Overexpression of a type II 3-dehydroquinate dehydratase enhances the biotransformation of quinate to 3-dehydroshikimate in Gluconobacter oxydans

Shikimate and 3-dehydroshikimate are useful chemical intermediates for the synthesis of various compounds, including the antiviral drug oseltamivir. Here, we show an almost stoichiometric biotransformation of quinate to 3-dehydroshikimate by an engineered Gluconobacter oxydans strain. Even under pH control, 3-dehydroshikimate was barely detected during the growth of the wild-type G. oxydans strain NBRC3244 on the medium containing quinate, suggesting that the activity of 3-dehydroquinate dehydratase (DHQase) is the rate-limiting step. To identify the gene encoding G. oxydans DHQase, we overexpressed the gox0437 gene from the G. oxydans strain ATCC621H, which is homologous to the aroQ gene for type II DHQase, in Escherichia coli and detected high DHQase activity in cell-free extracts. We identified the aroQ gene in a draft genome sequence of G. oxydans NBRC3244 and constructed G. oxydans NBRC3244 strains harboring plasmids containing aroQ and different types of promoters. All recombinant G. oxydans strains produced a significant amount of 3-dehydroshikimate from quinate, and differences between promoters affected 3-dehydroshikimate production levels with little statistical significance. By using the recombinant NBRC3244 strain harboring aroQ driven by the lac promoter, a sequential pH adjustment for each step of the biotransformation was determined to be crucial because 3-dehydroshikimate production was enhanced. Under optimal conditions with a shift in pH, the strain could efficiently produce a nearly equimolar amount of 3-dehydroshikimate from quinate. In the present study, one of the important steps to convert quinate to shikimate by fermenting G. oxydans cells was investigated.     

Biotransformation of glucose to 5-keto-<Emphasis Type="SmallCaps">d</Emphasis>-gluconic acid by recombinant<Emphasis Type="Italic"> Gluconobacter oxydans</Emphasis> DSM 2343

For the conversion of glucose to 5-keto-d-gluconate (5-KGA), a precursor of the industrially important l-(+)-tartaric acid, Gluconobacter strains were genetically engineered. In order to increase 5-KGA formation, a plasmid-encoded copy of the gene encoding the gluconate:NADP-5 oxidoreductase (gno) was overexpressed in G. oxydans strain DSM 2434. This enzyme is involved in the nonphosphorylative ketogenic oxidation of glucose and oxidizes gluconate to 5-KGA. As the 5-KGA reductase activity depends on the cofactor NADP⁺, the sthA gene (encoding Escherichia coli transhydrogenase) was cloned and overexpressed in the GNO-overproducing G. oxydans strain. Growth of the sthA-carrying strains was indistinguishable from the G. oxydans wild-type strain and therefore they were chosen for the coupled overexpression of sthA and gno. G. oxydans strain DSM 2343/pRS201-gno-sthA overproducing both enzymes showed an enhanced accumulation of 5-KGA.     

<Emphasis Type="Italic">Gluconobacter oxydans</Emphasis> NAD-dependent, <Emphasis Type="SmallCaps">D</Emphasis>-fructose reducing,polyol dehydrogenases activity: screening,medium optimisation and application for enzymatic polyol production

Gluconobacter oxydans LMG 1489 was selected as the best strain for NAD(P)-dependent polyol dehydrogenase production. The highest enzyme activities were obtained when this strain was cultivated on a medium consisting of 30 g glycerol l^–1, 7.2 g peptone l–1 and 1.8 g yeast extract l^–1. Two D-fructose reducing, NAD-dependent intracellular enzymes were present in the G. oxydans cell-free extract: sorbitol dehydrogenase, and mannitol dehydrogenase. Substrate reduction occurred optimally at a low pH (pH 6), while the optimum for substrate oxidation was situated at alkaline pHs (pH 9.5–10.5). The mannitol dehydrogenase was more thermostable than the sorbitol dehydrogenase. The cell-free extract could be used to produce D-mannitol and D-sorbitol enzymatically from D-fructose. Efficient coenzyme regeneration was accomplished by formate dehydrogenase-mediated oxidation of formate into CO₂.     

High-yield 5-keto-d-gluconic acid formation is mediated by soluble and membrane-bound gluconate-5-dehydrogenases of Gluconobacter oxydans

Gluconobacter oxydans DSM 2343 is known to catalyze the oxidation of glucose to gluconic acid, and subsequently, to 2-keto-d-gluconic acid (2-KGA) and 5-keto-d-gluconic acid (5-KGA), by membrane-bound and soluble dehydrogenases. In G. oxydans MF1, in which the membrane-bound gluconate-2-dehydrogenase complex was inactivated, formation of the undesired 2-KGA was absent. This mutant strain uniquely accumulates high amounts of 5-KGA in the culture medium. To increase the production rate of 5-KGA, which can be converted to industrially important l-(+)-tartaric acid, we equipped G. oxydans MF1 with plasmids allowing the overproduction of the soluble and the membrane-bound 5-KGA-forming enzyme. Whereas the overproduction of the soluble gluconate:NADP 5-oxidoreductase resulted in the accumulation of up to 200 mM 5-KGA, the detected 5-KGA accumulation was even higher when the gene coding for the membrane-bound gluconate-5-dehydrogenase was overexpressed (240 to 295 mM 5-KGA). These results provide a basis for designing a biotransformation process for the conversion of glucose to 5-KGA using the membrane-bound as well as the soluble enzyme system.The corresponding author contributed equally to the first author.     

A Gluconobacter oxydans mutant converting glucose almost quantitatively to 5-keto-d-gluconic acid

Gluconobacter oxydans converts glucose to gluconic acid and subsequently to 2-keto-d-gluconic acid (2-KGA) and 5-keto-d-gluconic acid (5-KGA) by membrane-bound periplasmic pyrroloquinoline quinone-dependent and flavin-dependent dehydrogenases. The product pattern obtained with several strains differed significantly. To increase the production of 5-KGA, which can be converted to industrially important l-(+)-tartaric acid, growth parameters were optimized. Whereas resting cells of G. oxydans ATCC 621H converted about 11% of the available glucose to 2-KGA and 6% to 5-KGA, with growing cells and improved growth under defined conditions (pH 5, 10% pO₂, 0.05% pCO₂) a conversion yield of about 45% 5-KGA from the available glucose was achieved. As the accumulation of the by-product 2-KGA is highly disadvantageous for an industrial application of G. oxydans, a mutant was generated in which the membrane-bound gluconate-2-dehydrogenase complex was inactivated. This mutant, MF1, grew in a similar way to the wild type, but formation of the undesired 2-KGA was not observed. Under improved growth conditions, mutant MF1 converted the available glucose almost completely (84%) into 5-KGA. Therefore, this newly developed recombinant strain is suitable for the industrial production of 5-KGA.     

Genetic analysis of D-xylose metabolism pathways in Gluconobacter oxydans 621H

D-xylose is one of the most abundant carbohydrates in nature. This work focuses on xylose metabolism of Gluconobacter oxydans as revealed by a few studies conducted to understand xylose utilization by this strain. Interestingly, the G. oxydans 621H Δmgdh strain (deficient in membrane-bound glucose dehydrogenase) was greatly inhibited when grown on xylose and no xylonate accumulation was observed in the medium. These experimental observations suggested that the mgdh gene was responsible for the conversion of xylose to xylonate in G. oxydans, which was also verified by whole-cell biotransformation. Since 621H Δmgdh could still grow on xylose in a very small way, two seemingly important genes in the oxo-reductive pathway for xylose metabolism, a xylitol dehydrogenase-encoding gox0865 (xdh) gene and a putative xylulose kinase-encoding gox2214 (xk) gene, were knocked out to investigate the effects of both genes on xylose metabolism. The results showed that the gox2214 gene was not involved in xylose metabolism, and there might be other genes encoding xylulose kinase. Though the gox0865 gene played a less important role in xylose metabolism compared to the mgdh gene, it was significant in xylitol utilization in G. oxydans, which meant that gox0865 was a necessary gene for the oxo-reductive pathway of xylose in vivo. To sum up, when xylose was used as the carbon source, the majority of xylose was directly oxidized to xylonate for further metabolism in G. oxydans, whereas only a minor part of xylose was metabolized by the oxo-reductive pathway.     

Growth effects and assimilation of organic acids in chemostat and batch cultures of <Emphasis Type="Italic">Acidithiobacillus caldus</Emphasis>

The ability of Acidithiobacillus caldus to grow aerobically using pyruvate, acetate, citrate, 2-ketoglutarate, succinate, and malate as either an electron donor and carbon source (heterotrophic growth), or as a carbon source when potassium tetrathionate was added as an electron donor (mixotrophic growth), was tested in chemostat cultures. Under both heterotrophic and mixotrophic conditions, organic acids were added to a sub-lethal concentration (50 μM). Under mixotrophic conditions, potassium tetrathionate was added to an excess concentration (10 mM). No cell growth was observed under heterotrophic conditions; however, effluent cell concentrations increased over threefold when pyruvate was coupled with potassium tetrathionate. Under these conditions, the effluent pyruvate concentration was reduced to below the detection limit (2 μM), and oxygen consumption increased by approximately 100%. Although pyruvate provided a carbon source in these experiments, ambient carbon dioxide was also available to the cells. To test whether At. caldus could grow mixotrophically using pyruvate as a sole carbon source and potassium tetrathionate as an electron donor, cells were batch cultured in a medium free of dissolved inorganic carbon, and with no carbon dioxide in the headspace. These experiments showed that At. caldus was able to convert between 65 ± 8 and 82 ± 15% of the pyruvate carbon to cellular biomass, depending on the initial pyruvate concentrations. This work is the first to identify a defined organic-carbon source, other than glucose, that At. caldus can assimilate. This has important implications, as mixotrophic and heterotrophic activity has been shown to increase mineral leaching in acidic systems.     

Studies on the microbial production of theobromine and heteroxanthine from caffeine

Summary From soil a caffeine degrading bacterium was isolated which is able to grow on media containing up to 2% caffeine as the sole source of carbon and nitrogen. The organism was identified as Pseudomonas putida and referred to as Pseudomonas putida WS. Mutants of this strain converted caffeine and were shown to accumulate a mixture of theobromine and heteroxanthine during resting cells experiments.The highest yield in accumulation products was obtained with the mutant strain H8, however the production rate with resting cells was too small for commercial purposes. The yield was significantly increased by growth of the mutant on diluted complex media. With this technique a yield of 50% based on the amount of caffeine could be obtained for heteroxanthine. The concentration maximum is reached when caffeine is completely converted and only traces of theobromine are present.Dedicated to Professor G. Braunitzer on the occasion of his 65th birthday     

Ketogluconate formation by Gluconobacter species

Summary When G. oxydans ATCC 621-H was grown in batch culture in a complex medium with glucose, ketogluconates were produced when the pH in the culture was maintained at 5.5. Without pH control gluconate was the only product of glucose oxidation, but at pH 5.5 the gluconate so produced was further oxidized to ketogluconates. Production of ketogluconates started when glucose was almost completely exhausted. It was shown that the actual glucose and gluconate concentrations in the culture do not determine the onset of ketogluconate formation during growth. Both 2 and 5 ketogluconate were produced. Addition of CaCO₃ to the medium favored the production of 5 ketogluconate. However, under these conditions minor quantities of 2 ketogluconate were also formed. The sequential production of gluconate and ketogluconates from glucose was not only restricted to G. oxydans ATCC 621-H. A number of G. oxydans strains when grown under standard conditions in a pH controlled batch culture, all produced ketogluconates from glucose via an intermediate accumulation of gluconate. Although the ratios of the ketogluconates produced varied from strain to strain, all strains produced both 2 and 5 ketogluconate.     

Characterization of trophic changes and a functional oxidative pentose phosphate pathway in <Emphasis Type="Italic">Synechocystis</Emphasis> sp. PCC 6803

Cyanobacteria have a tremendous activity to adapt to environmental changes of their growth conditions. In this study, Synechocystis sp. PCC 6803 was used as a model organism to focus on the alternatives of cyanobacterial energy metabolism. Glucose oxidation in Synechocystis sp. PCC6803 was studied by inactivation of slr1843, encoding glucose-6-phosphate dehydrogenase (G6PDH), the first enzyme of the oxidative pentose phosphate pathway (OPPP). The resulting zwf strain was not capable of glucose supported heterotrophic growth. Growth under autotrophy and under mixotrophy was similar to that of the wild-type strain, even though oxygen evolution and uptake rates of the mutant were decreased in the presence of glucose. The organic acids citrate and succinate supported photoheterotrophic growth of both WT and zwf. Proteome analysis of soluble and membrane fractions allowed identification of four growth condition-dependent proteins, pentose-5-phosphate 3-epimerase (slr1622), inorganic pyrophosphatase (sll0807), hypothetical protein (slr2032) and ammonium/methylammonium permease (sll0108) revealing details of maintenance of the cellular carbon/nitrogen/phosphate balance under different modes of growth.     

Biotransformation of Meloxicam by <Emphasis Type="Italic">Cunninghamella blakesleeana</Emphasis>: Significance of Carbon and Nitrogen Source

Influence of carbon and nitrogen source, on biotransformation of meloxicam was studied by employing Cunninghamella blakesleeana NCIM 687 with an aim to achieve maximum transformation of meloxicam and in search of new metabolites. The transformation was confirmed by HPLC and based on LC–MS–MS data and previous reports the metabolites were predicted as 5-hydroxymethyl meloxicam, 5-carboxy meloxicam and a novel metabolite. The quantification of metabolites was performed using HPLC peak areas. The results obtained indicate that glucose as carbon source, ammonium nitrate as nitrogen source, were found to be optimum for maximum transformation of meloxicam. The study suggests the significance of these factors in biotransformation of meloxicam using microbial cultures. The fermentation was scaled up to 1 l level.     

Production of free gluconic acid by cells ofGluconobacter oxydans

Summary Microbial oxidation of glucose to free gluconic acid by growingG.oxydans batch cultures was investigated. Kinetic data for the discussed process were obtained and attention was paid mainly to the influence of the initial glucose concentration and of the conversion degree on the course of the process. It was determined that relatively high maximum specific growth rates of about 0,39 h⁻¹ and gluconic acid volumetric productivities up to 53 mmol/h could be reached usingG.oxydans NBIMCC 1043 in runs without pH control. A maximum conversion degree of 90,4% was achieved.     

Construction of a Novel Shuttle Vector for Use in <Emphasis Type="Italic">Gluconobacter oxydans</Emphasis>

A shuttle vector pZL1 which can replicate both in Gluconobacter oxydans and Escherichia coli was constructed based on G. oxydans DSM2003 cryptic plasmid pGOX3, a homology of G. oxydans 621H pGOX3, and E. coli cloning vector pUC18. It was found to be stably maintained in G. oxydans during the serial subcultures in the absence of antibiotic pressure for 144 h. With pGOX3 as the reference sample, the relative copy number of pZL1 in G. oxydans is 13 determined by real-time fluorescence quantitative PCR (qPCR). The copy number of pZL1 is much higher than pBBR1MCS5 in E. coli. The vector pZL1 contains six commonly used restriction endonuclease sites, HindIII, SalI, XbaI, BamHI, SmaI, KpnI, and SacI, and is easy to manipulate in molecular biology experiments. The shuttle vector was used to express a reporter protein wasabi successfully in G. oxydans DSM2003 under the control of the tufB promoter.     

An analysis of the growth of Gluconobacter oxydans in chemostat cultures

Gluconobacter oxydans was grown successively in glucose and nitrogen-limited chemostat cultures. Construction of mass balances of organisms growing at increasing dilution rates in glucose-limited cultures, at pH 5.5, revealed a major shift from extensive glucose metabolism via the pentose phosphate pathway to the direct pathway of glucose oxidation yielding gluconic acid. Thus, whereas carbon dioxide production from glucose accounted for 49.4% of the carbon input at a dilution rate (D)=0.05 h^-1, it accounted for only 1.3% at D=0.26 h^-1. This decline in pentose phosphate pathway activity resulted in decreasing molar growth yields on glucose. At dilution rates of 0.05 h^-1 and 0.26 h^-1 molar growth yields of 19.5 g/mol and 3.2 g/mol, respectively, were obtained. Increase of the steady state glucose concentration in nitrogen-limited chemostat cultures maintained at a constant dilution rate also resulted in a decreased flow of carbon through the pentose phosphate pathway. Above a threshold value of 15–20 mM glucose in the culture, pentose phosphate pathway activity almost completely inhibited. In G. oxydans the coupling between energy generation and growth was very inefficient; yield values obtained at various dilution rates varied between 0.8–3.4 g/cells synthesized per 0.5 mol of oxygen consumed.     

Biooxidation of 2-phenylethanol to phenylacetic acid by whole-cell Gluconobacter oxydans biocatalyst immobilized in polyelectrolyte complex capsules

A high-performance biocatalyst in the form of encapsulated cells of Gluconobacter oxydans have been developed for production of phenylacetic acid (PAA) as a natural flavor component. Polyelectrolyte complex (PEC) capsules consisting of sodium alginate, cellulose sulfate, poly(methylene-co-guanidine), CaCl₂, and NaCl were used for highly controlled and mild encapsulation of cells. Utilization of encapsulated G. oxydans cells was a significant improvement on existing data on operational stability of cells and cumulative product concentration during biocatalytic production of PAA from 2-phenylethanol. Concerning operational stability, encapsulated cells were active over 12 cycles with a high biotransformation rate, while free cells were inactive after 7 cycles of use. The biocatalytic properties of encapsulated G. oxydans were tested in a bubble column reactor over 7 days with a final cumulative product concentration of 25 g/L. High cell viability (90%) was observed within PEC capsules by confocal laser scanning microscopy, performed before and after repetitive PAA production in the bubble column reactor. The surface microstructure of fully hydrated capsules with and without G. oxydans cells was investigated and compared using an environmental scanning electron microscope.     

ATP limitation in a pyruvate formate lyase mutant of <Emphasis Type="Italic">Escherichia coli</Emphasis> MG1655 increases glycolytic flux to <Emphasis Type="SmallCaps">d</Emphasis>-lactate

A derivative strain of Escherichia coli MG1655 for d-lactate production was constructed by deleting the pflB, adhE and frdA genes; this strain was designated “CL3.” Results show that the CL3 strain grew 44% slower than its parental strain under nonaerated (fermentative) conditions due to the inactivation of the main acetyl-CoA production pathway. In contrast to E. coli B and W3110 pflB derivatives, we found that the MG1655 pflB derivative is able to grow in mineral media with glucose as the sole carbon source under fermentative conditions. The glycolytic flux was 2.8-fold higher in CL3 when compared to the wild-type strain, and lactate yield on glucose was 95%. Although a low cell mass formed under fermentative conditions with this strain (1.2 g/L), the volumetric productivity of CL3 was 1.31 g/L h. In comparison with the parental strain, CL3 has a 22% lower ATP/ADP ratio. In contrast to wild-type E. coli, the ATP yield from glucose to lactate is 2 ATP/glucose, so CL3 has to improve its glycolytic flux in order to fulfill its ATP needs in order to grow. The aceF deletion in strains MG1655 and CL3 indicates that the pyruvate dehydrogenase (PDH) complex is functional under glucose-fermentative conditions. These results suggest that the pyruvate to acetyl-CoA flux in CL3 is dependent on PDH activity and that the decrease in the ATP/ADP ratio causes an increase in the flux of glucose to lactate.     

Stereoselective epoxidation of <Emphasis Type="Italic">cis</Emphasis>-propenylphosphonic acid to fosfomycin by a newly isolated bacterium <Emphasis Type="Italic">Bacillus</Emphasis><Emphasis Type="Italic">simplex</Emphasis> strain S101

In industry, fosfomycin is mainly prepared via chemical epoxidation of cis-propenylphosphonic acid (cPPA). The conversion yield of fosfomycin is less than 50% in the whole process and a large quantity of waste is produced. Biotransformation by microorganisms is an alternative method of preparation. This kind of conversion is more delicate, environmentally friendly, and the conversion yield of fosfomycin would be higher. In this work, an aerobic bacterium capable of transforming cPPA to fosfomycin was isolated. The organism, designated as strain S101, was identified as Bacillus simplex by morphological and physiological characteristics as well as by analysis of the gene encoding the 16S rRNA. Fosfomycin was assayed by two means, bioassay and gas chromatography (GC). Glycerol was a good carbon source for growth and cPPA conversion of strain S101. When cPPA was used as the sole carbon source, neither growth nor conversion to fosfomycin occurred. The optimum cPPA concentration in the conversion medium was 2,000 μg ml⁻¹. After 6 days of incubation, the concentration of fosfomycin reached its maximum level (1,838.2 μg ml⁻¹), with a conversion ratio of 81.3%. Air was indispensable for the growth but not for the conversion to fosfomycin. Furthermore, vanadium ions were found to be essential for the conversion. High concentrations of cPPA had fewer inhibitory effects on the growth of strain S101.     

Effect of modified glucose catabolism on xanthan production in <Emphasis Type="Italic">Xanthomonas oryzae</Emphasis> pv. <Emphasis Type="Italic">oryzae</Emphasis>

In this study, the glucose 6-phosphate dehydrogenase gene (XOO2314) was inactivated in order to modulate the intracellular glucose 6-phosphate, and its effects on xanthan production in a wild-type strain of Xanthomonas oryzae were evaluated. The intracellular glucose 6-phosphate was increased from 17.6 to 99.4 μmol g⁻¹ (dry cell weight) in the gene-disrupted mutant strain. The concomitant increase in the glucose 6-phosphate was accompanied by an increase in xanthan production of up to 2.23 g l⁻¹ (culture medium). However, in defined medium supplemented with 0.4% glucose, the growth rate of the mutant strain was reduced to 52.9% of the wild-type level. Subsequently, when a family B ATP-dependent phosphofructokinase from Escherichia coli was overexpressed in the mutant strain, the growth rate was increased to 142.9%, whereas the yields of xanthan per mole of glucose remained approximately the same.     

Effects of membrane-bound glucose dehydrogenase overproduction on the respiratory chain of Gluconobacter oxydans

The acetic acid bacterium Gluconobacter oxydans incompletely oxidizes carbon sources as a natural part of its metabolism, and this feature has been exploited for many biotechnological applications. The most important enzymes used to harness the biocatalytic oxidative capacity of G. oxydans are the pyrroloquinoline quinone (PQQ)-dependent dehydrogenases. The membrane-bound PQQ-dependent glucose dehydrogenase (mGDH), encoded by gox0265, was used as model protein for homologous membrane protein production using the previously described Gluconobacter expression vector pBBR1p452. The mgdh gene had ninefold higher expression in the overproduction strain compared to the parental strain. Furthermore, membranes from the overexpression strain had a five- and threefold increase of mGDH activity and oxygen consumption rates, respectively. Oxygen consumption rate of the membrane fraction could not be increased by the addition of a substrate combination of glucose and ethanol in the overproduction strain, indicating that the terminal quinol oxidases of the respiratory chain were rate limiting. In contrast, addition of glucose and ethanol to membranes of the control strain increased oxygen consumption rates approaching the observed rates with G. oxydans overproducing mGDH. The higher glucose oxidation rates of the mGDH overproduction strain corresponded to a 70 % increase of the gluconate production rate compared to the control strain. The high rate of glucose oxidation may be useful in the industrial production of gluconates and ketogluconates, or as whole-cell biosensors. Furthermore, mGDH was purified to homogeneity by one-step strep-tactin affinity chromatography and characterized. To our knowledge, this is the first report of a membrane integral quinoprotein being purified by affinity chromatography and serves as a proof-of-principle for using G. oxydans as a host for membrane protein expression and purification.     

Analysis of growth of Gluconobacter oxydans in glucose containing media

Gluconobacter oxydans oxidizes glucose via alternative pathways: one involves the non-phosphorylative, direct oxidation route to gluconic acid and ketogluconic acids, and the second requires an initial phosphorylation and then oxidation via the pentose phosphate pathway enzymes. During growth of G. oxydans in glucose-containing media, the activity of this pathway is strongly influenced by (1) the pH value of the environment and (2) the actual concentration of glucose present in the culture. At pH values below 3.5 the activity of the pentose phosphate pathway was completely inhibited resulting in an increased requirement of the organism for nutrient substances, and a poor cell yield. At pH 5.5 a triphasic growth response was observed when G. oxydans was grown in a defined medium. Above a threshold value of 5–15 mM glucose, oxidation of both glucose and gluconate by the pentose phosphate pathway enzymes was repressed, causing a rapid accumulation of gluconic acid in the culture medium. When growing under these conditions, a low affinity for the oxidation of glucose was found (K _s=13 mM). Below this threshold glucose concentration, pentose phosphate pathway enzymes were synthesized and glucose was actively assimilated via this pathway. It was shown that de novo enzyme synthesis was necessary for increased pentose phosphate pathway activity and that assimilation of gluconate by washed cell suspensions was inhibited by glucose.