Influence of constant and oscillating dissolved oxygen concentrations on keto acid production by Gluconobacter oxydans subsps. melanogenum.

Gluconobacter species are known to oxidise glucose via a direct oxidation pathway which is distinct from the pentose phosphate pathway. In the present communication results of an investigation on the influence of different dissolved oxygen concentrations (DO) on the production of 2,5-diketogluconic acid in batch and chemostat cultures are given. DO of 30% relative to air at 1 bar was found as a threshold level for optimum productivity. The positive influence of continuous availability of dissolved oxygen on the process of rapid glucose oxidation was unambiguously shown as the result of induction of membrane bound dehydrogenases involved in direct glucose oxidation. Furthermore data of scale-down experiments in which the organism was cultivated under oscillations of dissolved oxygen, are given. The influences of such oscillations of DO in the region of the established threshold (30% saturation) were found to result in a prolonged lag phase for growth and product formation. The data obtained in this study revealed critical residence times at low DO that could be employed as a criterion for scale up of this aerobic process.     

Inhibitory effects of glycerol on Gluconobacter oxydans

Summary The inhibitory effects of glycerol on Gluconobacter oxydans were measured separately. The kinetics of oxygen uptake rate representing the DHA production, the CO₂ evolution rate representing the assimilation of the product, and the specific growth rate were mathematically modelled. Glycerol does not inhibit DHA formation and CO₂-evolution.now: Institut für Biotechnologie, TU Graz, Petersgasse 12, 8010 Graz, Austria     

Biotransformation of patulin by Gluconobacter oxydans

A bacterium isolated from patulin-contaminated apples was capable of degrading patulin to a less-toxic compound, ascladiol. The bacterium was identified as Gluconobacter oxydans by 16S rRNA gene sequencing, whereas ascladiol was identified by liquid chromatography-tandem mass spectrometry and proton and carbon nuclear magnetic resonance. Degradation of up to 96% of patulin was observed in apple juices containing up to 800 microg/ml of patulin and incubated with G. oxydans.     

Oxidative d-xylose metabolism of Gluconobacter oxydans

Summary Gluconobacter oxydans subsp. suboxydans ATCC 621 oxidizes d-xylose to xylonic acid very efficiently, although it cannot grow on xylose as sole carbon source. The oxidation of xylose was found to be catalyzed by a membrane-bound xylose dehydrogenase. The xylono--lactone formed in the oxidation reaction is subsequently hydrolyzed to xylonic acid by a -lactonase. The complete oxidation pathway of d-xylose in G. oxydans is evidently located in the periplasmic space.     

Biotransformation of Patulin by Gluconobacter oxydans

A bacterium isolated from patulin-contaminated apples was capable of degrading patulin to a less-toxic compound, ascladiol. The bacterium was identified as Gluconobacter oxydans by 16S rRNA gene sequencing, whereas ascladiol was identified by liquid chromatography-tandem mass spectrometry and proton and carbon nuclear magnetic resonance. Degradation of up to 96% of patulin was observed in apple juices containing up to 800 μg/ml of patulin and incubated with G. oxydans.     

Influence of dissolved oxygen concentration on the biosynthesis of cephalosporin C.

Cephalosporin C was produced by a highly productive strain of Cephalosporium acremonium under industrial production conditions by fed-batch cultivation in a 40-l stirred-tank reactor using a complex medium containing 50 g l-1 peanut flour. The influence of dissolved oxygen concentration (pO2, DOC), which was maintained at different constant levels between 5 and 40% of its saturation value, during the production phase by means of a parameter-adaptive pO2-controller, on the cephalosporin C biosynthesis, was investigated. The concentrations of cephalosporin C (CPC) and its precursors penicillin N (PEN N), deacetoxycephalosporin C (DAOC), and deacetylcephalosporin C (DAC) were monitored by on-line HPLC. The concentrations of amino acids, valine (VAL), cysteine (CYS), alpha-amino-adipic acid (alpha-AAA), the dipeptide alpha-amino-adipyl-cysteine (AC), and the tripeptide alpha-amino-adipyl-cysteinyl-valine (ACV) were determined by off-line HPLC. By reducing the pO2 in the production phase from 40 to 5% of its saturation value, the CPC concentration diminished from 7.2 to 1.1 g l-1 and the PEN N concentration increased from 2.57 to 7.65 g l-1. The DAC concentration also dropped from 3.13 to 0.42 g l-1; however, the DAOC concentration was less influenced. The concentrations of AC and ACV were also less affected. The small DOC did not lead to an accumulation of the intermediate AC and ACV during the production phase. With increasing DOC in the range of 5-20%, the maximal specific production rate, the cell mass concentration-based and the substrate-based yield coefficients for CPC increased almost linearly, and fell back for PEN N.(ABSTRACT TRUNCATED AT 250 WORDS)     

Dextran dextrinase and dextran of Gluconobacter oxydans

Certain strains of Gluconobacter oxydans have been known since the 1940s to produce the enzyme dextran dextrinase (DDase; EC2.4.1.2)—a transglucosidase converting maltodextrins into (oligo)dextran. The enzyme catalyses the transfer of an α1,4 linked glucosyl unit from a donor to an acceptor molecule, forming an α1,6 linkage: consecutive glucosyl transfers result in the formation of high molecular weight dextran from maltodextrins. In the early 1990s, the group of K. Yamamoto in Japan revived research on DDase, focussing on the purification and characterisation of the intracellular DDase produced by G. oxydans ATCC 11894. More recently, this was taken further by Y. Suzuki and coworkers, who investigated the properties and kinetics of the extracellular DDase formed by the same strain. Our group further elaborated on fermentation processes to optimise DDase production and dextran formation, DDase characterisation and its use as a biocatalyst, and the physiological link between intracellular and extracellular DDase. Here, we present a condensed overview of the current scientific status and the application potential of G. oxydans DDase and its products, (oligo)dextrans. The production of DDase as well as of dextran is first described via optimised fermentation processes. Specific assays for measuring DDase activity are also outlined. The general characteristics, substrate specificity, and mode of action of DDase as a transglucosidase are described in detail. Two forms of DDase are produced by G. oxydans depending on nutritional fermentation conditions: an intracellular and an extracellular form. The relationship between the two enzyme forms is also discussed. Furthermore, applications of DDase, e.g. production of (oligo)dextran, transglucosylated products and speciality oligosaccharides, are summarized.     

Influence of dissolved oxygen on the nitrification kinetics in a circulating bed biofilm reactor

The influence of dissolved oxygen concentration on the nitrification kinetics was studied in the circulating bed reactor (CBR). The study was partly performed at laboratory scale with synthetic water, and partly at pilot scale with secondary effluent as feed water. The nitrification kinetics of the laboratory CBR as a function of the oxygen concentration can be described according to the half order and zero order rate equations of the diffusion-reaction model applied to porous catalysts. When oxygen was the rate limiting substrate, the nitrification rate was close to a half order function of the oxygen concentration. The average oxygen diffusion coefficient estimated by fitting the diffusion-reaction model to the experimental results was around 66% of the respective value in water. The experimental results showed that either the ammonia or the oxygen concentration could be limiting for the nitrification kinetics. The latter occurred for an oxygen to ammonia concentration ratio below 1.5–2 gO₂/gN-NH₄ ⁺ for both laboratory and pilot scale reactors. The volumetric oxygen mass transfer coefficient (k _L a) determined in the laboratory scale reactor was 0.017?s^?1 for a superficial air velocity of 0.02?m s^?1, and the one determined in the pilot scale reactor was 0.040?s^?1 for a superficial air velocity of 0.031?m?s^?1. The k _L a for the pilot scale reactor did not change significantly after biofilm development, compared to the value measured without biofilm.     

Hydrogen peroxide as an oxygen source for immobilized Gluconobacter oxydans converting glycerol to dihydroxyacetone

Summary A flow injection analysis (FIA) system with amperometric detection was developed for measuring hydrogen peroxide which was used as an oxygen source for immobilized cells. A constant concentration of peroxide in the reactor was maintained by processing the analytical signal in a computer programmed as a PI-regulator. The concentration of dissolved oxygen was followed using a commercial Clark-electrode. The simultaneous measurements of hydrogen peroxide and dissolved oxygen are discussed with respect to process control.Conversion of glycerol to dihydroxyacetone by Gluconobacter oxydans immobilized in calcium alginate was used as a model system.Initial specific productivity increased with increasing hydrogen peroxide concentration. However, decreases in viable counts, enzymatic activities and overall productivities were noted. Various techniques for improving operational stability are discussed.     

Kinetics of polyol oxidation with Gluconobacter oxydans

Summary The influence of culture pH on the metabolism of Gluconobacter oxydans was determined. An acidic milieu during growth of the organism enhances the oxidation rate. The CO₂ evolution rate representing the assimilation of the product is inhibited by a low pH value. Growth of the bacteria is possible both on glycerol and DHA in separate phases, which is not a controlled as diauxic growth. Product formation follows Luedeking-Piret kinetics.now: Institut für Biotechnologie, TU Graz, Petersgasse 12, 8010 Graz, Austria     

Genetic heterogeneity among keto-acid-producing strains of Gluconobacter oxydans

The genomes of four keto-acid-producing Gluconobacter oxydans strains (ATCC9937, IFO3293, IFO12258 and DSM2343) were analysed by pulse-field gel electrophoresis (PFGE). PFGE of undigested DNA allowed the detection of plasmids in the following strains: ATCC9937 (3 plasmids; 8, 27, 31 kb), IFO3293 (9 kb), DSM2343 (21 kb). The three plasmids in ATCC9937 showed no homology to each other or to plasmids in the other strains. Seventeen restriction enzymes were tested for use in PFGE analysis of the G. oxydans strains and XbaI was chosen for restriction fragment analysis of the genomes. Fairly good resolution of restriction fragments at all size ranges was achieved by using three different pulse–time programs. The genome sizes of the four strains were estimated to be between 2240 kb and 3787 kb. The XbaI restriction patterns of the four strains showed no similarities to each other. Ten random cosmid clones of ATCC9937 were used as hybridization probes against the four strains, but, with the exception of one clone, hybridization signals were only observed with ATCC9937 itself. These data show that the four strains are not closely related.     

氧化葡萄糖酸杆菌酶学和分子生物学研究

对氧化葡萄糖酸杆菌初级代谢途径中的关键酶及分子生物学研究做了系统的评述 ,展望了分子技术改造氧化葡萄糖酸杆菌和优化 2 KGA代谢途径的可能。     

基于重组氧化葡萄糖酸杆菌生物合成吡咯喹啉醌

吡咯喹啉醌(Pyrroloquinoline quinone,PQQ)是一种重要的氧化还原酶辅基,具有多种生理生化功能,在食品、医药卫生及农业等领域具有广泛的应用。文中采用重组氧化葡萄糖酸杆菌生物合成吡咯喹啉醌。首先构建丙酮酸脱羧酶基因GOX1081敲除的重组菌G. oxydans T1,减少副产物乙酸的形成。然后利用筛选的内源性组成型启动子P0169融合表达pqqABCDE基因簇及tldD基因,构建重组菌G. oxydans T2。最后对发酵培养基添加物和发酵条件进行优化。结果显示重组菌G. oxydans T1、G. oxydans T2生物量较野生菌分别提高43.02%和38.76%,而PQQ的产量分别是野生菌的4.82倍和20.5倍。进一步优化G. oxydans T2碳源及培养条件,最终PQQ产量达(51.3241±0.8997)mg/L,是野生菌的345.62倍。通过基因工程手段,可以有效提高氧化葡萄糖酸杆菌的生物量和合成PQQ的产量,为改善PQQ生物合成效率奠定基础。     

Influence of dissolved oxygen concentration and shear rate on the production of pullulan byAureobasidium pullulans

Summary Experiments were carried out withA. pullulans (ATCC 9348) at constant dissolved oxygen concentration (DO=100 and 50% related to air saturation at 1 bar) and at constant stirrer speeds (n=500 and 150 [min^–1]). The highest pullulan yield was achieved at decreased constant DO in connection with decreased shear rate. Biomass production was not affected.     

Effect of dissolved oxygen concentration on sludge settleability

This laboratory study presents a detailed evaluation of the effects of dissolved oxygen concentration and accumulation of storage polymers on sludge settleability in activated sludge systems with an aerobic selector. The oxygen and substrate availability regime were simulated in laboratory sequencing batch reactor systems. The experiments showed that low dissolved oxygen concentration (1.1 mg O₂ l^–1) had a strong negative effect on sludge settleability, leading to the proliferation of filamentous bacteria (Thiothrix spp., Type 021N and Type 1851). This negative effect was stronger at high chemical oxygen demand loading rate. This indicates that a compartmentalised (plug flow) aerobic contact tank, designed at short hydraulic residence time to guarantee a strong substrate gradient, with low dissolved oxygen concentration, might be worse for sludge settleability than an "overdesigned" completely mixed contact tank. Contrary to the general hypothesis, the maximum specific acetate uptake rate, poly--hydroxybutyrate production rate, and resistance to short starvation periods are similar in both poor- and well-settling sludge. The results of this study support our previous hypothesis on the importance of substrate gradients for the development of filamentous structures in biological flocs, from soluble organic substrate gradients to dissolved oxygen gradients in sludge flocs.     

Incapability of Gluconobacter oxydans to produce tartaric acid

The dependence of tartaric acid production by Gluconobacter oxydans ssp. oxydans ATCC 19357 and G. oxydans ssp. suboxydans ATCC 621 on vanadate was investigated. It was found with both organisms that trataric acid could only be produced in a medium containing vanadate (NH(4)VO(3)). A proposed intermediate of the tartaric acid metabolism in G. oxydans, 5-ketogluconic acid, was tested on its reactivity in the presence of the oxidizing catalyst vanadate. It could be shown that 5-ketogluconic acid and the catalyst vanadate, but not the activity of G. oxydans, were responsible for the formation of tartaric acid. G. oxydans was not able to produce tartaric acid by itself. The stereochemical identity of the formed tartaric acid could be identified as the L-(+)-type. Oxalic acid was formed from 5-ketogluconic acid with vanadate in the absence and in the presence of G. oxydans. The ratio of oxalic acid to tartaric acid was 1:1.     

Characterization of Gluconobacter oxydans immobilized in calcium alginate

Summary Gluconobacter oxydans cells were immobilized in calcium alginate and the preparation was used for the oxidation of glycerol to dihydroxyacetone. The characterization was done according to the guidelines given by the Working Party on Immobilized Biocatalysts of the European Federation of Biotechnology. The pH optimum of the preparation was found to be 5.0 and the temperature optimum was 40°C. However, the operational stability was better at 30°C. The glycerol concentration required to obtain half the maximal reaction rate was about 5 mM for both immobilized and free cells. At low concentrations of glycerol and high concentrations of dihydroxyacetone a slight inhibition was noted. No loss of activity of the immobilized preparation was observed after storage for 68 days at +4°C. Investigation of the operational stability revealed a half-life of 5 days. Studies of the influence of particle size and cell densities as well as that of oxygen concentration revealed that the oxygen supply was the rate limiting step.     

氧化葡萄糖酸杆菌SCB329的培养及保存

氧化葡萄糖酸杆菌SCB329和苏云金芽孢杆菌SCB933是混合发酵产生维生素C前体2－KLG两株主要菌种,本文对氧化葡萄糖酸杆菌SCB329的纯培养,传代及纯小菌的保存及其对产酸的影响作了研究。     

Analysis of aldehyde reductases from Gluconobacter oxydans 621H

Two cytosolic nicotinamide adenine dinucleotide phosphate-dependent aldehyde reductases, Gox1899 and Gox2253, from Gluconobacter oxydans 621H were overproduced and purified from Escherichia coli. The purified proteins exhibited subunit masses of 26.4 (Gox1899) and 36.7 kDa (Gox2253). Both proteins formed homo-octamers exhibiting native masses of 210 and 280 kDa, respectively. The substrate spectra, optimal reaction conditions, and kinetic constants were determined for Gox1899 and Gox2253. Both enzymes efficiently catalyzed the reduction of medium/long-chain aldehydes. However, Gox1899 had a wider substrate spectrum and was more catalytically efficient. The best activity with Gox1899 was found for aliphatic aldehydes of C6-C10. In contrast, Gox2253 had a limited substrate spectrum and reduced octanal, nonanal, and decanal. Both enzymes were unable to oxidize primary alcohols. Aldehyde removal may be of particular importance for Gluconobacter because the membrane-bound alcohol dehydrogenase rapidly oxidizes short to long-chain alcohols, and large quantities of aldehydes could enter the cell, making detoxification necessary.     

Asymmetric reduction of diketones by two Gluconobacter oxydans oxidoreductases

Two genes encoding recombinant cytosolic oxidoreductases from Gluconobacter oxydans, gox0313 and gox0646, were heterologously expressed in Escherichia coli and the resulting proteins were purified and characterized. GOX0313 was identified as a medium-chain alcohol dehydrogenase, whereas GOX0646 was classified as a ketocarbonyl reductase. GOX0313 had a broad substrate spectrum and oxidized various primary alcohols. However, GOX0313 had a preference for substrate reduction, reducing many aldehydes and α-diketones. In contrast, GOX0646 had a narrow substrate spectrum and reduced α-diketones, preferring short-chain ketocarbonyls. Both enzymes regio- and stereospecifically reduced α-diketones to the corresponding (S)-hydroxy ketone, as shown by NMR. These products are difficult to produce chemically, requiring complicated protecting group chemistry. Furthermore, hydroxy ketones find industrial application in the production of pheromones, fragrances, flavors, and pharmaceuticals. Hence, these enzymes are interesting biocatalysts for the production of enantiomerically pure building blocks that are difficult to prepare chemically.