Yoshitaka Ano

5-Keto-d-Gluconate Production Is Catalyzed by a Quinoprotein Glycerol Dehydrogenase, Major Polyol Dehydrogenase, in Gluconobacter Species

ABSTRACT Acetic acid bacteria, especially Gluconobacter species, have been known to catalyze the extensive oxidation of sugar alcohols (polyols) such as d-mannitol, glycerol, d-sorbitol, and so on. Gluconobacter species also oxidize sugars and sugar acids and uniquely accumulate two different keto-d-gluconates, 2-keto-d-gluconate and 5-keto-d-gluconate, in the culture medium by the oxidation of d-gluconate. However, there are still many controversies regarding their enzyme systems, especially on d-sorbitol and also d-gluconate oxidations. Recently, pyrroloquinoline quinone-dependent quinoprotein d-arabitol dehydrogenase and d-sorbitol dehydrogenase have been purified from G. suboxydans, both of which have similar and broad substrate specificity towards several different polyols. In this study, both quinoproteins were shown to be identical based on their immuno-cross-reactivity and also on gene disruption and were suggested to be the same as the previously isolated glycerol dehydrogenase (EC 1.1.99.22). Thus, glycerol dehydrogenase is the major polyol dehydrogenase involved in the oxidation of almost all sugar alcohols in Gluconobacter sp. In addition, the so-called quinoprotein glycerol dehydrogenase was also uniquely shown to oxidize d-gluconate, which was completely different from flavoprotein d-gluconate dehydrogenase (EC 1.1.99.3), which is involved in the production of 2-keto-d-gluconate. The gene disruption experiment and the reconstitution system of the purified enzyme in this study clearly showed that the production of 5-keto-d-gluconate in G. suboxydans is solely dependent on the quinoprotein glycerol dehydrogenase.

Microbial Production of Glyceric Acid, an Organic Acid That Can Be Mass Produced from Glycerol

ABSTRACT Glyceric acid (GA), an unfamiliar biotechnological product, is currently produced as a small by-product of dihydroxyacetone production from glycerol by Gluconobacter oxydans. We developed a method for the efficient biotechnological production of GA as a target compound for new surplus glycerol applications in the biodiesel and oleochemical industries. We investigated the ability of 162 acetic acid bacterial strains to produce GA from glycerol and found that the patterns of productivity and enantiomeric GA compositions obtained from several strains differed significantly. The growth parameters of two different strain types, Gluconobacter frateurii NBRC103465 and Acetobacter tropicalis NBRC16470, were optimized using a jar fermentor. G. frateurii accumulated 136.5 g/liter of GA with a 72% d-GA enantiomeric excess (ee) in the culture broth, whereas A. tropicalis produced 101.8 g/liter of d-GA with a 99% ee. The 136.5 g/liter of glycerate in the culture broth was concentrated to 236.5 g/liter by desalting electrodialysis during the 140-min operating time, and then, from 50 ml of the concentrated solution, 9.35 g of GA calcium salt was obtained by crystallization. Gene disruption analysis using G. oxydans IFO12528 revealed that the membrane-bound alcohol dehydrogenase (mADH)-encoding gene (adhA) is required for GA production, and purified mADH from G. oxydans IFO12528 catalyzed the oxidation of glycerol. These results strongly suggest that mADH is involved in GA production by acetic acid bacteria. We propose that GA is potentially mass producible from glycerol feedstock by a biotechnological process.

Membrane-bound Sugar Alcohol Dehydrogenase in Acetic Acid Bacteria catalyzes L-Ribulose Formation and NAD-Dependent Ribitol Dehydrogenase is Independent of the Oxidative Fermentation

To identify the enzyme responsible for pentitol oxidation by acetic acid bacteria, two different ribitol oxidizing enzymes, one in the cytosolic fraction of NAD(P)-dependent and the other in the membrane fraction of NAD(P)-independent enzymes, were examined with respect to oxidative fermentation. The cytoplasmic NAD-dependent ribitol dehydrogenase (EC 1.1.1.56) was crystallized from Gluconobacter suboxydans IFO 12528 and found to be an enzyme having 100kDa of molecular mass and 5 s as the sedimentation constant, composed of four identical subunits of 25 kDa. The enzyme catalyzed a shuttle reversible oxidoreduction between ribitol and D-ribulose in the presence of NAD and NADH, respectively. Xylitol and L-arabitol were well oxidized by the enzyme with reaction rates comparable to ribitol oxidation. D-Ribulose, L-ribulose, and L-xylulose were well reduced by the enzyme in the presence of NADH as cosubstrates. The optimum pH of pentitol oxidation was found at alkaline pH such as 9.5-10.5 and ketopentose reduction was found at pH 6.0. NAD-Dependent ribitol dehydrogenase seemed to be specific to oxidoreduction between pentitols and ketopentoses and D-sorbitol and D-mannitol were not oxidized by this enzyme. However, no D-ribulose accumulation was observed outside the cells during the growth of the organism on ribitol. L-Ribulose was accumulated in the culture medium instead, as the direct oxidation product catalyzed by a membrane-bound NAD(P)-independent ribitol dehydrogenase. Thus, the physiological role of NAD-dependent ribitol dehydrogenase was accounted to catalyze ribitol oxidation to D-ribulose in cytoplasm, taking D-ribulose to the pentose phosphate pathway after being phosphorylated. L-Ribulose outside the cells would be incorporated into the cytoplasm in several ways when need for carbon and energy sources made it necessary to use L-ribulose for their survival. From a series of simple experiments, membrane-bound sugar alcohol dehydrogenase was concluded to be the enzyme responsible for L-ribulose production in oxidative fermentation by acetic acid bacteria.

High Shikimate Production from Quinate with Two Enzymatic Systems of Acetic Acid Bacteria

3-Dehydroshikimate was formed with a yield of 57–77% from quinate via 3-dehydroquinate by two successive enzyme reactions, quinoprotein quinate dehydrogenase (QDH) and 3-dehydroquinate dehydratase, in the cytoplasmic membranes of acetic acid bacteria. 3-Dehydroshikimate was then reduced to shikimate (SKA) with NADP-dependent SKA dehydrogenase (SKDH) from the same organism. When SKDH was coupled with NADP-dependent D-glucose dehydrogenase (GDH) in the presence of excess D-glucose as an NADPH re-generating system, SKDH continued to produce SKA until 3-dehydroshikimate added initially in the reaction mixture was completely converted to SKA. Based on the data presented, a strategy for high SKA production was proposed.

Isolation and Characterization of Thermotolerant Gluconobacter Strains Catalyzing Oxidative Fermentation at Higher Temperatures

Thermotolerant acetic acid bacteria belonging to the genus Gluconobacter were isolated from various kinds of fruits and flowers from Thailand and Japan. The screening strategy was built up to exclude Acetobacter strains by adding gluconic acid to a culture medium in the presence of 1% D-sorbitol or 1% D-mannitol. Eight strains of thermotolerant Gluconobacter were isolated and screened for D-fructose and L-sorbose production. They grew at wide range of temperatures from 10°C to 37°C and had average optimum growth temperature between 30-33°C. All strains were able to produce L-sorbose and D-fructose at higher temperatures such as 37°C. The 16S rRNA sequences analysis showed that the isolated strains were almost identical to G. frateurii with scores of 99.36-99.79%. Among these eight strains, especially strains CHM16 and CHM54 had high oxidase activity for D-mannitol and D-sorbitol, converting it to D-fructose and L-sorbose at 37°C, respectively. Sugar alcohols oxidation proceeded without a lag time, but Gluconobacter frateurii IFO 3264T was unable to do such fermentation at 37°C. Fermentation efficiency and fermentation rate of the strains CHM16 and CHM54 were quite high and they rapidly oxidized D-mannitol and D-sorbitol to D-fructose and L-sorbose at almost 100% within 24 h at 30°C. Even oxidative fermentation of D-fructose done at 37°C, the strain CHM16 still accumulated D-fructose at 80% within 24 h. The efficiency of L-sorbose fermentation by the strain CHM54 at 37°C was superior to that observed at 30°C. Thus, the eight strains were finally classified as thermotolerant members of G. frateurii.

Membrane-Bound, 2-Keto-d-Gluconate-Yielding d-Gluconate Dehydrogenase from “Gluconobacter dioxyacetonicus” IFO 3271: Molecular Properties and Gene Disruption

ABSTRACT Most Gluconobacter species produce and accumulate 2-keto-d-gluconate (2KGA) and 5KGA simultaneously from d-glucose via GA in culture medium. 2KGA is produced by membrane-bound flavin adenine dinucleotide-containing GA 2-dehydrogenase (FAD-GADH). FAD-GADH was purified from “Gluconobacter dioxyacetonicus” IFO 3271, and N-terminal sequences of the three subunits were analyzed. PCR primers were designed from the N-terminal sequences, and part of the FAD-GADH genes was cloned as a PCR product. Using this PCR product, gene fragments containing whole FAD-GADH genes were obtained, and finally the nucleotide sequence of 9,696 bp was determined. The cloned sequence had three open reading frames (ORFs), gndS, gndL, and gndC, corresponding to small, large, and cytochrome c subunits of FAD-GADH, respectively. Seven other ORFs were also found, one of which showed identity to glucono-δ-lactonase, which might be involved directly in 2KGA production. Three mutant strains defective in either gndL or sldA (the gene responsible for 5KGA production) or both were constructed. Ferricyanide-reductase activity with GA in the membrane fraction of the gndL-defective strain decreased by about 60% of that of the wild-type strain, while in the sldA-defective strain, activity with GA did not decrease and activities with glycerol, d-arabitol, and d-sorbitol disappeared. Unexpectedly, the strain defective in both gndL and sldA (double mutant) still showed activity with GA. Moreover, 2KGA production was still observed in gndL and double mutant strains. 5KGA production was not observed at all in sldA and double mutant strains. Thus, it seems that “G. dioxyacetonicus” IFO 3271 has another membrane-bound enzyme that reacts with GA, producing 2KGA.

Purification and Properties of NADP-Dependent Shikimate Dehydrogenase from Gluconobacter oxydans IFO 3244 and Its Application to Enzymatic Shikimate Production

NADP-Dependent shikimate dehydrogenae (SKDH, EC 1.1.1.25) was purified from Gluconobacter oxydans IFO 3244. SKDH showed a single protein band on native-PAGE accompanying enzyme activity. It required NADP exclusively and catalyzed only the shuttle reaction between shikimate and 3-dehydroshikimate. The optimum pH for shikimate oxidation and 3-dehydroshikimate reduction was found at pH 10 and 7 respectively. SKDH proved to be a useful catalyst for shikimate production from 3-dehydroshikimate.

Crystallization and Properties of NADPH-Dependent L -Sorbose Reductase from Gluconobacter melanogenus IFO 3294

NADPH-Dependent L-sorbose reductase (SORD, synonimously NADP-dependent D-srobitol dehydrogenase) was purified and crystallized for the first time from the cytosolic fraction of Gluconobacter melanogenus IFO 3294. The enzyme catalyzed oxidoreduction between D-sorbitol and L-sorbose in the presence of NADP or NADPH. Affinity chromatography by a Blue-dextran Sepharose 4B column was effective for purifying the enzyme giving about 770-fold purification with an overall yield of more than 50%. The crystalline enzyme showed a single sedimentation peak in analytical ultracentrifugation, giving an apparent sedimentation constant of 3.8 s. Gel filtration on a Sephadex G-75 column gave the molecular mass of 60 kDa to the enzyme, which dissociated into 30 kDa subunit on SDS-PAGE, indicating that the enzyme is composed of 2 identical subunits. Reduction of L-sorbose to D-sorbitol predominated in the presence of NADPH with the optimum pH of 5.0-7.0. Oxidation of D-sorbitol to L-sorbose was observed in the presence of NADP at the optimum pH of 7.0-9.0. The relative rate of L-sorbose reduction was more than seven times higher to that of D-sorbitol oxidation. NAD and NADH were inert for both reactions. D-Fructose reduction in the presence of NADPH did not occur with SORD. Since the reaction rate in L-sorbose reduction highly predominated over D-sorbitol oxidation over a wide pH range, the enzyme could be available for direct enzymatic measurement of L-sorbose. Even in the presence of a large excess of D-glucose and other substances, oxidation of NADPH to NADP was highly specific and stoichiometric to the L-sorbose reduced. Judging from the enzymatic properties, SORD would contribute to the intracellular assimilation of L-sorbose incorporated from outside the cells where L-sorbose is accumulated in huge amounts in the culture medium.

Cyanide-insensitive Quinol Oxidase (CIO) from Gluconobacter oxydans is a unique terminal oxidase subfamily of cytochrome bd

Cyanide-insensitive terminal quinol oxidase (CIO) is a subfamily of cytochrome bd present in bacterial respiratory chain. We purified CIO from the Gluconobacter oxydans membranes and characterized its properties. The air-oxidized CIO showed some or weak peaks of reduced haemes b and of oxygenated and ferric haeme d, differing from cytochrome bd. CO- and NO-binding difference spectra suggested that haeme d serves as the ligand-binding site of CIO. Notably, the purified CIO showed an extraordinary high ubiquinol-1 oxidase activity with the pH optimum of pH 5-6. The apparent Vmax value of CIO was 17-fold higher than that of G. oxydans cytochrome bo3. In addition, compared with Escherichia coli cytochrome bd, the quinol oxidase activity of CIO was much more resistant to cyanide, but sensitive to azide. The Km value for O2 of CIO was 7- to 10-fold larger than that of G. oxydans cytochrome bo3 or E. coli cytochrome bd. Our results suggest that CIO has unique features attributable to the structure and properties of the O2-binding site, and thus forms a new sub-group distinct from cytochrome bd. Furthermore, CIO of acetic acid bacteria may play some specific role for rapid oxidation of substrates under acidic growth conditions.

Selective, High Conversion of D-Glucose to 5-Keto-D-gluoconate by Gluconobacter suboxydans

Selective, high-yield production of 5-keto-D-gluconate (5KGA) from D-glucose by Gluconobacter was achieved without genetic modification. 5KGA production by Gluconobacter suffers byproduct formation of 2-keto-D-gluconate (2KGA). By controlling the medium pH strictly in a range of pH 3.5–4.0, 5KGA was accumulated with 87% conversion yield from D-glucose. The pH dependency of 5KGA formation appeared to be related to that of gluconate oxidizing activity.