Increasing l‐isoleucine production in Corynebacterium glutamicum by overexpressing global regulator Lrp and two‐component export system BrnFE

Aims

To increase the l ‐isoleucine production in Corynebacterium glutamicum by overexpressing the global regulator Lrp and the two‐component export system BrnFE.

Methods and Results

The brnFE operon and the lrp gene were cloned into the shuttle vector pDXW‐8 individually or in combination. The constructed plasmids were transformed into an l ‐isoleucine‐producing strain C. glutamicum JHI3‐156, and the l ‐isoleucine production in these different strains was analysed and compared. More l ‐isoleucine was produced when only Lrp was expressed than when only BrnFE was expressed. Significant increase in l ‐isoleucine production was observed when Lrp and BrnFE were expressed in combination. Compared to the control strain, l ‐isoleucine production in JHI3‐156/pDXW‐8‐lrp‐brnFE increased 63% in flask cultivation, and the specific yield of l ‐isoleucine increased 72% in fed‐batch fermentation.

Conclusions

Both Lrp and BrnFE are important to enhance the l ‐isoleucine production in C. glutamicum.

Significance and Impact of the Study

The results provide useful information to enhance l ‐isoleucine or other branched‐chain amino acid production in C. glutamicum.     

Engineering of Phosphoserine Aminotransferase Increases the Conversion of l‐Homoserine to 4‐Hydroxy‐2‐ketobutyrate in a Glycerol‐Independent Pathway of 1,3‐Propanediol Production from Glucose

Phosphoserine aminotransferase (SerC) from Escherichia coli (E. coli) MG1655 is engineered to catalyze the deamination of homoserine to 4‐hydroxy‐2‐ketobutyrate, a key reaction in producing 1,3‐propanediol (1,3‐PDO) from glucose in a novel glycerol‐independent metabolic pathway. To this end, a computation‐based rational approach is used to change the substrate specificity of SerC from l ‐phosphoserine to l ‐homoserine. In this approach, molecular dynamics simulations and virtual screening are combined to predict mutation sites. The enzyme activity of the best mutant, SerC_R42W/R77W, is successfully improved by 4.2‐fold in comparison to the wild type when l ‐homoserine is used as the substrate, while its activity toward the natural substrate l ‐phosphoserine is completely deactivated. To validate the effects of the mutant on 1,3‐PDO production, the “homoserine to 1,3‐PDO” pathway is constructed in E. coli by coexpression of SerC_R42W/R77W with pyruvate decarboxylase and alcohol dehydrogenase. The resulting mutant strain achieves the production of 3.03 g L^?1 1,3‐PDO in fed‐batch fermentation, which is 13‐fold higher than the wild‐type strain and represents an important step forward to realize the promise of the glycerol‐independent synthetic pathway for 1,3‐PDO production from glucose.     

Membrane Inlet Mass Spectrometry for the on‐line Measurement of Metabolic Fluxes: Case Lysine‐Production by Corynebacterium glutamicum

A miniaturized reactor system with on‐line measurement of respiration rates by membrane inlet mass spectrometry was applied for the on‐line metabolic flux analysis at different phases of a 1.2 L batch culture of lysine‐producing Corynebacterium glutamicum. For this purpose, cells taken from the batch culture were transferred into the 12 mL mini reactor, and incubated for 15 min with [1‐¹⁸O]glucose. Quantification of oxygen uptake rate and CO₂ mass isotopomer production rates in combination with a simple metabolic model allowed the estimation of the flux partitioning ratio between the pentose phosphate pathway and glycolysis during the process. The relative flux into the pentose pathway increased during growth, and reached maxima at 11 and 17 h cultivation time coinciding with maxima of the differential lysine yield. The developed system is a promising tool for determination of metabolic flux dynamics in industrially relevant batch and fed‐batch cultures.     

CRISPR interference–mediated metabolic engineering of Corynebacterium glutamicum for homo‐butyrate production

Combinatorial metabolic engineering enabled the development of efficient microbial cell factories for modulating gene expression to produce desired products. Here, we report the combinatorial metabolic engineering of Corynebacterium glutamicum to produce butyrate by introducing a synthetic butyrate pathway including phosphotransferase and butyrate kinase reactions and repressing the essential acn gene‐encoding aconitase, which has been targeted for downregulation in a genome‐scale model. An all‐in‐one clustered regularly interspaced short palindromic repeats interference system for C. glutamicum was used for tunable downregulation of acn in an engineered strain, where by‐product‐forming reactions were deleted and the synthetic butyrate pathway was inserted, resulting in butyrate production (0.52 ± 0.02 g/L). Subsequently, biotin limitation enabled the engineered strain to produce butyrate (0.58 ± 0.01 g/L) without acetate formation for the entire duration of the culture. These results demonstrate the potential homo‐production of butyrate using engineered C. glutamicum. This method can also be applied to other industrial microorganisms.     

Production of <Emphasis Type="Italic">Chryseobacterium proteolyticum</Emphasis> protein-glutaminase using the twin-arginine translocation pathway in <Emphasis Type="Italic">Corynebacterium glutamicum</Emphasis>

The protein glutaminase (PG) secreted by the Gram-negative bacterium Chryseobacterium proteolyticum can deamidate glutaminyl residues in several substrate proteins, including insoluble wheat glutens. This enzyme therefore has potential application in the food industry. We assessed the possibility to produce PG containing a pro-domain in Corynebacterium glutamicum which we have successfully used for production of several kinds of proteins at industrial-scale. When it was targeted to the general protein secretion pathway (Sec) via its own signal sequence, the protein glutaminase was not secreted in this strain. In contrast, we showed that pro-PG could be efficiently produced using the recently discovered twin-arginine translocation (Tat) pathway when the typical Sec-dependent signal peptide was replaced by a Tat-dependent signal sequence from various bacteria. The accumulation of pro-PG in C. glutamicum ATCC13869 reached 183 mg/l, and the pro-PG was converted to an active form as the native one by SAM-P45, a subtilisin-like serine protease derived from Streptomyces albogriseolus. The successful secretion of PG via this approach confirms that the Tat pathway of C. glutamicum is an efficient alternative for the industrial-scale production of proteins that are not efficiently secreted by other systems.     

Enhancement of 5-aminolevulinic acid production by metabolic engineering of the glycine biosynthesis pathway in <Emphasis Type="Italic">Corynebacterium glutamicum</Emphasis>

Objective

To construct a strain of Corynebacterium glutamicum capable of efficiently producing 5-aminolevulinic acid (5-ALA) via the C4 pathway by modification of serine and glycine pathway using glucose as sole carbon source.

Results

The recombinant C. glutamicum strain AP2 harboring a codon-optimized hemA gene from Rhodobacter sphaeroides was used as host strain for 5-ALA production. A plasmid harboring the serine operon, which contained serB, serC and the site-specific mutant serA ^Δ197 , was constructed and introduced into C. glutamicumAP2, leading to an increase of 70% in 5-ALA production. Further overexpression of the glyA gene increased production of 5-ALA by 150% over the control. 5-ALA production was thus significantly enhanced by engineering the glycine biosynthetic pathway. C.glutamicum AG3 produced 3.4 ± 0.2 g 5-ALA/l in shake-flask cultures in CGIIIM medium with the addition of 7.5 g glycine/l.

Conclusion

This is the first report of remodeling the serine and glycine biosynthetic pathway to improve the production of 5-ALA in C. glutamicum.

     

Crystallographic and mutational analyses of cystathionine β‐synthase in the H2S‐synthetic gene cluster in Lactobacillus plantarum

Cystathionine β‐synthase (CBS) catalyzes the formation of l ‐cystathionine from l ‐serine and l ‐homocysteine. The resulting l ‐cystathionine is decomposed into l ‐cysteine, ammonia, and α‐ketobutylic acid by cystathionine γ‐lyase (CGL). This reverse transsulfuration pathway, which is catalyzed by both enzymes, mainly occurs in eukaryotic cells. The eukaryotic CBS and CGL have recently been recognized as major physiological enzymes for the generation of hydrogen sulfide (H₂S). In some bacteria, including the plant‐derived lactic acid bacterium Lactobacillus plantarum, the CBS‐ and CGL‐encoding genes form a cluster in their genomes. Inactivation of these enzymes has been reported to suppress H₂S production in bacteria; interestingly, it has been shown that H₂S suppression increases their susceptibility to various antibiotics. In the present study, we characterized the enzymatic properties of the L. plantarum CBS, whose amino acid sequence displays a similarity with those of O‐acetyl‐l ‐serine sulfhydrylase (OASS) that catalyzes the generation of l ‐cysteine from O‐acetyl‐l ‐serine (l ‐OAS) and H₂S. The L. plantarum CBS shows l ‐OAS‐ and l ‐cysteine‐dependent CBS activities together with OASS activity. Especially, it catalyzes the formation of H₂S in the presence of l ‐cysteine and l ‐homocysteine, together with the formation of l ‐cystathionine. The high affinity toward l ‐cysteine as a first substrate and tendency to use l ‐homocysteine as a second substrate might be associated with its enzymatic ability to generate H₂S. Crystallographic and mutational analyses of CBS indicate that the Ala70 and Glu223 residues at the substrate binding pocket are important for the H₂S‐generating activity.     

Metabolic engineering and flux analysis of <Emphasis Type="Italic">Corynebacterium glutamicum</Emphasis> for L-serine production

l-Serine plays a critical role as a building block for cell growth, and thus it is difficult to achieve the direct fermentation of l-serine from glucose. In this study, Corynebacterium glutamicum ATCC 13032 was engineered de novo by blocking and attenuating the conversion of l-serine to pyruvate and glycine, releasing the feedback inhibition by l-serine to 3-phosphoglycerate dehydrogenase (PGDH), in combination with the co-expression of 3-phosphoglycerate kinase (PGK) and feedback-resistant PGDH (PGDH^r). The resulting strain, SER-8, exhibited a lower specific growth rate and significant differences in l-serine levels from Phase I to Phase V as determined for fed-batch fermentation. The intracellular l-serine pool reached (14.22±1.41) μmol g_CDM ⁻¹, which was higher than glycine pool, contrary to fermentation with the wild-type strain. Furthermore, metabolic flux analysis demonstrated that the over-expression of PGK directed the flux of the pentose phosphate pathway (PPP) towards the glycolysis pathway (EMP), and the expression of PGDH^r improved the l-serine biosynthesis pathway. In addition, the flux from l-serine to glycine dropped by 24%, indicating that the deletion of the activator GlyR resulted in down-regulation of serine hydroxymethyltransferase (SHMT) expression. Taken together, our findings imply that l-serine pool management is fundamental for sustaining the viability of C. glutamicum, and improvement of C₁ units generation by introducing the glycine cleavage system (GCV) to degrade the excessive glycine is a promising target for l-serine production in C. glutamicum.     

CARBON SOURCE DEPENDENCE OF THE RATIO OF δ‐AMINOLEVULINIC ACID BIOSYNTHESIS VIA THE C5 AND SHEMIN PATHWAYS IN EUGLENA GRACILIS (EUGLENOPHYCEAE)1

The ratio of two biosynthetic pathways was estimated, the C5 and Shemin pathways, to δ‐aminolevulinic acid (ALA, a biosynthetic intermediate of tetrapyrrole) from the ¹³C‐enrichment ratios (¹³C‐ER) at the carbon atoms of chl a (after conversion to methyl pheophorbide a) biosynthesized by Euglena gracilis G. A. Klebs when l ‐[3‐¹³C]alanine was used as a carbon source. On the basis of these estimations, we confirmed that ALA was efficiently biosynthesized via both the C5 and Shemin pathways in the plastids of E. gracilis, and we determined that the ratio of ALA biosynthesis via the Shemin pathway was increased in the ratio of 14%–67%, compared with that in our previous d ‐[1‐¹³C]glucose feeding experiment ( Iida et al. 2002 ). This carbon source dependence of the contributions of the two biosynthetic pathways might be related to activation of gluconeogenesis by the amino acid substrate. The methoxy carbon of the methoxycarbonyl group at C‐13² of chl a was labeled with the ¹³C‐carbon of l ‐[methyl‐¹³C]methionine derived from l ‐[3‐¹³C]alanine via [2‐¹³C]acetyl coenzyme A (CoA), through the atypical tricarboxylic acid (TCA) cycle, gluconeogenesis, and l‐ [3‐¹³C]serine. The phytyl moiety of chl a was also labeled on C‐P2, C‐P3¹, C‐P4, C‐P6, C‐P7¹, C‐P8, C‐P10, C‐P11¹, C‐P12, C‐P14, C‐P15¹, and C‐P16 from ¹³C‐isoprene (2‐[1,2‐methyl,3‐¹³C₃]methyl‐1,3‐butadiene) generated from l ‐[3‐¹³C]alanine via [2‐¹³C]acetyl CoA.     

Improvement of <Emphasis Type="Italic">Escherichia coli</Emphasis> production strains by modification of the phosphoenolpyruvate:sugar phosphotransferase system

The application of metabolic engineering in Escherichia coli has resulted in the generation of strains with the capacity to produce metabolites of commercial interest. Biotechnological processes with these engineered strains frequently employ culture media containing glucose as the carbon and energy source. In E. coli, the phosphoenolpyruvate:sugar phosphotransferase system (PTS) transports glucose when this sugar is present at concentrations like those used in production fermentations. This protein system is involved in phosphoenolpyruvate-dependent sugar transport, therefore, its activity has an important impact on carbon flux distribution in the phosphoenolpyruvate and pyruvate nodes. Furthermore, PTS has a very important role in carbon catabolite repression. The properties of PTS impose metabolic and regulatory constraints that can hinder strain productivity. For this reason, PTS has been a target for modification with the purpose of strain improvement. In this review, PTS characteristics most relevant to strain performance and the different strategies of PTS modification for strain improvement are discussed. Functional replacement of PTS by alternative phosphoenolpyruvate-independent uptake and phosphorylation activities has resulted in significant improvements in product yield from glucose and productivity for several classes of metabolites. In addition, inactivation of PTS components has been applied successfully as a strategy to abolish carbon catabolite repression, resulting in E. coli strains that use more efficiently sugar mixtures, such as those obtained from lignocellulosic hydrolysates.     

Modular pathway engineering of key carbon‐precursor supply‐pathways for improved N‐acetylneuraminic acid production in Bacillus subtilis

N‐acetylneuraminic acid (NeuAc) is widely used as a nutraceutical for facilitating infant brain development, maintaining brain health, and enhancing immunity. Currently, NeuAc is mainly produced by extraction from egg yolk and milk, or via chemical synthesis. However, its low concentration in natural resources and its non‐ecofriendly chemical synthesis result in insufficient NeuAc production and environmental pollution, respectively. In this study, improved NeuAc production was attained via modular pathway engineering of the supply pathways of two key precursors—N‐acetylglucosamine (GlcNAc) and phosphoenolpyruvate (PEP)—and by balancing NeuAc biosynthesis and cell growth in engineered Bacillus subtilis. Specifically, we used a previously constructed GlcNAc‐producing B. subtilis as the initial host for NeuAc biosynthesis. First, we constructed a de novo NeuAc biosynthetic pathway utilizing glucose by coexpressing glucosamine‐6‐phosphate acetyl‐transferase (GNA1), N‐acetylglucosamine 2‐epimerase (AGE), and N‐acetylneuraminic acid synthase (NeuB), resulting in 0.33 g/l NeuAc production. Next, to balance the supply of the two key precursors for NeuAc biosynthesis, modular pathway engineering was performed. The optimal strategy for balancing the GlcNAc module and PEP supply module involved the use of an engineered, unique glucose and malate coutilization pathway in B. subtilis, supplied with both glucose (for the GlcNAc moiety) and malate (for the PEP moiety) at high strength. This led to 1.65 g/L NeuAc production, representing a 5.0‐fold improvement over the existing methods. Furthermore, to enhance the NeuAc yield on cell, glucose and malate coutilization pathways were engineered to balance NeuAc biosynthesis and cell growth via the blocking of glycolysis, the introduction of the Entner–Doudoroff pathway, and the overexpression of the malic enzyme YtsJ. NeuAc titer reached 2.18 g/L, with 0.38 g/g dry cell weight NeuAc yield on cell, which represented a 1.32‐fold and 2.64‐fold improvement over the existing methods, respectively. The strategy of modular pathway engineering of key carbon precursor supply pathways via engineering of the unique glucose‐malate coutilization pathway in B. subtilis should be generically applicable for engineering of B. subtilis for the production of other important biomolecules. Our study also provides a good starting point for further metabolic engineering to achieve industrial production of NeuAc by a Generally Regarded As Safe bacterial strain.     

Enhanced succinic acid production in <Emphasis Type="Italic">Corynebacterium glutamicum</Emphasis> with increasing the available NADH supply and glucose consumption rate by decreasing H<Superscript>+</Superscript>-ATPase activity

Objectives

To enhance succinic acid production in Corynebacterium glutamicum by increasing the supply of NADH and the rate of glucose consumption by decreasing H⁺-ATPase activity.

Results

A mutant of C. glutamicum NC-3-1 with decreased H⁺-ATPase activity was constructed. This increased the rate of glycolysis and the supply of NADH. Fermentation of C. glutamicum NC-3-1 gave 39 % higher succinic acid production (113 and 81 g/l), a 29 % higher succinic acid yield (0.94 and 0.73 g succinic acid/g glucose) and decreased by-products formation compared to that of C. glutamicum NC-3 in 5 l bioreactor.

Conclusion

The point mutation in C. glutamicum NC-3-1 increased the rate of glycolysis and resulted in higher succinic acid production, higher succinic acid yield and significantly decreased formation of by-products.

     

Effect of pyruvate dehydrogenase complex deficiency on <Emphasis Type="SmallCaps">l</Emphasis>-lysine production with <Emphasis Type="Italic">Corynebacterium glutamicum</Emphasis>

Intracellular precursor supply is a critical factor for amino acid productivity of Corynebacterium glutamicum. To test for the effect of improved pyruvate availability on l-lysine production, we deleted the aceE gene encoding the E1p enzyme of the pyruvate dehydrogenase complex (PDHC) in the l-lysine-producer C. glutamicum DM1729 and characterised the resulting strain DM1729-BB1 for growth and l-lysine production. Compared to the host strain, C. glutamicum DM1729-BB1 showed no PDHC activity, was acetate auxotrophic and, after complete consumption of the available carbon sources glucose and acetate, showed a more than 50% lower substrate-specific biomass yield (0.14 vs 0.33 mol C/mol C), an about fourfold higher biomass-specific l-lysine yield (5.27 vs 1.23 mmol/g cell dry weight) and a more than 40% higher substrate-specific l-lysine yield (0.13 vs 0.09 mol C/mol C). Overexpression of the pyruvate carboxylase or diaminopimelate dehydrogenase genes in C. glutamicum DM1729-BB1 resulted in a further increase in the biomass-specific l-lysine yield by 6 and 56%, respectively. In addition to l-lysine, significant amounts of pyruvate, l-alanine and l-valine were produced by C. glutamicum DM1729-BB1 and its derivatives, suggesting a surplus of precursor availability and a further potential to improve l-lysine production by engineering the l-lysine biosynthetic pathway. This study is dedicated to Prof. Dr. Hermann Sahm on the occasion of his 65th birthday.     

Reconstruction of tricarboxylic acid cycle in Corynebacterium glutamicum with a genome-scale metabolic network model for trans-4-hydroxyproline production

trans-4-Hydroxy- l -proline (Hyp) is an abundant component of mammalian collagen and functions as a chiral synthon for the syntheses of anti-inflammatory drugs in the pharmaceutical industry. Proline 4-hydroxylase (P4H) can catalyze the conversion of l -proline to Hyp; however, it is still challenging for the fermentative production of Hyp from glucose using P4H due to the low yield and productivity. Here, we report the metabolic engineering of Corynebacterium glutamicum for the fermentative production of Hyp by reconstructing tricarboxylic acid (TCA) cycle together with heterologously expressing the p4h gene from Dactylosporangium sp. strain RH1. In silico model-based simulation showed that α-ketoglutarate was redirected from the TCA cycle toward Hyp synthetic pathway driven by P4H when the carbon flux from succinyl-CoA to succinate descended to zero. The interruption of the TCA cycle by the deletion of sucCD-encoding the succinyl-CoA synthetase (SUCOAS) led to a 60% increase in Hyp production and had no obvious impact on the growth rate. Fine-tuning of plasmid-borne ProB* and P4H abundances led to a significant increase in the yield of Hyp on glucose. The final engineered Hyp-7 strain produced up to 21.72 g/L Hyp with a yield of 0.27 mol/mol (Hyp/glucose) and a volumetric productivity of 0.36 g·L ⁻¹·hr ⁻¹ in the shake flask fermentation. To our knowledge, this is the highest yield and productivity achieved by microbial fermentation in a glucose-minimal medium for Hyp production. This strategy provides new insights into engineering C. glutamicum by flux coupling for the fermentative production of Hyp and related products.     

Comparative assessment of the Euglena gracilis var. saccharophila variant strain as a producer of the β‐1,3‐glucan paramylon under varying light conditions

Euglena gracilis Z and a “sugar loving” variant strain E. gracilis var. saccharophila were investigated as producers of paramylon, a β‐1,3‐glucan polysaccharide with potential medicinal and industrial applications. The strains were grown under diurnal or dark growth conditions on a glucose–yeast extract medium supporting high‐level paramylon production. Both strains produced the highest paramylon yields (7.4–8 g · L^?1, respectively) while grown in the dark, but the maximum yield was achieved faster by E. gracilis var. saccharophila (48 h vs. 72 h). The glucose‐to‐paramylon yield coefficient Y_par/glu = 0.46 ± 0.03 in the E. gracilis var. saccharophila cultivation, obtained in this study, is the highest reported to date. Proteomic analysis of the metabolic pathways provided molecular clues for the strain behavior observed during cultivation. For example, overexpression of enzymes in the gluconeogenesis/glycolysis pathways including fructokinase‐1 and chloroplastic fructose‐1,6‐bisphosphatase (FBP ) may have contributed to the faster rate of paramylon accumulation in E. gracilis var. saccharophila . Differentially expressed proteins in the early steps of chloroplastogenesis pathway including plastid uroporphyrinogen decarboxylases, photoreceptors, and a highly abundant (68‐fold increase) plastid transketolase may have provided the E. gracilis var. saccharophila strain an advantage in paramylon production during diurnal cultivations. In conclusion, the variant strain E. gracilis var. saccharophila seems to be well suited for producing large amounts of paramylon. This work has also resulted in the identification of molecular targets for future improvement of paramylon production in E. gracilis , including the FBP and phosophofructokinase 1, the latter being a key regulator of glycolysis.     

β‐poly(l‐malic acid) production by fed‐batch culture of Aureobasidium pullulans ipe‐1 with mixed sugars

β‐poly(l ‐malic acid) (PMLA) is a biopolyester, which has attracted growing attention due to its potential applications in medicine and other industries. In this study, the biosynthetic pathway of PMLA and the fermentation strategies with mixed sugars were both investigated to enhance PMLA production by Aureobasidium pullulans ipe‐1. Metabolic intermediates and inhibitors were used to study the biosynthetic pathway of PMLA. It showed that exogenous addition of l ‐malic acid, succinic acid, TFA, and avidin had negligible effect on PMLA production, while pyruvic acid and biotin were the inhibitors, indicating that PMLA biosynthesis was probably related to phosphoenolpyruvate via oxaloacetate catalyzed by phosphoenolpyruvate carboxylase. Sucrose was suitable for achieving the highest PMLA concentration, while fructose generated a higher yield of PMLA (PMLA produced per biomass). Furthermore, the fed‐batch culture using fed solution with different sugar mixture for PMLA production was implemented. During the fed‐batch culture with mixed solution, fructose could increase PMLA production. Compared with the batch culture, the feeding with mixed sugar (sucrose and glucose) increased PMLA concentration by 23.9%, up to 63.2 g/L, and the final volume of the broth was increased by 25%. These results provide a good reference for process development and optimization of PMLA production.