Engineering cofactor flexibility enhanced 2,3-butanediol production in <Emphasis Type="Italic">Escherichia coli</Emphasis>

Enzymatic reduction of acetoin into 2,3-butanediol (2,3-BD) typically requires the reduced nicotinamide adenine dinucleotide (NADH) or its phosphate form (NADPH) as electron donor. Efficiency of 2,3-BD biosynthesis, therefore, is heavily influenced by the enzyme specificity and the cofactor availability which varies dynamically. This work describes the engineering of cofactor flexibility for 2,3-BD production by simultaneous overexpression of an NADH-dependent 2,3-BD dehydrogenase from Klebsiella pneumoniae (KpBudC) and an NADPH-specific 2,3-BD dehydrogenase from Clostridium beijerinckii (CbAdh). Co-expression of KpBudC and CbAdh not only enabled condition versatility for 2,3-BD synthesis via flexible utilization of cofactors, but also improved production stereo-specificity of 2,3-BD without accumulation of acetoin. With optimization of medium and fermentation condition, the co-expression strain produced 92 g/L of 2,3-BD in 56 h with 90% stereo-purity for (R,R)-isoform and 85% of maximum theoretical yield. Incorporating cofactor flexibility into the design principle should benefit production of bio-based chemical involving redox reactions.     

A shortened,two-enzyme pathway for 2,3-butanediol production in <Emphasis Type="Italic">Escherichia coli</Emphasis>

The platform chemical 2,3-butanediol (2,3-BDO) is produced by a number of microorganisms via a three-enzyme pathway starting from pyruvate. Here, we report production of 2,3-BDO via a shortened, two-enzyme pathway in Escherichia coli. A synthetic operon consisting of the acetolactate synthase (ALS) and acetoin reductase (AR) genes from Enterobacter under control of the T7 promoter was cloned in an episomal plasmid. E. coli transformed with this plasmid produced 2,3-BDO and the pathway intermediate acetoin, demonstrating that the shortened pathway was functional. To assemble a synthetic operon for inducer- and plasmid-free production of 2,3-BDO, ALS and AR genes were integrated in the E. coli genome under control of the constitutive ackA promoter. Shake flask-level cultivation led to accumulation of ~1 g/L acetoin and ~0.66 g/L 2,3-BDO in the medium. The novel biosynthetic route for 2,3-BDO biosynthesis described herein provides a simple and cost-effective approach for production of this important chemical.     

Production of Vanillin by Metabolically Engineered <Emphasis Type="Italic">Escherichia coli</Emphasis>

E. coli was metabolically engineered to produce vanillin by expression of the fcs and ech genes from Amycolatopsis sp. encoding feruloyl-CoA synthetase and enoyl-CoA hydratase/aldolase, respectively. Vanillin production was optimized by leaky expression of the genes, under the IPTG-inducible trc promoter, in complex 2YT medium. Supplementation with glucose, fructose, galactose, arabinose or glycerol severely decreased vanillin production. The highest vanillin production of 1.1 g l⁻¹ was obtained with cultivation for 48 h in 2YT medium with 0.2% (w/v) ferulate, without IPTG and no supplementation of carbon sources.     

Regulation of <Emphasis Type="Italic">lac</Emphasis> Transcription in Antibiotic-treated <Emphasis Type="Italic">E. coli</Emphasis>

Chloramphenicol stabilizes pre-existing lac mRNA, but inhibits further accumulation by allowing rapid degradation of nascent message. Puromycin accelerates decay of pre-existing and new lac message by discharging protective ribo-somes. Both effects are partially reversed by the suA mutation.     

Enhanced 2,3-butanediol production by <Emphasis Type="Italic">Klebsiella pneumoniae</Emphasis> SDM

Enhanced 2,3-butanediol (BD) production was carried out by Klebsiella pneumoniae SDM. The nutritional requirements for BD production by K. pneumoniae SDM were optimized statistically in shake flask fermentations. Corn steep liquor powder and (NH₄)₂HPO₄ were identified as the most significant factors by the two-level Plackett–Burman design. Steepest ascent experiments were applied to approach the optimal region of the two factors and a central composite design was employed to determine their optimal levels. The optimal medium was used to perform fed-batch fermentations with K. pneumoniae SDM. BD production was then studied in a 5-l bioreactor applying different fed-batch strategies, including pulse fed batch, constant feed rate fed batch, constant residual glucose concentration fed batch, and exponential fed batch. The maximum BD concentration of 150 g/l at 38 h with a diol productivity of 4.21 g/l h was obtained by the constant residual glucose concentration feeding strategy. To the best of our knowledge, these results were new records on BD fermentation. Cuiqing Ma and Ailong Wang contributed equally to this work.     

Chemically defined medium and <Emphasis Type="Italic">Caenorhabditis elegans</Emphasis>

Background  

C. elegans has been established as a powerful genetic system. Use of a chemically defined medium (C. elegans Maintenance Medium (CeMM)) now allows standardization and systematic manipulation of the nutrients that animals receive. Liquid cultivation allows automated culturing and experimentation and should be of use in large-scale growth and screening of animals.     

Engineering <Emphasis Type="Italic">Escherichia coli</Emphasis> for efficient cellobiose utilization

Escherichia coli normally cannot utilize the β-glucoside sugar cellobiose as a carbon and energy source unless a stringent selection pressure for survival is present. The cellobiose-utilization phenotype can be conferred by mutations in the two cryptic operons, chb and asc. In this study, the cellobiose-utilization phenotype was conferred to E. coli by replacing the cryptic promoters of these endogenous operons with a constitutive promoter. Evolutionary adaptation of the engineered strain CP12CHBASC by repeated subculture in cellobiose-containing minimal medium led to an increase in the rate of cellobiose uptake and cell growth on cellobiose. An efficient cellobiose-metabolizing E. coli strain would be of great importance over glucose-metabolizing E. coli for a simultaneous saccharification and fermentation process, as the cost of the process would be reduced by eliminating one of the three enzymes needed to hydrolyze cellulose into simple sugars.     

Inheritance of the <Emphasis Type="Italic">ps</Emphasis> mutation in sugar beet

Genetic analysis of the inheritance of mutation ps in sugar beet was conducted. This mutation causes the meiotic abnormalities leading to the development of diploid pollen grains and influences several other morphological traits, namely, annual or biennial habit, stem color, and aggregation of pollen grains into tetrads, which are controlled by the genes B, Stc, and ap, respectively. The literature data on the linkage of genes B and Stc were confirmed; the obtained recombination coefficient between these genes amounts to 15.0 ± 3.6%. It was demonstrated that gene ap was inherited independently of genes B and Stc. Statistical analysis of the data shows that the mutation ps is recessive and is inherited independently of the mutation ap but in a linked manner with the traits development habit and stem color. The conclusion is made that a gene with a strong phenotypic effect that determines the development of the phenotype characteristic of mutation ps is located in the first linkage group near genes B and Stc.     

Regulation of the <Emphasis Type="Italic">htpX</Emphasis> Gene of <Emphasis Type="Italic">Xylella fastidiosa</Emphasis> and Its Expression in <Emphasis Type="Italic">E. coli</Emphasis>

Xylella fastidiosa was the first phytopathogen to be completely sequenced, and its genome revealed several interesting features to be used in functional studies. In the present work, the htpX gene, which encodes a protein involved in the heat shock response in other bacteria, was analyzed by RT-PCR by using cells derived from different cultural conditions. This gene was induced after a temperature upshift to 37°C after growth in minimal medium, XDM, but showed constitutive expression in rich medium or in XDM plus plant extracts. Sequences upstream to the htpX gene, containing a putative regulatory region, were also transferred to E. coli, and the thermoregulation was maintained in the new host, since it was constitutively transcribed at 37°C or 45°C in all culture media tested, but not at 28°C in minimal culture medium. The gene was also cloned into the expression vector pET32Xa/LIC, and the expression of the corresponding protein was confirmed by Western blotting.     

Expression of <Emphasis Type="Italic">recA</Emphasis> gene of <Emphasis Type="Italic">Deinococcus radiodurans</Emphasis> in <Emphasis Type="Italic">Escherichia coli</Emphasis> cells

Plasmids pKS5 and pKSrec30 carrying normal and mutant alleles of the Deinococcus recA gene controlled by the lactose promoter slightly increase radioresistance of Escherichia coli cells with mutations in genes recA and ssb. The RecA protein of D. radiodurans is expressed in E. coli cells, and its synthesis can be supplementary induced. The radioprotective effect of the xenologic protein does not exceed 1.5 fold and yields essentially to the contribution of plasmid pUC19-recA1.1 harboring the E. coli recA ⁺ gene in the recovery of resistance of the ΔrecA deletion mutant. These data suggest that the expression of D. radiodurans recA gene in E. coli cells does not complement mutations at gene recA in the chromosome possibly due to structural and functional peculiarities of the D. radiodurans RecA protein.     

Enhanced production of 2,3-butanediol by engineered <Emphasis Type="Italic">Bacillus subtilis</Emphasis>

Production of 2,3-butanediol by Bacillus subtilis takes place in late-log or stationary phase, depending on the expression of bdhA gene encoding acetoin reductase, which converts acetoin to 2,3-butanediol. The present work focuses on the development of a strain of B. subtilis for enhanced production of 2,3-butanediol in early log phase of growth cycle. For this, the bdhA gene was expressed under the control of P _alsSD promoter of AlsSD operon for acetoin fermentation which served the substrate for 2,3-butanediol production. Addition of acetic acid in the medium induced the production of 2,3-butanediol by 2-fold. Two-step aerobic–anaerobic fermentation further enhanced 2,3-butanediol production by 4-fold in comparison to the control parental strain. Thus, addition of acetic acid and low dissolved oxygen in the medium are involved in activation of bdhA gene expression from P _alsSD promoter in early log phase. Under the conditions tested in this work, the maximum production of 2,3-butanediol, 2.1 g/l from 10 g/l glucose, was obtained at 24 h. Furthermore, under the optimized microaerophilic condition, the production of 2,3-butanediol improved up to 6.1 g/l and overall productivity increased by 6.7-fold to 0.4 g/l h in the engineered strain compared to that in the parental control.     

Production of <Emphasis Type="SmallCaps">d</Emphasis>-lactic acid from sugarcane molasses,sugarcane juice and sugar beet juice by <Emphasis Type="Italic">Lactobacillus delbrueckii</Emphasis>

Lactobacillus delbrueckii was grown on sugarcane molasses, sugarcane juice and sugar beet juice in batch fermentation at pH 6 and at 40°C. After 72 h, the lactic acid from 13% (w/v) sugarcane molasses (119 g total sugar l⁻¹) and sugarcane juice (133 g total sugar l⁻¹) was 107 g l⁻¹ and 120 g l⁻¹, respectively. With 10% (w/v) sugar beet juice (105 g total sugar l⁻¹), 84 g lactic acid l⁻¹ was produced. The optical purities of d-lactic acid from the feedstocks ranged from 97.2 to 98.3%.     

Cloning of <Emphasis Type="Italic">srfA</Emphasis> operon from <Emphasis Type="Italic">Bacillus subtilis</Emphasis> C9 and its expression in <Emphasis Type="Italic">E. coli</Emphasis>

The srfA operon is required for the nonribosomal biosynthesis of the cyclic lipopeptide, surfactin. The srfA operon is composed of the four genes, srfAA, srfAB, srfAC, and srfAD, encoding the surfactin synthetase subunits, plus the sfp gene that encodes phosphopantetheinyl transferase. In the present study, 32 kb of the srfA operon was amplified from Bacillus subtilis C9 using a long and accurate PCR (LA-PCR), and ligated into a pIndigoBAC536 vector. The ligated plasmid was then transformed into Escherichia coli DH10B. The transformant ET2 showed positive signals to all the probes for each open reading frame (ORF) region of the srfA operon in southern hybridization, and a reduced surface tension in a culture broth. Even though the surface-active compound extracted from the E. coli transformant exhibited a different R _f value of 0.52 from B. subtilis C9 or authentic surfactin (R _f = 0.63) in a thin layer chromatography (TLC) analysis, the transformant exhibited a much higher surface-tension-reducing activity than the wild-type strain E. coli DH10B. Thus, it would appear that an intermediate metabolite of surfactin was expressed in the E. coli transformant harboring the srfA operon.     

Production of optically pure 2,3-butanediol from <Emphasis Type="Italic">Miscanthus floridulus</Emphasis> hydrolysate using engineered <Emphasis Type="Italic">Bacillus licheniformis</Emphasis> strains

2,3-Butanediol (2,3-BD) can be produced by fermentation of natural resources like Miscanthus. Bacillus licheniformis mutants, WX-02ΔbudC and WX-02ΔgldA, were elucidated for the potential to use Miscanthus as a cost-effective biomass to produce optically pure 2,3-BD. Both WX-02ΔbudC and WX-02ΔgldA could efficiently use xylose as well as mixed sugars of glucose and xylose to produce optically pure 2,3-BD. Batch fermentation of M. floridulus hydrolysate could produce 21.6 g/L d-2,3-BD and 23.9 g/L meso-2,3-BD in flask, and 13.8 g/L d-2,3-BD and 13.2 g/L meso-2,3-BD in bioreactor for WX-02ΔbudC and WX-02ΔgldA, respectively. Further fed-batch fermentation of hydrolysate in bioreactor showed both of two strains could produce optically pure 2,3-BD, with 32.2 g/L d-2,3-BD for WX-02ΔbudC and 48.5 g/L meso-2,3-BD for WX-02ΔgldA, respectively. Collectively, WX-02ΔbudC and WX-02ΔgldA can efficiently produce optically pure 2,3-BD with M. floridulus hydrolysate, and these two strains are candidates for industrial production of optical purity of 2,3-BD with M. floridulus hydrolysate.     

Minimizing acetate formation in <Emphasis Type="Italic">E. coli</Emphasis> fermentations

Escherichia coli remains the best-established production organism in industrial biotechnology. However, when aerobic fermentation runs at high growth rates, considerable amounts of acetate are accumulated as by-product. This by-product has negative effects on growth and protein production. Over the last 20 years, substantial research efforts have been expended on reducing acetate accumulation during aerobic growth of E. coli on glucose. From the onset it was clear that this quest would not be a simple or uncomplicated one. Simple deletion of the acetate pathway reduced the acetate accumulation, but other by-products were formed. This mini review gives a clear outline of these research efforts and their outcome, including bioprocess level approaches and genetic approaches. Recently, the latter seems to have some promising results.     

Genome-wide analysis of <Emphasis Type="Italic">E. coli</Emphasis> cell-gene interactions

Background

The pursuit of standardization and reliability in synthetic biology has achieved, in recent years, a number of advances in the design of more predictable genetic parts for biological circuits. However, even with the development of high-throughput screening methods and whole-cell models, it is still not possible to predict reliably how a synthetic genetic construct interacts with all cellular endogenous systems. This study presents a genome-wide analysis of how the expression of synthetic genes is affected by systematic perturbations of cellular functions. We found that most perturbations modulate expression indirectly through an effect on cell size, putting forward the existence of a generic Size-Expression interaction in the model prokaryote Escherichia coli.

Results

The Size-Expression interaction was quantified by inserting a dual fluorescent reporter gene construct into each of the 3822 single-gene deletion strains comprised in the KEIO collection. Cellular size was measured for single cells via flow cytometry. Regression analyses were used to discriminate between expression-specific and gene-specific effects. Functions of the deleted genes broadly mapped onto three systems with distinct primary influence on the Size-Expression map. Perturbations in the Division and Biosynthesis (DB) system led to a large-cell and high-expression phenotype. In contrast, disruptions of the Membrane and Motility (MM) system caused small-cell and low-expression phenotypes. The Energy, Protein synthesis and Ribosome (EPR) system was predominantly associated with smaller cells and positive feedback on ribosome function.

Conclusions

Feedback between cell growth and gene expression is widespread across cell systems. Even though most gene disruptions proximally affect one component of the Size-Expression interaction, the effect therefore ultimately propagates to both. More specifically, we describe the dual impact of growth on cell size and gene expression through cell division and ribosomal content. Finally, we elucidate aspects of the tight control between swarming, gene expression and cell growth. This work provides foundations for a systematic understanding of feedbacks between genetic and physiological systems.

     

Function of the <Emphasis Type="Italic">rel</Emphasis> Gene in <Emphasis Type="Italic">Escherichia coli</Emphasis>

Sokawa et al. suggest that rel^- strains of Escherichia coli possess abnormal protein synthesizing machinery, which cannot carry out normal protein synthesis when the supply of amino-acids is limited.     

Peroxidase activity of cytochrome <Emphasis Type="Italic">bd</Emphasis> from <Emphasis Type="Italic">Escherichia coli</Emphasis>

Cytochrome bd from Escherichia coli is able to oxidize such substrates as guaiacol, ferrocene, benzohydroquinone, and potassium ferrocyanide through the peroxidase mechanism, while none of these donors is oxidized in the oxidase reaction (i.e. in the reaction that involves molecular oxygen as the electron acceptor). Peroxidation of guaiacol has been studied in detail. The dependence of the rate of the reaction on the concentration of the enzyme and substrates as well as the effect of various inhibitors of the oxidase reaction on the peroxidase activity have been tested. The dependence of the guaiacol-peroxidase activity on the H₂O₂ concentration is linear up to the concentration of 8 mM. At higher concentrations of H₂O₂, inactivation of the enzyme is observed. Guaiacol markedly protects the enzyme from inactivation induced by peroxide. The peroxidase activity of cytochrome bd increases with increasing guaiacol concentration, reaching saturation in the range from 0.5 to 2.5 mM, but then starts falling. Such inhibitors of the ubiquinol-oxidase activity of cytochrome bd as cyanide, pentachlorophenol, and 2-n-heptyl 4-hydroxyquinoline-N-oxide also suppress its guaiacol-peroxidase activity; in contrast, zinc ions have no influence on the enzyme-catalyzed peroxidation of guaiacol. These data suggest that guaiacol interacts with the enzyme in the center of ubiquinol binding and donates electrons into the di-heme center of oxygen reduction via heme b ₅₅₈, and H₂O₂ is reduced by heme d. Although the peroxidase activity of cytochrome bd from E. coli is low compared to peroxidases, it might be of physiological significance for the bacterium itself and plays a pathophysiological role for humans and animals.     

Enhanced production of recombinant galactose oxidase from <Emphasis Type="Italic">Fusarium graminearum</Emphasis> in <Emphasis Type="Italic">E. coli</Emphasis>

The gene gaoA encoding the copper-dependent enzyme galactose oxidase (GAO) from Fusarium graminearum PH-1 was cloned and successfully overexpressed in E. coli. Culture conditions for cultivations in shaken flasks were optimized, and optimal conditions were found to be double-strength LB medium, 0.5% lactose as inducer, and induction at the reduced temperature of 25°C. When using these cultivation conditions ~24 mg of active GAO could be produced in shaken flasks per litre medium. Addition of copper to the fermentation medium decreased the enzyme production significantly. The His-tagged recombinant enzyme could be purified conveniently with a single affinity chromatography step. The purified enzyme showed a single band on SDS–PAGE with an apparent molecular mass of 66 kDa and had kinetic properties similar to those of the fungal wild-type enzyme.     

Extracellular expression of keratinase Ker P from <Emphasis Type="Italic">Pseudomonas aeruginosa</Emphasis> in <Emphasis Type="Italic">E. coli</Emphasis>

Keratinase from Pseudomonas aeruginosa KS-1 was expressed constitutively as an extracellular protein in Escherichia coli with high specific activity of 3.7 kU/mg. It was purified fourfold as a 33 kDa monomeric protein by Q-Sepharose ion exchange chromatography with a recovery of 95%. It is a serine protease with optimal activity at pH 9 and 50°C. It was stable from pH 4 to 12 for 1 h with a t_1/2 of 12 min at 70°C. It hydrolyzed haemoglobin > fibrin > feather keratin > azo-casein > casein > meat protein > gelatin. Among synthetic substrates, it efficiently hydrolyzed N-Suc-ala-ala-pro-phe-pNA, N-Suc-ala-ala-ala-pNA, N-Suc-ala-ala-pro-leu-pNA and also plasmin substrate, d-Val-Leu-Lys-pNA