Expression of various genes to enhance ubiquinone metabolic pathway in Agrobacterium tumefaciens

Ubiquinone (UQ), a lipid-soluble component, acts as a mobile component of the respiratory chain by playing an essential role in the electron transport system in many organisms, and has been widely used in pharmaceuticals due to its antioxidant property. The biosynthesis of UQ involves 10 sequential reactions brought about by various enzymes. In this study, dps gene, which encodes decaprenyl diphosphate synthase, involved in ubiquinone biosynthesis from Agrobacterium tumefaciens, and coq2 gene of Saccharomyces cerevisiae, ppt1 gene of Schizosaccahromyces pombe and ubiA gene of Escherichia coli, all of them encoding 4-hydroxybenzoate:polyprenyl diphosphate (4-HB:PPP) transferase, were reconfigured into an operon under the control of a single promoter to yield various plasmids including pBIV-dps, pBIV-dpsq, pBIV-dpsp and pBIV-dpsca. The recombinant A. tumefaciens containing dps-ubiC-ubiA gene showed the highest level ubiquinone production than that of the other recombinants and the nonrecombinant bacterium. In an aerobic fed-batch fermentation, A. tumefaciens containing the pBIV-dpsca plasmid produced 25.2 mg of ubiquinone-10 per liter which was 1.68 times higher than that of nonrecombinant type. While in microaerobic fed-batch fermentation, recombinant cell pBIV-dpsca produced 30.8 mg L⁻¹ of ubiquinone-10. Compared to the original A. tumefaciens, the ubiquinone-10 yield and productivities of the recombinant bacterium pBIV-dpsca increased 88.9% and 77.7%, respectively, under microaerobic fed-batch conditions.     

High efficiency production of astaxanthin by autotrophic cultivation of Haematococcus pluvialis in a bubble column photobioreactor

Haematococcus pluvialis was cultivated under photoautotrophic conditions in a bubble column with fed-batch addition of nutrients, especially nitrate, and a cell number above 5 × 10⁶ cells mL⁻¹ was attained after 300 h.The reduction of nutrient concentrations accompanied by dilution of the fermentation broth and an increase in the light intensity enhanced accumulation of astaxanthin. The final astaxanthin concentration of 390 mg L⁻¹ was several times higher than ever reported. This combination of fed-batch addition of nutrients and dilution of broth for nutrient deficiency is a promising method for attainment of high cell and astaxanthin concentrations in a bubble column photobioreactor.     

Combined strategies for improving the heterologous expression of an alkaline lipase from Acinetobacter radioresistens CMC-1 in Pichia pastoris

In this study, a series of strategies was developed to enhance the expression of an alkaline lipase from Acinetobacter radioresistens (ARL) in Pichia pastoris. Activity of the lipase from recombinant strain carrying a single copy of codon-optimized ARL gene was 65 U/mL in shake flask culture with p-nitrophenyl caprylate as the substrate. The lipase yield was increased to 104 U/mL by introducing a short N-extension spacer peptide coding for the 10 amino acids (EEAEAEAEPK) between α-factor signal peptide and ARL. The N-terminal extension spacer did not affect the pH or temperature properties of the recombinant ARL. After the multi-copy constructs were identified by Q-PCR assay, a higher lipase activity of 180 U/mL was obtained. Further introduction of the spliced HAC1 gene into multi-copy integrants (>6 copies) extensively enhanced the ARL yield by 30–40%. As a result, the ARL yield reached 1.06 × 10⁴ U/mL in a 10-L scaled-up fed-batch fermenter as well as the lipase showed some better properties compared to that wild one from A. radioresistens.     

Fed-batch fermentation of recombinant Citrobacter freundii with expression of a violacein-synthesizing gene cluster for efficient violacein production from glycerol

The extensive prospects of violacein in the pharmaceutical industry have attracted increasing interest. However, the fermentation levels of violacein are currently inadequate to meet the demands of industrial production. This study was undertaken to develop an efficient process for the production of violacein by recombinant Citrobacter freundii. The effects of dissolved oxygen (DO) and pH on cell growth and violacein production in batch cultures were investigated first. When the DO and pH of the medium were controlled at around 25% and 7.0, respectively, the biomass and concentration of violacein were maximized. Based on the consumption of nutrients in the medium observed during batch culture, a fed-batch fermentation strategy with controlled DO and pH was implemented. By continuously feeding glycerol, NH₄Cl, and l-tryptophan at a constant feeding rate of 16 mL h⁻¹, the final concentration of violacein reached 4.13 g L⁻¹, which was 4.09-fold higher than the corresponding batch culture, and the maximal dry cell weight (DCW) and average violacein productivity obtained for the fed-batch culture were 3.34 g DCW L⁻¹ and 82.6 mg L⁻¹ h⁻¹, respectively. To date, this is the first report on the efficient production of violacein by genetically engineered strains in a fermentor.     

Efficient production of (R)-(−)-mandelic acid with highly substrate/product tolerant and enantioselective nitrilase of recombinant Alcaligenes sp.

For efficient production of (R)-(−)-mandelic acid, a nitrilase gene from Alcaligenes sp. ECU0401 was cloned and overexpressed in Escherichia coli. After simple optimization of the culture conditions, the biocatalyst production was greatly increased from 500 to 7000 U/l. The recombinant E. coli whole cells showed strong tolerance against a high substrate concentration of up to 200 mM, and the concentration of (R)-(−)-mandelic acid after only 4 h of transformation reached 197 mM with an enantiomeric excess (ee_p) of 99%. In a fed-batch reaction with 600 mM mandelonitrile as the substrate, the cumulative production of (R)-(−)-mandelic acid after 17.5 h of conversion reached 520 mM. The recombinant E. coli cells could also be repeatedly used in the biotransformation, retaining 40% of the initial activity after 10 batches of reaction. The highly substrate/product tolerable and enantioselective nature of this recombinant nitrilase suggests that it is of great potential for the practical production of optically pure (R)-(−)-mandelic acid.     

Enhancing GDP-fucose production in recombinant Escherichia coli by metabolic pathway engineering

Guanosine 5′-diphosphate (GDP)-fucose is the indispensible donor substrate for fucosyltransferase-catalyzed synthesis of fucose-containing biomolecules, which have been found involving in various biological functions. In this work, the salvage pathway for GDP-fucose biosynthesis from Bacterioides fragilis was introduced into Escherichia coli. Besides, the biosynthesis of guanosine 5′-triphosphate (GTP), an essential substrate for GDP-fucose biosynthesis, was enhanced via overexpression of enzymes involved in the salvage pathway of GTP biosynthesis. The production capacities of metabolically engineered strains bearing different combinations of recombinant enzymes were compared. The shake flask fermentation of the strain expressing Fkp, Gpt, Gmk and Ndk obtained the maximum GDP-fucose content of 4.6 ± 0.22 μmol/g (dry cell mass), which is 4.2 fold that of the strain only expressing Fkp. Through fed-batch fermentation, the GDP-fucose content further rose to 6.6 ± 0.14 μmol/g (dry cell mass). In addition to a better productivity than previous fermentation processes based on the de novo pathway for GDP-fucose biosynthesis, the established schemes in this work also have the advantage to be a potential avenue to GDP-fucose analogs encompassing chemical modification on the fucose residue.     

Cloning,purification and characterization of a thermostable β-galactosidase from Thermotoga naphthophila RUK-10

A novel β-galactosidase gene (Tnap1577) from the hyperthermophilic bacterium Thermotoga naphthophila RUK-10 was cloned and expressed in Escherichia coli BL21 (DE3) cells to produce β-galactosidase. The recombinant β-galactosidase was purified in three steps: heat treatment to deactivate E. coli proteins, Ni-NTA affinity chromatography and Q-sepharose chromatography. The optimum temperatures for the hydrolysis of o-nitrophenyl-β-d-galactoside (o-NPG) and lactose with the recombinant β-galactosidase were found to be 90 °C and 70 °C, respectively. The corresponding optimum pH values were 6.8 and 5.8, respectively. The molecular mass of the enzyme was estimated to be 70 kDa by SDS-PAGE analysis. Thermostability studies showed that the half-lives of the recombinant enzyme at 75 °C, 80 °C, 85 °C and 90 °C were 10.5, 4, 1, and 0.3 h, respectively. Kinetic studies on the recombinant β-galactosidase revealed K_m values for the hydrolysis of o-NPG and lactose of 1.31 mM and 1.43 mM, respectively. These values are considerably lower than those reported for other hyperthermophilic β-galactosidases, indicating high intrinsic affinity for these substrates. The recombinant β-galactosidase from Thermotoga naphthophila RUK-10 also showed transglycosylation activity in the synthesis of alkyl galactopyranoside. This additional activity suggests the enzyme has potential for broader biotechnological applications beyond the degradation of lactose.     

Modulation of guanosine 5′-diphosphate-d-mannose metabolism in recombinant Escherichia coli for production of guanosine 5′-diphosphate-l-fucose

Guanosine 5’-diphosphate (GDP)-l-fucose, an activated form of a nucleotide sugar, plays an important role in a wide range of biological functions. In this study, the enhancement of GDP-l-fucose production was attempted by supplementation of mannose, which is a potentially better carbon source to be converted into GDP-l-fucose than glucose, and combinatorial overexpression of the genes involved in the biosynthesis of GDP-d-mannose, a precursor of GDP-l-fucose. Supply of a mannose and glucose led to a 1.3-fold-increase in GDP-l-fucose concentration (52.5 ± 0.8 mg l^?1) in a fed-batch fermentation of recombinant E. coli BL21star(DE3) overexpressing the gmd and wcaG genes, compared with the case using glucose as a sole carbon source. A maximum GDP-l-fucose concentration of 170.3 ± 2.3 mg l^?1, corresponding to a 4.4-fold enhancement compared with the control strain overexpressing gmd and wcaG genes only, was achieved in a glucose-limited fed-batch fermentation of a recombinant E. coli BL21star(DE3) strain overexpressing manB, manC, gmd and wcaG genes. Further improvement of GDP-l-fucose production was not obtained by additional overexpression of the manA gene.     

Operation of a fixed-bed bioreactor in batch and fed-batch modes for production of inulinase by solid-state fermentation

This work is focused on the inulinase production by solid-state fermentation (SSF) in a fixed-bed reactor (34 cm diameter and 50 cm height) with working capacity of 2-kg of dry substrate operated in batch and fed-batch modes. It was investigated different strategies for feeding the inlet air in the bioreactor (saturated and unsaturated air) as alternative to remove the metabolic heat generated during the microbial growth by evaporative cooling. The kinetic evaluation of the process carried out in batch mode using unsaturated air showed that the evaporative cooling decreasing the mean temperature of the solid-bed, although the enzyme production was lower than that obtained using saturated air. Results showed that maximum enzyme activity (586 ± 63 U gds⁻¹) was obtained in the fed-batch mode using saturated air after 24 h of fermentation. The enzymatic extract obtained by fed-batch mode was characterized and presented optimum temperature and pH in the range of 52–57 °C and 4.8–5.2, respectively. For a temperature range from 40 to 70 °C the enzyme presented decimal reduction time, D-value, ranging from 5748 to 47 h, respectively. For a pH range from 3.5 to 5.5 the enzyme showed good stability, presenting D-values higher than 2622 h. In terms of Michaelis–Mentem parameters were demonstrated that the crude inulinase activity presented higher affinity for substrate sucrose compared to inulin.     

Simultaneous saccharification and fermentation of kraft pulp by recombinant Escherichia coli for phenyllactic acid production

Simultaneous saccharification and fermentation (SSF) of renewable cellulose for the production of 3-phenyllactic acid (PhLA) by recombinant Escherichia coli was investigated. Kraft pulp recovered from biomass fractionation processes was used as a model cellulosic feedstock and was hydrolyzed using 10–50 filter paper unit (FPU) g⁻¹ kraft pulp of a commercial cellulase mixture, which increased the glucose yield from 21% to 72% in an enzyme dose-dependent manner. PhLA fermentation of the hydrolyzed kraft pulp by a recombinant E. coli strain expressing phenylpyruvate reductase from Wickerhamia fluorescens TK1 produced 1.9 mM PhLA. The PhLA yield obtained using separate hydrolysis and fermentation was enhanced from 5.8% to 42% by process integration into SSF of kraft pulp (20 g L⁻¹) in a complex medium (pH 7.0) at 37 °C. The PhLA yield was negatively correlated with the initial glucose concentration, with a five-fold higher PhLA yield observed in culture medium containing 10 g L⁻¹ glucose compared to 100 g L⁻¹. Taken together, these results suggest that the PhLA yield from cellulose in kraft pulp can be improved by SSF under glucose-limited conditions.     

Coenzyme Q10 in human blood: Native levels and determinants of oxidation during processing and storage

Coenzyme Q10 (Q10) is present in the circulation mainly in its reduced form (ubiquinol-10; UL10), but oxidizes quickly ex vivo to ubiquinone-10 (UN10). Therefore, native UL10:UN10 ratios, used as markers of redox status and disease risk, are difficult to measure. We established an RP-(U)HPLC method with coulometric detection to measure natively circulating UL10 and UN10 concentrations by adding a ubiquinol/ubiquinone mixture as an internal standard immediately after plasma preparation. This allowed adjustment for unavoidable artificial UL10 oxidation as well as for total losses (or gains) of analytes during sample storage, processing, and analysis because the internal standards exactly paralleled the chemical behavior of Q10. This technique applied to blood (n = 13) revealed Q10 levels of 680–3300 nM with a mean UL10:UN10 ratio of 95:5, which was inversely associated with total Q10 (r = ? 0.69; p = 0.004). The oxidation of UL10 to UN10 was equimolar, increased by O₂, and decreased by lower temperatures or various degassing methods. Although UL10 was stable in blood or when pure in organic solvents at 22 °C, its oxidation was catalyzed dose dependently by α-tocopherol and butylated hydroxytoluene, particularly when present in combination. Key structural features for the catalytic pro-oxidant properties of phenolic antioxidants included two substituents vicinal to the phenolic hydroxyl group.     

Secretory expression of functional barley limit dextrinase by Pichia pastoris using high cell-density fermentation

Heterologous production of large multidomain proteins from higher plants is often cumbersome. Barley limit dextrinase (LD), a 98 kDa multidomain starch and α-limit dextrin debranching enzyme, plays a major role in starch mobilization during seed germination and is possibly involved in starch biosynthesis by trimming of intermediate branched α-glucan structures. Highly active barley LD is obtained by secretory expression during high cell-density fermentation of Pichia pastoris. The LD encoding gene fragment without signal peptide was subcloned in-frame with the Saccharomyces cerevisiae α-factor secretion signal of the P. pastoris vector pPIC9K under control of the alcohol oxidase 1 promoter. Optimization of a fed-batch fermentation procedure enabled efficient production of LD in a 5-L bioreactor, which combined with affinity chromatography on β-cyclodextrin–Sepharose followed by Hiload Superdex 200 gel filtration yielded 34 mg homogenous LD (84% recovery). The identity of the recombinant LD was verified by N-terminal sequencing and by mass spectrometric peptide mapping. A molecular mass of 98 kDa was estimated by SDS–PAGE in excellent agreement with the theoretical value of 97419 Da. Kinetic constants of LD catalyzed pullulan hydrolysis were found to K_m,app = 0.16 ± 0.02 mg/mL and k_cat,app = 79 ± 10 s^?1 by fitting the uncompetitive substrate inhibition Michaelis–Menten equation, which reflects significant substrate inhibition and/or transglycosylation. The resulting catalytic coefficient, k_cat,app/K_m,app = 488 ± 23 mL/(mg s) is 3.5-fold higher than for barley malt LD. Surface plasmon resonance analysis showed α-, β-, and γ-cyclodextrin binding to LD with K_d of 27.2, 0.70, and 34.7 μM, respectively.     

Metabolic engineering of Escherichia coli for the production of 5-aminovalerate and glutarate as C5 platform chemicals

5-Aminovalerate (5AVA) is the precursor of valerolactam, a potential building block for producing nylon 5, and is a C5 platform chemical for synthesizing 5-hydroxyvalerate, glutarate, and 1,5-pentanediol. Escherichia coli was metabolically engineered for the production of 5-aminovalerate (5AVA) and glutarate. When the recombinant E. coli WL3110 strain expressing the Pseudomonas putida davAB genes encoding delta-aminovaleramidase and lysine 2-monooxygenase, respectively, were cultured in a medium containing 20 g/L of glucose and 10 g/L of l-lysine, 3.6 g/L of 5AVA was produced by converting 7 g/L of l-lysine. When the davAB genes were introduced into recombinant E. coli strainXQ56allowing enhanced l-lysine synthesis, 0.27 and 0.5 g/L of 5AVA were produced directly from glucose by batch and fed-batch cultures, respectively. Further conversion of 5AVA into glutarate could be demonstrated by expression of the P. putida gabTD genes encoding 5AVA aminotransferase and glutarate semialdehyde dehydrogenase. When recombinant E. coli WL3110 strain expressing the davAB and gabTD genes was cultured in a medium containing 20 g/L glucose, 10 g/L l-lysine and 10 g/L α-ketoglutarate, 1.7 g/L of glutarate was produced.     

Constitutive expression of a novel isoamylase from Bacillus lentus in Pichia pastoris for starch processing

Isoamylase is essential to saccharifying starch by cleavage of 1,6-glucoside linkages in starch molecules. In this study, a novel isoamylase gene from Bacillus lentus JNU3 was cloned. The open reading frame of the gene was 2412 base pairs long and encoded a polypeptide of 804 amino acids with a calculated molecular mass of 90 kDa. The deduced amino acid sequence shared less than 40% homology with that of microbial isoamylase ever reported, which indicated it was a novel isoamylase. A constitutive GAP promoter was used to express the recombinant isoamylase in the yeast Pichia pastoris by continuous high cell-density fermentation to avoid the use of methanol, which resulted in 318 U/mL extracellular isoamylase activity after 72 h in a 10 L fermenter. The recombinant enzyme was purified and characterized. It had an estimated molecular mass of 90 kDa, with its optimal activity at 70 °C, pH 6.5 and was quite stable between 30 °C and 70 °C. The recombinant isoamylase proves to be superior to pullulanase as an auxiliary enzyme in maltose production from starch. Therefore it will contribute significantly to the starch debranching process.     

Fermentative production of succinic acid from straw hydrolysate by Actinobacillus succinogenes

In this work, straw hydrolysates were used to produce succinic acid by Actinobacillus succinogenes CGMCC1593 for the first time. Results indicated that both glucose and xylose in the straw hydrolysates were utilized in succinic acid production, and the hydrolysates of corn straw was better than that of rice or wheat straw in anaerobic fermentation of succinic acid. However, cell growth and succinic acid production were inhibited when the initial concentration of sugar, which was from corn straw hydrolysate (CSH), was higher than 60 g l^?1. In batch fermentation, 45.5 g l^?1 succinic acid concentration and 80.7% yield were attained after 48 h incubation with 58 g l^?1 of initial sugar from corn straw hydrolysate in a 5-l stirred bioreactor. While in fed-batch fermentation, concentration of succinic acid achieved 53.2 g l^?1 at a rate of 1.21 g l^?1 h^?1 after 44 h of fermentation. Our work suggested that corn straw could be utilized for the economical production of succinic acid by A. succinogenes.     

Bio-based succinate from sucrose: High-resolution 13C metabolic flux analysis and metabolic engineering of the rumen bacterium Basfia succiniciproducens

Succinic acid is a platform chemical of recognized industrial value and accordingly faces a continuous challenge to enable manufacturing from most attractive raw materials. It is mainly produced from glucose, using microbial fermentation. Here, we explore and optimize succinate production from sucrose, a globally applied substrate in biotechnology, using the rumen bacterium Basfia succiniciproducens DD1. As basis of the strain optimization, the yet unknown sucrose metabolism of the microbe was studied, using ¹³C metabolic flux analyses. When grown in batch culture on sucrose, the bacterium exhibited a high succinate yield of 1 mol mol⁻¹ and a by-product spectrum, which did not match the expected PTS-mediated sucrose catabolism. This led to the discovery of a fructokinase, involved in sucrose catabolism. The flux approach unraveled that the fructokinase and the fructose PTS both contribute to phosphorylation of the fructose part of sucrose. The contribution of the fructokinase reduces the undesired loss of the succinate precursor PEP into pyruvate and into pyruvate-derived by-products and enables increased succinate production, exclusively via the reductive TCA cycle branch. These findings were used to design superior producers. Mutants, which (i) overexpress the beneficial fructokinase, (II) lack the competing fructose PTS, and (iii) combine both traits, produce significantly more succinate. In a fed-batch process, B. succiniciproducens ΔfruA achieved a titer of 71 g L⁻¹ succinate and a yield of 2.5 mol mol⁻¹ from sucrose.     

Purification and characterisation of a xylanase from Thermomyces lanuginosus and its functional expression by Pichia pastoris

A xylanase produced by Thermomyces lanuginosus 195 by solid state fermentation (SSF) was purified 9.3-fold from a crude koji extract, with a 7.6% final yield. The purified xylanase (with an estimated mass of 22 kDa by SDS-PAGE) retained 18% relative activity when treated for 10 min at 100 °C and approximately 90% relative activity when incubated at pH values ranging from 6 to 10. Xylanase activity in the purified preparation was significantly enhanced following treatment with manganese and potassium chlorides (p < 0.05) but significantly reduced by calcium, cobalt and iron (p < 0.05). The purified enzyme was also shown to be exclusively xylanolytic. The gene encoding xylanase activity from T. lanuginosus 195 was functionally expressed by Pichia pastoris. MALDI-ToF mass spectrometry and zymography were employed to confirm functional recombinant expression. Maximum xylanase titres were achieved following 120 h induction of the recombinant culture, yielding 26.8 U/mL. Achieving functional protein expression facilitates future efforts to optimise the cultivation conditions for heterologous xylanase production.     

The P170 expression system enhances hyaluronan molecular weight and production in metabolically-engineered Lactococcus lactis

Recombinant Lactococcus lactis strains based on the P170 expression system were developed for hyaluronan (HA) production, by incorporating genes from the has operon of Streptococcus zooepidemicus and compared with nisin-inducible recombinant L. lactis strains containing the hasABC and hasABD constructs. It was found across all batch and fed-batch experimental studies that HA concentration and molecular weight (MW) were higher for the P170 expression systems than the corresponding NICE-based strains. The highest hyaluronan MW was obtained for all constructs in batch studies at 60 g/L initial glucose concentration, the highest being 2.94 MDa for the P170 strains with hasABC construct (L. lactis APJ3). In fed-batch studies with constant feed rate, the L. lactis APJ3 gave better HA yield (0.03 g/g) than the NICE-based strain. A higher hyaluronan MW was obtained for all strains in pulse fed-batch compared to constant feed experiments, the highest being 2.52 MDa for L. lactis APJ3.     

Enhanced production of valienamine by Stenotrophomonas maltrophilia with fed-batch culture in a stirred tank bioreactor

Valienamine is an important medicinal intermediate with broad use in the synthesis of some stronger α-glucosidase inhibitors. In order to improve valienamine concentration in the fermentation broth and make the downstream treatment easy, a fed-batch process for the enhanced production of valienamine by Stenotrophomonas maltrophilia in a stirred tank bioreactor was developed. Results showed that supplementation of validamycin A in the process of cultivation could increase the valienamine concentration. One-pulse feeding was observed to be the best strategy. The maximum valienamine concentration of 2.35 g L⁻¹ was obtained at 156 h when 86.4 g of validamycin A was added to a 15-L bioreactor containing 8 L fermentation medium with one-pulse feeding. The maximum valienamine concentration had a great improvement and was increased above 100% compared to batch fermentation in the stirred tank bioreactor. The pH-controlled experiments showed that controlling the pH in the process of one-pulse feeding fermentation had not obvious effect on the production of valienamine.