Study of the inhibitory effect of the product dihydroxyacetone on Gluconobacter oxydans in a semi-continuous two-stage repeated-fed-batch process

The influence of the product inhibition by dihydroxyacetone (DHA) on Gluconobacter oxydans for a novel semi-continuous two-stage repeated-fed-batch process was examined quantitatively. It was shown that the culture was able to grow up to a DHA concentration of 80 kg m⁻³ without any influence of product inhibition. The regeneration capability of the reversibly product inhibited culture from a laboratory-scale bioreactor system was observed up to a DHA concentration of about 160 kg m⁻³. At higher DHA concentrations, the culture was irreversibly product inhibited. However, due to the robust membrane-bound glycerol dehydrogenase of G. oxydans, product formation was still active for a prolonged period of time. The reachable maximum final DHA concentration was as high as 220 kg m⁻³. The lag phases for growth increased exponentially with increasing DHA threshold values of the first reactor stage. These results correlated well with fluorescence in situ hybridization (FISH) measurements confirming that the number of active cells decreased exponentially with increasing DHA concentrations.     

Optimization of the microbial synthesis of dihydroxyacetone from glycerol with <Emphasis Type="Italic">Gluconobacter oxydans</Emphasis>

An optimized repeated-fed-batch fermentation process for the synthesis of dihydroxyacetone (DHA) from glycerol utilizing Gluconobacter oxydans is presented. Cleaning, sterilization, and inoculation procedures could be reduced significantly compared to the conventional fed-batch process. A stringent requirement was that the product concentration was kept below a critical threshold level at all times in order to avoid irreversible product inhibition of the cells. On the basis of experimentally validated model calculations, a threshold value of about 60 kg m^-3 DHA was obtained. The innovative bioreactor system consisted of a stirred tank reactor combined with a packed trickle-bed column. In the packed column, active cells could be retained by in situ immobilization on a hydrophilized Ralu-ring carrier material. Within 17 days, the productivity of the process could be increased by 75% to about 2.8 kg m^-3 h^-1. However, it was observed that the maximum achievable productivity had not been reached yet.Abbreviations K _O Monod half saturation constant of dissolved oxygen (kg m^-3) - K _S Monod half saturation constant of substrate glycerol (kg m^-3) - O Dissolved oxygen concentration (kg m^-3) - P Product concentration (kg m^-3) - P _crit Critical product concentration constant (kg m^-3) - S Substrate concentration (kg m^-3) - t Time (s) - X Biomass concentration (dry weight) (kg m^-3) - Y _P/S Yield coefficient of product from substrate - Y _X/S Yield coefficient of biomass from substrate - Growth dependent specific production rate constant (kg m^-3) - Growth independent specific production rate constant (s^-1) - Specific growth rate (s^-1) - _max Maximum specific growth rate constant (s^-1)     

Use of glycerol for producing 1,3-dihydroxyacetone by Gluconobacter oxydans in an airlift bioreactor

1,3-Dihydroxyacetone can be produced by biotransformation of glycerol with glycerol dehydrogenase from Gluconobacter oxydans cells. Firstly, improvement the activity of glycerol dehydrogenase was carried out by medium optimization. The optimal medium for cell cultivation was composed of 5.6 g/l yeast extract, 4.7 g/l glycerol, 42.1 g/l mannitol, 0.5 g/l K₂HPO₄, 0.5 g/l KH₂PO₄, 0.1 g/l MgSO₄·7H₂O, and 2.0 g/l CaCO₃ with the initial pH of 4.9. Secondly, an internal loop airlift bioreactor was applied for DHA production from glycerol by resting cells of G. oxydans ZJB09113. Furthermore, the effects of pH, aeration rate and cell content on DHA production and glycerol feeding strategy were investigated. 156.3 ± 7.8 g/l of maximal DHA concentration with 89.8 ± 2.4% of conversion rate of glycerol to DHA was achieved after 72 h of biotransformation using 10 g/l resting cells at 30 °C, pH 5.0 and 1.5 vvm of aeration rate.     

Glycerol and dihydroxyacetone metabolizing enzymes in fission yeasts of the genus Schizosaccharomyces

The only species of fission yeasts capable of growing on glycerol or dihydroxyacetone were Schizosaccharomyces pombe and S. malidevorans. When growing on glycerol or grown on glucose until it was exhausted, these species contained glycerol:NAD⁺ 2-oxidoreductase and dihydroxyacetone kinase but no glycerol kinase, consistent with utilization of glycerol via dihydroxyacetone. When grown to exhaustion of glucose, S. octosporus, S. slooffiae and S. japonicus contained dihydroxyacetone kinase but no glycerol:NAD⁺ 2-oxidoreductase or glycerol kinase. Prior to exhaustion of glucose in the medium, all species contained dihydroxyacetone kinase, all species except S. japonicus contained glycerol:NADP⁺ 2-oxidoreductase, and only S. pombe and S. malidevorans contained glycerol:NAD⁺ 2-oxidoreductase. Possible roles for the glycerol:NAD⁺ 2-oxidoreductase, glycerol:NADP⁺ 2-oxidoreductase and dihydroxyacetone kinase in metabolism of glycerol and dihydroxyacetone are discussed.Non-standard abbreviations DHA dihydroxyacetone - DHAK dihydroxyacetone kinase - DHAP dihydroxyacetone phosphate - GK glycerol kinase - G2DH-NAD glycerol - NAD⁺ 2-oxidoreductase - G2DH-NADP glycerol - NADP⁺ 2-oxidoreductase - MEA malt extract agar - YEP yeast extract phosphate medium     

Biochemical and structural analysis of Gox2181, a new member of the SDR superfamily from Gluconobacter oxydans

Gluconobacter oxydans enable to oxidize sugars and polyols incompletely to corresponding materials with potential industrial applications, containing around 75 putative dehydrogenases. One of these putative dehydrogenases, Gox2181, was cloned and expressed in Escherichia coli BL21 (DE3), and its X-ray crystal structure was determined to a resolution of 1.8 Å. Gox2181 formed a homo-tetramer in the crystal that was coincident with the apparent molecular mass determined in the solution. Gox2181 displayed α/β-folding patterns, the conserved catalytic tetrad of Asn119-Ser147-Tyr162-Lys166, and the NAD-binding pocket, which aligned well with the ‘classical’ type of short-chain dehydrogenase/reductase (SDR) enzymes. Gox2181 was denoted SDR51C based on the SDR nomenclature system. The purified recombinant Gox2181 was demonstrated to be NAD(H)-dependent and active towards a wide range of substrates, including sugar alcohols, secondary alcohols, ketones, and ketoses. Among the substrates tested, Gox2181 displayed preference for secondary hydroxyl or carbonyl groups, showing low K_m values with d-arabitol and butanedione.     

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.     

A metabolic study of the regulation of proteolysis by sugars in maize root tips: effects of glycerol and dihydroxyacetone

Sugars, the main growth substrates of plants, act as physiological signals in the complex regulatory network of sugar metabolism. To investigate the function of different glycolytic steps in sugar sensing and signaling we compared the effects of carbon starvation with those of glucose, glycerol and dihydroxyacetone on carbon metabolism, proteolysis, and protease expression in excised maize (Zea mays L.) root tips. Respiration, soluble proteins, protein turnover and proteolytic activities were monitored as a function of time, along with in vitro and in vivo analysis of a variety of metabolites (sugars, amino and organic acids, phosphoesters, adenine nucleotides...) using ¹³C, ³¹P and ¹H NMR spectroscopy. Our results indicate that, in maize root tips, endopeptidase activities and protease expression are induced in response to a decrease in carbon supply to the upper part of the glycolytic pathway, i.e. at the hexokinase step. Proteolysis would be controlled downstream glycolysis, probably at the level of the respiratory substrate supply to mitochondria. Electronic Supplementary Material Supplementary material is available in the online version of this article at and is accessible for authorized users.     

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.     

A single amino acid substitution changes the substrate specificity of quinoprotein glucose dehydrogenase in Gluconobacter oxydans.

Summary Gluconobacter oxydans contains pyrroloquinoline quinone-dependent glucose dehydrogenase (GDH). Two isogenic G. oxydans strains, P1 and P2, which differ in their substrate specificity with respect to oxidation of sugars have been analysed. P1 can oxidize only d-glucose, whereas P2 is also capable of the oxidation of the disaccharide maltose. To investigate the nature of this maltose-oxidizing property we cloned the gene encoding GDH from P2. Expression of P2 gdh in P1 enables the latter strain to oxidize maltose, indicating that a mutation in the P2 gdh gene is responsible for the change in substrate specificity. This mutation could be ascribed to a 1 by substitution resulting in the replacement of His 787 by Asn.     

Overflow metabolism during anaerobic growth of Klebsiella aerogenes NCTC 418 on glycerol and dihydroxyacetone in chemostat culture

Klebsiella aerogenes NCTC 418 was grown anaerobically in chemostat culture with glycerol as source of carbon and energy. Glycerol-limited cultures did not ferment the carbon source with maximal efficiency but produced considerable amounts of 1,3-propanediol. The fraction of glycerol converted to this product depended on the growth rate and on the limitation: faster growing cells produced relatively more of this compound. Under glycerol excess conditions the energetic efficiency of fermentation was decreased due to the high 1,3-propanediol excretion rate. Evidence is presented that 1,3-propanediol accumulation exerts a profound effect on the cells' metabolic behaviour.When steady state glycerol-limited cultures were instantaneously relieved of the growth limitation a vastly enhanced glycerol uptake rate was observed, accompanied by a shift in the fermentation pattern towards 1,3-propanediol and acetate. This observation was consistent with the extremely high glycerol dehydrogenase activity that was measured in vitro. Some mechanisms that could be responsible for the energy dissipation during this response are discussed.     

<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.     

Catalytic and biocatalytic oxidation of glucose to gluconic acid in a modified three-phase reactor

A comparative study of catalytic and biocatalytic glucose oxidation was carried out. Gluconobacter oxydans NBIMCC 1043 strain was used for biocatalytic glucose conversion. In the case of cell recycle coupled with cross-flow microfiltration the productivity and biomass concentration reached 40% and 3 g l^–1 respectively, in comparison to those of batch fermentation (21% and 2.3 g l^–1, respectively).     

Regulation of gluconate and ketogluconate production in Gluconobacter oxydans ATCC 621-H

Gluconobacter spp. possess the enzymic potential for two pathways of direct glucose oxidation. It has been proposed that the major part of glucose is oxidized to gluconate via NADP-dependent glucose dehydrogenase and that reoxidation of NADPH under these conditions proceeds via recycling of gluconate through ketogluconates. This hypothesis was tested in experiments in which Gluconobacter oxydans ATCC 621-H was grown in glucose-yeast extract medium containing [¹⁴C]2-ketogluconate. As expected, glucose was almost quantitatively oxidized to gluconate, without further accumulation of 2- and 5-ketogluconate. Interestingly, the total amount of neither [¹⁴C]2-ketogluconate nor [¹⁴C]gluconate did change significantly during this oxidation phase, indicating that recycling of gluconate through ketogluconates did not occur. An analysis of enzyme activities in cell-free extracts of glucose-grown cells of G. oxydans ATCC 621-H showed that the membrane-bound glucose dehydrogenase was far more active than the NADP-linked glucose dehydrogenase. The activity of the latter enzyme constituted only 10–15% of that of quinoprotein glucose dehydrogenase and was far too low to match the in vivo rates of gluconate production in batch cultures of G. oxydans. It is concluded that under these conditions glucose is mainly oxidized to gluconate via the membrane-bound glucose dehydrogenase. Implications of these results for the regulation of ketogluconate formation are discussed.Abbreviations DCPIP 2,6-dichlorophenolindophenol - PMS phenazine methosulphate - PQQ pyrrolo-quinoline quinone     

Glycerol and dihydroxyacetone dissimilation in Desulfovibrio strains

During growth on glycerol two marine Desulfovibrio strains that can grow on an unusually broad range of substrates contained high activities of glycerol kinase, NAD(P)-independent glycerol 3-phosphate dehydrogenase and the other enzymes necessary for the conversion of dihydroxyacetone phosphate to pyruvate. Glycerol dehydrogenase and a specific dihydroxyacetone kinase were absent. During growth on dihydroxyacetone, glycerol kinase is involved in the initial conversion of this compound to dihydroxyacetone phosphate which is then further metabolized. Some kinetic properties of the partially purified glycerol kinase were determined. The role of NAD as electron carrier in the energy metabolism during growth of these strains on glycerol and dihydroxyacetone is discussed.Glycerol also supported growth of three out of four classical Desulfovibrio strains tested. D. vulgaris strain Hildenborough grew slowly on glycerol and contained glycerol kinase, glycerol 3-phosphate dehydrogenase and enzymes for the dissimilation of dihydroxyacetone phosphate. In D. gigas which did not grow on glycerol the enzymes glycerol kinase and glycerol 3-phosphate dehydrogenase were absent in lactate-grown cells.Abbreviations DHA dihydroxyacetone - DHAP dihydroxyacetone phosphate - G3P glycerol 3-phosphate - GAP glyceraldehyde 3-phosphate - 3-PGA 3-phosphoglycerate - 2-PGA 2-phosphoglycerate - 2,3-DPGA 2,3-diphosphoglycerate - PEP phosphoenolpyruvate - DH dehydrogenase - GK glycerol kinase - DHAK dihydroxyacetone kinase - TIM triosephosphate isomerase - PGK 3-phosphoglycerate kinase - PK pyruvate kinase - LDH lactate dehydrogenase - DTT dithiotreitol - HEPES 4-(2-hydroxyethyl)-1-piperazine ethane sulfonic acid - PIPES piperazine-1,1-bis(2-ethane sulfonic acid) - BV²⁺/BV⁺ oxidized/reduced benzylviologen - PMS phenazine methosulfate - DCPIP 2,6-dichlorophenolindophenol - MTT 3-(4,5-dimethylthiazol-2-yl)-2,4-diphenyltetrazolium bromide     

Coupling of permeabilized cells of Gluconobacter oxydans and Ralstonia eutropha for asymmetric ketone reduction using H2 as reductant

A combined two-cell reaction system containing Gluconobacter oxydans and Ralstonia eutropha was evaluated with regard to asymmetric ketone reduction using H₂ as the reductant. Whole cells permeabilized by EDTA/toluene were used, and synthesis was performed in a biphasic aqueous/organic reaction medium. The two-cell system was compared with a system in which G. oxydans alone was used for both ketone reduction and cofactor regeneration, using an alcohol as co-substrate. The two-cell system exhibited almost twice the initial reaction rate of the single-cell system, a higher yield (75% vs. 48%) but slightly lower enantiomeric purity (93% vs. 98%) of the product (S)-2-octanol. The permeabilized R. eutropha cells are worth evaluating for byproduct-free NADH regeneration in combination with other whole cell catalysts.     

A pyrroloquinoline quinine-dependent membrane-bound d-sorbitol dehydrogenase from Gluconobacter oxydans exhibits an ordered Bi Bi reaction mechanism

A membrane-bound pyrroloquinoline quinine (PQQ)-dependent d-sorbitol dehydrogenase (mSLDH) in Gluconobacter oxydans participates in the oxidation of d-sorbitol to l-sorbose by transferring electrons to ubiquinone which links to the respiratory chain. To elucidate the kinetic mechanism, the enzyme purified was subjected to two-substrate steady-state kinetic analysis, product and substrate inhibition studies. These kinetic data indicate that the catalytic reaction follows an ordered Bi Bi mechanism, where the substrates bind to the enzyme in a defined order (first ubiquinone followed by d-sorbitol), while products are released in sequence (first l-sorbose followed by ubiquinol). From these findings, we proposed that the native mSLDH bears two different substrate-binding sites, one for ubiquinone and the other for d-sorbitol, in addition to PQQ-binding and Mg²⁺-binding sites in the catalytic center.     

Glycerol metabolism in the methylotrophic yeast Hansenula polymorpha: phosphorylation as the initial step

In hansenula polymorpha glycerol is metabolized via glycerol kinase and NAD(P)-independent glycerol-3-phosphate (G3P) dehydrogenase, enzymes which hitherto were reported to be absent in this methylotrophic yeast. Activity of glycerol kinase was readily detectable when cell-free extracts were incubated at pH 7–8 with glycerol/ATP/Mg²⁺ and a discontinuous assay for G3P formation was used. This glycerol kinase activity could be separated from dihydroxyacetone (DHA) kinase activity by ion exchange chromatography. Glycerol kinase showed relatively low affinities for glycerol (apparent K _m=1.0 mM) and ATP (apparent K _m=0.5 mM) and was not active with other substrates tested. No inhibition by fructose-1,6-bisphosphate (FBP) was observed. Both NAD-dependent and NAD(P)-independent G3P dehydrogenases were present. The latter enzyme could be assayed with PMS/MTT and cosedimented with the mitochondrial fraction. Glucose partly repressed synthesis of glycerol kinase and NAD(P)-independent G3P dehydrogenase, but compared to several other non-repressing carbon sources no clear induction of these enzymes by glycerol was apparent. Amongst glycerolnegative mutants of H. polymorpha strain 17B (a DHA kinase-negative mutant), strains blocked in either glycerol kinase or membrane-bound G3P dehydrogenase were identified. Crosses between representatives of the latter mutants and wild type resulted in the isolation of, amongst others, segregants which had regained DHA kinase but were still blocked in the membrane-bound G3P dehydrogenase. These strains, employing the oxidative pathway, were only able to grow very slowly in glycerol mineral medium.Abbreviations DHA dihydroxyacetone - G3P glycerol-3-phosphate - EMS ethyl methanesulphonate - MTT 3-(4,5-dimethyl-thiazolyl-2)-2,5-diphenyl tetrazolium bromide - PMS phenazine methosulphate - FBP fructose-1,6-bisphosphate     

普通生酮基古龙酸菌中山梨糖脱氢酶和山梨酮脱氢酶的纯化及酶学性质分析

【目的】对源于普通生酮基古龙酸菌(Ketogulonicigenium vulgare WSH-001)的山梨糖脱氢酶(Sorbose dehydrogenase,SDH)和山梨酮脱氢酶(Sorbosone dehydrogenase,SNDH)的酶学性质进行分析。【方法】以K.vulgare WSH-001基因组DNA为模板,PCR扩增得到山梨糖脱氢酶基因(sdh)和山梨酮脱氢酶基因(sndh),构建重组表达质粒p ET28a-sdh、p ET28a-sndh,并分别转入大肠杆菌BL21(DE3)中。利用镍柱亲和层析和凝胶过滤层析得到纯化的SDH和SNDH。【结果】成功构建产SDH和SNDH的大肠杆菌BL21(DE3)并对目的酶进行纯化。SDS-PAGE分析结果表明,SDH和SNDH的大小分别为64 k Da和48 k Da,与理论预测值一致。显色法测得SDH酶活为3.15 U/mg,最适反应温度为30°C,最适反应pH为8.0左右;SNDH酶活为6.12 U/mg,最适反应温度为35°C,最适反应pH为8.0左右。在pH 3.0、4.0、5.0的偏酸性条件下,2个酶的酶活受到显著影响。【结论】表达并纯化了来源于普通生酮基古龙酸菌来源的SDH、SNDH,并进行了酶学性质分析,为利用SDH、SNDH实现维生素C前体2-酮基-L-古龙酸的一步法发酵生产提供了必要的参考。     

Conversion of puerarin into its 7-O-glycoside derivatives by Microbacterium oxydans (CGMCC 1788) to improve its water solubility and pharmacokinetic properties

Microbacterium oxydans strain NJ 6 isolated from soil samples converted puerarin into two novel compounds, puerarin-7-O-glucoside and puerarin-7-O-isomaltoside, via an unreported O-glycosylation of the phenolic hydroxyl group at the 7-position of puerarin. Sucrose, maltotriose, and maltose could be used as glucosyl donors for glycosylation of puerarin, but uridine-diphosphate glucose, glucose, fructose, lactose, cyclodextrin, and starch could not. Regardless of the position of B-ring in the (iso)flavonoids core structure, the glycosylation of the phenolic hydroxyl group at the 7-position of (iso)flavonoids was governed by the presence or absence of a glucosyl residue at 8-C. The apparent solubility of puerarin-7-O-glucoside and puerarin-7-O-isomaltoside was approximately 18 and 100 times that of natural puerarin, respectively. Like parent puerarin, puerarin-7-O-glucoside maintained its physiological ability to relax the contractions of isolated rat thoracic aortic rings in vitro induced by phenylephrine. However, puerarin-7-O-glucoside was able to maintain higher plasma concentrations and have a longer mean residence time in the blood than the parent puerarin.