Continuous 2-Keto-L-gulonic acid fermentation by mixed culture of Ketogulonicigenium vulgare DSM 4025 and Bacillus megaterium or Xanthomonas maltophilia.

The fermentation process of 2-keto-L-gulonic acid (2KGA) from L-sorbose was developed using a two-stage continuous fermentation system. The mixed culture of Ketogulonicigenium vulgare DSM 4025 and Bacillus megaterium DSM 4026 produced 90 g/L of 2KGA from 120 g/L of L-sorbose at the dilution rate of 0.01 h(-1) in a single-stage continuous fermentation process. But after the production period was beyond 150 h, the significant decrease of 2KGA productivity was observed. When the non-spore forming bacteria Xanthomonas maltophilia IFO 12692 was used instead of B. megaterium DSM 4026 as a partner strain for K. vulgare DSM 4025, the 2KGA productivity was significantly improved in a two-stage continuous culture mode, in which two fermentors of the same size and volume were connected in series. In this mode, with two sets of 3-L jar fermentors, the steady state could be continued to over 1,331.5 h at least, when the dilution rates were 0.0382 h(-1) and 0.0380 hour(-1), respectively, for the first and second fermentors. The overall productivity was calculated to be 2.15 g/L/h at 113.1 g/L and a molar conversion yield of 90.1%. In the up-scaling fermentation to 30-L jar fermentors, 118.5 g/L of 2KGA was produced when dilution rates in both stages were 0.0430 hour(-1), and the overall productivity was calculated to be 2.55 g/L/h.

Continuous 2-keto-L-gulonic acid fermentation from L-sorbose by Ketogulonigenium vulgare DSM 4025.

A single-stage continuous fermentation process for the production of 2-keto-L-gulonic acid (2KGA) from L-sorbose using Ketogulonigenium vulgare DSM 4025 was developed. The chemostat culture with the dilution rate that was calculated based on the relationship between the 2KGA production rate and the 2KGA concentration was feasible for production with high concentration of 2KGA. In this system, 112.2 g/L of 2KGA on the average was continuously produced from 114 g/L of L-sorbose. A steady state of the fermentation was maintained for the duration of more than 110 h. The dilution rate was kept in the range of 0.035 and 0.043 h(-1), and the 2KGA productivity was 3.90 to 4.80 g/L/h. The average molar conversion yield of 2KGA from L-sorbose was 91.3%. Under the optimal conditions, L-sorbose concentration was kept at 0 g/L. Meanwhile, the dissolved oxygen level was changing in response to the dilution rate and 2KGA concentration. In the dissolved oxygen (DO) range of 16% to 58%, it was revealed that the relationship between DO and D possessed high degree of positive correlation under the L-sorbose limiting condition (complete consumption of L-sorbose). Increasing D closer to the critical value for washing out point of the continuous fermentation, DO value tended to be gradually increased up to 58%. In conclusion, an efficient and reproducible continuous fermentation process for 2KGA production by K. vulgare DSM 4025 could be developed using a medium containing baker's yeast without using a second helper microorganism.

Pyrroloquinoline quinone-dependent dehydrogenases from Ketogulonicigenium vulgare catalyze the direct conversion of L-sorbosone to L-ascorbic acid.

A novel enzyme, L-sorbosone dehydrogenase 1 (SNDH1), which directly converts L-sorbosone to L-ascorbic acid (L-AA), was isolated from Ketogulonicigenium vulgare DSM 4025 and characterized. This enzyme was a homooligomer of 75-kDa subunits containing pyrroloquinoline quinone (PQQ) and heme c as the prosthetic groups. Two isozymes of SNDH, SNDH2 consisting of 75-kDa and 55-kDa subunits and SNDH3 consisting of 55-kDa subunits, were also purified from the bacterium. All of the SNDHs produced L-AA, as well as 2-keto-L-gulonic acid (2KGA), from L-sorbosone, suggesting that tautomerization of L-sorbosone causes the dual conversion by SNDHs. The sndH gene coding for SNDH1 was isolated and analyzed. The N-terminal four-fifths of the SNDH amino acid sequence exhibited 40% identity to the sequence of a soluble quinoprotein glucose dehydrogenase from Acinetobacter calcoaceticus. The C-terminal one-fifth of the sequence exhibited similarity to a c-type cytochrome with a heme-binding motif. A lysate of Escherichia coli cells expressing sndH exhibited SNDH activity in the presence of PQQ and CaCl2. Gene disruption analysis of K. vulgare indicated that all of the SNDH proteins are encoded by the sndH gene. The 55-kDa subunit was derived from the 75-kDa subunit, as indicated by cleavage of the C-terminal domain in the bacterial cells.

Microbial production of L-ascorbic acid from D-sorbitol, L-sorbose, L-gulose, and L-sorbosone by Ketogulonicigenium vulgare DSM 4025.

Ketogulonicigenium vulgare DSM 4025, known as a 2-keto-L-gulonic acid producing strain from L-sorbose via L-sorbosone, surprisingly produced L-ascorbic acid from D-sorbitol, L-sorbose, L-gulose, and L-sorbosone as the substrate under a growing or resting condition. As the best result, K. vulgare DSM 4025 produced 1.37 g per liter of L-AA from 5.00 g per liter of L-sorbosone during 4 h incubation time at 30 degrees C under the resting cell condition having 5.70 g per liter of wet cells. The precursor of L-AA formation from D-sorbitol and L-sorbose, except for L-gulose, was thought to be the putative furanose form of L-sorbosone. This is the first time it is reported that bacteria can produce vitamin C via L-sorbosone.

Membrane-bound D-sorbitol dehydrogenase of Gluconobacter suboxydans IFO 3255--enzymatic and genetic characterization.

Gluconobacter strains effectively produce L-sorbose from D-sorbitol because of strong activity of the D-sorbitol dehydrogenase (SLDH). L-sorbose is one of the important intermediates in the industrial vitamin C production process. Two kinds of membrane-bound SLDHs, which consist of three subunits, were reportedly found in Gluconobacter strains [Agric. Biol. Chem. 46 (1982) 135,FEMS Microbiol. Lett. 125 (1995) 45]. We purified a one-subunit-type SLDH (80 kDa) from the membrane fraction of Gluconobacter suboxydans IFO 3255 solubilized with Triton X-100 in the presence of D-sorbitol, but the cofactor could not be identified from the purified enzyme. The SLDH was active on mannitol, glycerol and other sugar alcohols as well as on D-sorbitol to produce respective keto-aldoses. Then, the SLDH gene (sldA) was cloned and sequenced. It encodes the polypeptide of 740 residues, which contains a signal sequence of 24 residues. SLDH had 35-37% identity to those of membrane-bound quinoprotein glucose dehydrogenases (GDHs) from Escherichia coli, Gluconobacter oxydans and Acinetobacter calcoaceticus except the N-terminal hydrophobic region of GDH. Additionally, the sldB gene located just upstream of sldA was found to encode the polypeptide consisting of 126 very hydrophobic residues that is similar to the one-sixth N-terminal region of the GDH. Development of the SLDH activity in E. coli required co-expression of the sldA and sldB genes and the presence of PQQ. The sldA gene disruptant showed undetectable oxidation activities on D-sorbitol in growing culture, and resting-cell reaction (pH 4.5 and 7); in addition, they showed undetectable activities on D-mannitol and glycerol. The disruption of the sldB gene by a gene cassette with a downward promoter to express the sldA gene resulted in formation of a larger size of the SLDH protein and in undetectable oxidation of the polyols. In conclusion, the SLDH of the strain 3255 functions as the main polyol dehydrogenase in vivo. The sldB polypeptide possibly has a chaperone-like function to process the SLDH polypeptide into a mature and active form.

5-keto-D-gluconate production is catalyzed by a quinoprotein glycerol dehydrogenase, major polyol dehydrogenase, in gluconobacter species.

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.

Purification and properties of membrane-bound D-sorbitol dehydrogenase from Gluconobacter suboxydans IFO 3255.

D-Sorbitol dehydrogenase was solubilized from the membrane fraction of Gluconobacter suboxydans IFO 3255 with Triton X-100 in the presence of D-sorbitol. Purification of the enzyme was done by fractionation with column chromatographies of DEAE-Cellulose, DEAE-Sepharose, hydroxylapatite, and Sephacryl HR300 in the presence of Triton X-100. The molecular mass of the enzyme was 800 kDa, consisting of homologous subunits of 80 kDa. The optimum pH of the enzyme activity was 6.0, and the optimum temperature was 30 degrees C. Western blot analysis suggested the occurrence of the enzyme in all the Gluconobacter strains tested.