstly, the ectABC gene cluster from Halomonas elongata was introduced into E. coli W3110 and the resultant strain synthesized 4.9g/L ectoine without high osmolarity. Subsequently, thrA encoding the bifunctional aspartokinase/homoserine dehydrogenase was deleted to weaken the competitive l-threonine branch, resulting in an increase of ectoine titer by 109%. Furthermore, a feedback resistant lysC from Corynebacterium glutamicum encoding the aspartate kinase was introduced to complement the enzymatic activity deficiency caused by thrA deletion and a 9% increase of ectoine titer was obtained. Finally, the promoter of ppc that encodes phosphoenolpyruvate carboxylase was replaced by a trc promoter, and iclR, a glyoxylate shunt transcriptional repressor gene, was deleted. The oxaloacetate pool, was thus reinforced and ectoine titer increased by 21%. The final engineered strain ECT05 (pTrcECT, pSTVLysC-CG) produced 25.1g/L ectoine by fed-batch fermentation in low salt concentration with glucose as a carbon source. The specific ectoine production and productivity was 0.8g/g DCW and 0.84gL(-)(1)h(-)(1) respectively. The overall ectoine yield was 0.11g/g of glucose.

Production of α-ketobutyrate using engineered Escherichia coli via temperature shift.

Alpha-ketobutyrate has been widely used in medicine and food additive industry. Because chemical and enzymatic methods are associated with many deficiencies, the recent focus shifted to fermentation for the production of α-ketobutyrate. In this study, a genetically engineered strain THRDΔrhtAΔilvIH/pWSK29-ilvA was constructed, starting from an L-threonine-producing strain, by overexpressing threonine dehydratase (TD), reducing α-ketobutyrate catabolism and L-threonine export. The shake flask cultivation of THRDΔrhtAΔilvIH/pWSK29-ilvA allowed the production of 16.2 g/L α-ketobutyrate. Accumulation of α-ketobutyrate severely inhibited the cell growth. To develop a better TD expression system and avoid the usage of the expensive inducer IPTG, a temperature-induced plasmid pBV220-ilvA was selected to transform the strain THRDΔrhtAΔilvIH for α-ketobutyrate production. The initial temperature was maintained at 35°C to guarantee normal cell growth, and then elevated to 40°C to induce the expression of TD. Under optimized conditions, the α-ketobutyrate titer reached 40.8 g/L after 28 h of fermentation, with a productivity of 1.46 g/L/h and a yield of 0.19 g/g glucose, suggesting large-scale production potential. Biotechnol. Bioeng. 2016;113: 2054-2059. © 2016 Wiley Periodicals, Inc.

Efficient production of α-ketoglutarate in the gdh deleted Corynebacterium glutamicum by novel double-phase pH and biotin control strategy.

Production of L-glutamate using a biotin-deficient strain of Corynebacterium glutamicum has a long history. The process is achieved by controlling biotin at suboptimal dose in the initial fermentation medium, meanwhile feeding NH4OH to adjust pH so that α-ketoglutarate (α-KG) can be converted to L-glutamate. In this study, we deleted glutamate dehydrogenase (gdh1 and gdh2) of C. glutamicum GKG-047, an L-glutamate overproducing strain, to produce α-KG that is the direct precursor of L-glutamate. Based on the method of L-glutamate fermentation, we developed a novel double-phase pH and biotin control strategy for α-KG production. Specifically, NH4OH was added to adjust the pH at the bacterial growth stage and NaOH was used when the cells began to produce acid; besides adding an appropriate amount of biotin in the initial medium, certain amount of additional biotin was supplemented at the middle stage of fermentation to maintain a high cell viability and promote the carbon fixation to the flux of α-KG production. Under this control strategy, 45.6 g/L α-KG accumulated after 30-h fermentation in a 7.5-L fermentor and the productivity and yield achieved were 1.52 g/L/h and 0.42 g/g, respectively.

[Effect of key-gene modification on uridine biosynthesis in Bacillus subtilis].

OBJECTIVE: We studied several crucial factors influencing the uridine biosynthesis in Bacillus subtilis, including mutations of phosphoribosylpyrophosphate synthetase (PRPP synthetase) (prs) and carbamyl phosphate synthetase (pyrAA/pyrAB), and overexpression of heterologous 5'-nucleotidase (sdt1). METHODS: According to the inferred allosteric sites, we introduced point mutation into coding sequences of prs and pyrAB. The mutated prs gene was integratedly expressed in the xylR locus of the chromosome and the pyrAB gene was modified in-situ. The sdt1 gene was overexpressed in the saB locus of the chromosome. The effect of the genetic modification on uridine biosynthesis was characterized by the analysis of uridine, cytidine and uracil in the fermentation broth. RESULTS: The mutations of Asn120Ser, Leu135Ile, Glu52Gly or Val312Ala on PRPP synthase resulted in an increase of uridine production by 67% and 96%, respectively. The mutations of Ser948Phe, Thr977Ala and Lys993Ile on carbamyl phosphate synthase resulted in a 182% increase of uridine yield to 6.97 g/L. The overexpression of heterologous 5'-nucleotidase resulted in a 17% increase of uridine yield to 8.16 g/L. CONCLUSION: The activity and regulation mechanism of PRPP synthase and carbamyl phosphate synthase was an important factor to limit the excessive synthesis of uridine. Asn120Ser and Leu135Ile mutations of PRPP synthase and Ser948Phe, Thr977Ala and Lys993Ile mutations of carbamyl phosphate synthase will facilitate the biosynthesis of uridine. The additional Glu52Gly and Val312Ala mutations of PRPP synthase were beneficial for uridine biosynthesis. The reaction from UMP to uridine also limited the biosynthesis of uridine in B. subtilis.

Strategy for enhancing adenosine production under the guidance of transcriptional and metabolite pool analysis.

OBJECTIVES: To rationally identify targets for enhancing adenosine production, transcription level of genes involved in adenosine synthesis of Bacillus subtilis XGL was detected during the fermentation process, complemented with metabolite pool analysis. RESULTS: PurR-regulated genes (pur operon and purA) and prs were down-regulated and 5-phosphoribosyl 1-pyrophosphate (PRPP) decreased considerably after 24 h when adenosine significantly accumulated. Since PRPP could strongly antagonize the binding of PurR to its targets, it was inferred that down-regulation of pur operon and purA might be due to a low PRPP pool, which was confirmed by metabolite analysis. So desensitized prs responsible for PRPP synthesis was overexpressed, resulting in increased PRPP concentration and pur operon transcription. To further enhance the adenosine production, desensitized purF and prs were co-overexpressed with integrating additional copy of purA to B. subtilis XGL genome, resulting in 24.3 % (1.29 g/g DCW) higher adenosine production than that by B. subtilis XG. CONCLUSIONS: Overexpression of prs, purF and purA under the guidance of transcriptional and metabolite pool analysis significantly increased adenosine production. Strategies used in this study have potential applications for rational modification of industrial microorganisms.

Optimization of carbon source and glucose feeding strategy for improvement of L-isoleucine production by Escherichia coli.

Fed-batch cultivations of L-isoleucine-producing Escherichia coli TRFP (SGr, α-ABAr, with a pTHR101 plasmid containing a thr operon and ilvA) were carried out on different carbon sources: glucose, sucrose, fructose, maltose and glycerol. The results indicated that sucrose was the best initial carbon source for L-isoleucine production and then sucrose concentration of 30 g·L-1 was determined in the production medium. The results of different carbon sources feeding showed that the glucose solution was the most suitable feeding media. The dissolved oxygen (DO) of L-isoleucine fermentation was maintained at 5%, 15% and 30% with DO-stat feeding, respectively. The results indicated that when the DO level was maintained at 30%, the highest biomass and L-isoleucine production were obtained. The accumulation of acetate was decreased and the production of L-isoleucine was increased markedly, when the glucose concentration was maintained at 0.15 g·L-1 by using glucose-stat feeding. Finally, the glucose concentration was maintained at 0.10 g·L-1 and the DO level was controlled at approximately 30% during the whole fermentation period, using the combined feeding strategy of glucose-stat feeding and DO feedback feeding. The acetate accumulation was decreased to 7.23 g·L-1, and biomass and production of L-isoleucine were increased to 46.8 and 11.95 g·L-1, respectively.