Production of fructooligosaccharides in high yield using a mixed enzyme system of β-fructofuranosidase and glucose oxidase

A mixed enzyme system, with -fructofuranosidase (obtained from Aspergillus japonicus) and commercial glucose oxidase (Gluzyme, Novo Nordisk), produced fructooligosaccharides (FOS) in high yield from sucrose. The reaction was performed in an aerated stirred tank reactor controlled at pH 5.5 by a slurry of CaCO₃. Glucose, an inhibitor of -fructofuranosidase, produced in the reaction was converted by glucose oxidase to gluconic acid, which was then precipitated to calcium gluconate in solution. The system produced more than 90% (w/w) FOS on a dry weight basis, the remainder was glucose, sucrose and a small amount of calcium gluconate. Most of the FOS and sucrose was hydrolyzed to fructose in the mixed enzyme system with glucose oxidase and -fructofuranosidase from Asp. niger.     

Production of Calcium Gluconate by Penicillium chrysogenum in Submerged Culture

The waste mycelium of Penicillium chrysogenum HA-10 (obtained at the end of penicillin fermentation), or a 24-hr-old freshly grown vegetative inoculum of this organism, was found to utilize glucose for the production of calcium gluconate by submerged fermentation in shake flasks. After 72 to 96 hr of fermentation at 24 C, 90 to 95% of the reducing sugar from the 15% glucose medium was converted to calcium gluconate. Reuse of the mycelium for successive experiments reduced the fermentation period to 72 hr or less because of an enhancement of glucose utilization. Ten successive batches of 15% glucose medium were fermented by the reuse method. Fermentation media containing up to 30% glucose could be used, provided boric acid was added to prevent the precipitation of calcium gluconate formed. We found that 30% hydrol (a by-product of glucose manufacture containing 50 to 55% reducing sugar), when used in place of glucose in the fermentation medium, inhibited the rate of glucose utilization. However, this effect was partially reversed by pretreatment of hydrol with 2 to 4% activated charcoal before addition to the fermentation medium.     

The regulation of transport of glucose, gluconate and 2-oxogluconate and of glucose catabolism in Pseudomonas aeruginosa.

1. The induction by glucose and gluconate of the transport systems and catabolic enzymes for glucose, gluconate and 2-oxogluconate was studied with Pseudomonas aeruginosa PAO1 growing in a chemostat under conditions of nitrogen limitation with citrate as the major carbon source. 2. In the presence of a residual concentration of 30mM-citrate an inflowing glucose concentration of 6-8 mM was required to induce the glucose-transport system and associated catabolic enzymes. When the glucose concentration was raised to 20mM the glucose-transport system was repressed, but the transport system for gluconate, and at higher glucose concentrations, that for 2-oxogluconate, were induced. No repression of the glucose-catabolizing enzymes occurred at the higher inflowing glucose concentrations. 3. In the presence of 30mM-citrate no marked threshold concentration was required for the induction of the gluconate-transport system by added gluconate. 4. In the presence of 30mM-citrate and various concentrations of added glucose and gluconate, the activity of the glucose-transport system accorded with the proposal that a major factor concerned in the repression of this system was the concentration of gluconate, produced extracellularly by glucose dehydrogenase. 5. This proposal was supported by chemostat experiments with mutants defective in glucose dehydrogenase. Such mutants showed no repression of the glucose-transport system by high inflowing concentrations, but with a mutant apparently defective only in glucose dehydrogenase, the addition of gluconate caused repression of the glucose-transport system. 6. Studies with the mutants showed that both glucose and gluconate can induce the enzymes of the Entner-Doudoroff system, whereas for the induction of the gluconate-transport system glucose must be converted into gluconate.     

Effect of ammonium and nitrate ratio on glucose oxidase activity during gluconic acid fermentation by a mutant strain of Aspergillus niger

Of the factors tested, the source and concentration of carbon and nitrogen in the medium exerted maximum effect on growth and acid production. Glucose (15%) and urea (0.14%) induced glucose oxidase synthesis and optimum yield of calcium gluconate. Potassium dihydrogen phosphate (0.2%) and magnesium sulphate (0.06%) stimulated glucose oxidase activity and calcium gluconate production. Borax at a concentration of 1.5 g/L induced maximum glucose oxidase and calcium gluconate production with increased glucose utilization.     

Enhanced l-lysine production in threonine-limited continuous culture of Corynebacterium glutamicum by using gluconate as a secondary carbon source with glucose

In order to improve the production rate of l-lysine, a mutant of Corynebacterium glutamicum ATCC 21513 was cultivated in complex medium with gluconate and glucose as mixed carbon sources. In a batch culture, this strain was found to consume gluconate and glucose simultaneously. In continuous culture at dilution rates ranging from 0.2 h⁻¹ to 0.25 h⁻¹, the specific l-lysine production rate increased to 0.12 g g⁻¹ h⁻¹ from 0.1 g g⁻¹ h⁻¹, the rate obtained with glucose as the sole carbon source [Lee et al. (1995) Appl Microbiol Biotechnol 43:1019–1027]. It is notable that l-lysine production was observed at higher dilution rates than 0.4 h⁻¹, which was not observed when glucose was the sole carbon source. The positive effect of gluconate was confirmed in the shift of the carbon source from glucose to gluconate. The metabolic transition, which has been characterized by decreased l-lysine production at the higher glucose uptake rates, was not observed when gluconate was added. These results demonstrate that the utilization of gluconate as a secondary carbon source improves the maximum l-lysine production rate in the threonine-limited continuous culture, probably by relieving the limiting factors in the lysine synthesis rate such as NADPH supply and/or phosphoenolpyruvate availability. Received: 16 May 1997 / Received revision: 28 August 1997 / Accepted: 29 August 1997     

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     

Influence of Phosvitin and Calcium Gluconate Concentration on Permeation and Intestinal Absorption of Calcium Ions

The effect of egg yolk phosvitin on the permeation and absorption of calcium was investigated in vitro in relation to calcium gluconate concentration. Obtained results indicate that phosvitin significantly reduces the intestinal calcium absorption from 1 and 10 mM of calcium gluconate solution. It is associated with the formation of the complex of Ca (II) ions with phosvitin. The process of calcium permeation increases under phosvitin influence when calcium gluconate concentrations rise up to 10 mM. At a higher concentration of calcium gluconate (20 mM), no effect of phosvitin was seen on permeation of calcium ions.     

Continuous production of high-purity fructooligosaccharides and ethanol by immobilized Aspergillus japonicus and Pichia heimii

High-purity fructooligosaccharides (FOS) were produced from sucrose by an innovative process incorporating immobilized Aspergillus japonicus and Pichia heimii cells. Intracellular FTase of A. japonicus converted sucrose into FOS and glucose, and P. heimii fermented glucose mainly into ethanol. The continuous production of FOS was carried out using a tanks-in-series bioreactor consisting of three stirred tanks. When a solution composed of 1 g L^?1 yeast extract and 300 g L^?1 sucrose was fed continuously to the bioreactor at a dilution rate of 0.1 h^?1, FOS at a purity of up to 98.2 % could be achieved and the value-added byproduct ethanol at 79.6 g L^?1 was also obtained. One gram of sucrose yielded 0.62 g FOS and 0.27 g ethanol. This immobilized dual-cell system was effective for continuous production of high-purity FOS and ethanol for as long as 10 days.     

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.     

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.     

The consequence of stimulating glucose dehydrogenase activity by the addition of PQQ on metabolite production by Agrobacterium radiobacter NCIB 11883

Summary Agrobacterium radiobacter NCIB 11 883 does not produce gluconate under conditions of glucose excess in batch or continuous culture. However, the addition of micromolar concentrations of pyrrolo quinoline quinone (PQQ) to fermentation media resulted in rapid excretion of gluconate by batch and continuous cultures. This rapid dehydrogenation of glucose was found in cells grown under carbon and nitrogen limitation and is constitutive which suggests that the only reason why this activity is not normally expressed is due to the inability of the organism to synthesize the prosthetic group (PQQ) of the glucose dehydrogenase enzyme.Although the addition of PQQ to batch and continuous cultures caused a very rapid specific rate of gluconate production (0.6–1.1 g gluconate g^-1 dry wt. h^-1) the rate of exopolysaccharide production remained unaltered. Indeed, when the rates of substrate and oxygen uptake are corrected for the rate of gluconate production in the presence of PQQ there appears to be little physiological consequence as a result of this oxidation.     

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.     

Gluconate metabolism of Klebsiella pneumoniae NCTC 418 grown in chemostat culture

The metabolism of gluconate by Klebsiella pneumoniae NCTC 418 was studied in continuous culture. Under all gluconate-excess conditions at low culture pH values (pH 4.5–5.5) the majority (70–90%) of the gluconate metabolized was converted to 2-oxogluconate via gluconate dehydrogenase (GADH), although specific 2-oxogluconate production rates under potassium-limited conditions were significantly lower than under other gluconate-excess conditions. At high culture pH values, metabolism shifted towards production of acetate. Levels of GADH were highest at low culture pH values and synthesis was stimulated by the presence of (high concentrations of) gluconate. An increase in activity of the tricarboxylic acid cycle was accompanied by a decrease in GADH activity in vivo and in vitro, suggesting that the GADH serves a role as an alternative energy-generating system. Anaerobic 2-oxogluconate production was found to be possible in the presence of nitrate as electron acceptor. Levels of gluconate kinase were highest when K. pneumoniae was grown under gluconate-limited conditions. Under carbon-excess conditions, levels of this enzyme correlated with the intracellular catabolic flux.Abbreviations GADH gluconate dehydrogenase (EC 1.1.99.3) - GAK gluconate kinase (EC 2.7.1.12) - GDH glucose dehydrogenase (EC 1.1.99.17) - PQQ pyrroloquinoline quinone [2,7,9-tricarboxy-1-H-pyrrolo (2,3-f) quinoline-4,5-dione] - TCA trichloroacetic acid     

Monitoring flux through the oxidative pentose phosphate pathway using [1-14C]gluconate

The aim of this work was to examine the metabolism of exogenous gluconate by a 4-day-old cell suspension culture of Arabidopsis thaliana (L.) Heynh. Release of (14)CO(2) from [1-(14)C]gluconate was dependent on the concentration in the medium and could be resolved into a substrate-saturable component (apparent K(m) of approximately 0.4 mM) and an unsaturable component. At an external concentration of 0.3 mM, the rate of decarboxylation of applied gluconate was 0.2% of the rate of oxygen consumption by the cells. There was no effect of 0.3 mM gluconate on the rate of oxygen consumption, or on the rate of (14)CO(2) release from either [1-(14)C]glucose or [6-(14)C]glucose by the culture. The following observations argue that gluconate taken up by the cells is metabolised by direct phosphorylation to 6-phosphogluconate and subsequent decarboxylation through 6-phosphogluconate dehydrogenase. First, more than 95% of the label released from [1-(14)C]gluconate during metabolism by the cell culture was recovered as (14)CO(2). Secondly, inhibition of the oxidative pentose phosphate pathway (OPPP) by treatment with 6-aminonicotinamide preferentially inhibited release of (14)CO(2) from [1-(14)C]gluconate relative to that from [1-(14)C]glucose. Thirdly, perturbation of glucose metabolism by glucosamine did not affect (14)CO(2) from [1-(14)C]gluconate. Fourth, stimulation of the OPPP by phenazine methosulphate stimulated release of (14)CO(2) from [1-(14)C]gluconate to a far greater extent than that from [1-(14)C]glucose. It is proposed that measurement of (14)CO(2) from [1-(14)C]gluconate provides a simple and sensitive technique for monitoring flux through the OPPP pathway in plants.     

Catabolism of carbohydrates and organic acids and expression of nitrogenase by azospirilla

Fructose, galactose, L-arabinose, gluconate, and several organic acids support rapid growth and N2 fixation of Azospirillum brasiliense ATCC 29145 (strain Sp7) as a sole source of carbon and energy. Growth of Azospirillum lipoferum ATCC 29707 (strain Sp59b) is also supported by glucose, mannose, mannitol, and alpha-ketoglutarate. Oxidation of fructose and gluconate by A. brasiliense Sp7 and of glucose, gluconate, and fructose by A. lipoferum Sp59b was achieved through inducible enzymatic mechanisms. Both strains exhibited all of the enzymes of the Embden-Meyerhof-Parnas pathway, and strain Sp59b also possesses all the enzymes of the Entner-Doudoroff pathway. Fluoride inhibited growth on fructose (strains Sp7 and Sp59b) or on glucose (strain Sp59b) but not on malate. There was no activity via the oxidative hexose monophosphate pathway in either strain. There was greater activity with 1-phosphofructokinase than with 6-phosphofructokinase in both strains. Strain Sp59b formed fructose-6-phosphate via hexokinase, an enzyme that is lacking in strain Sp7. A. brasiliense and A. lipoferum exhibited the enzymes both of the tricarboxylic acid cycle and of the glyoxylate shunt; iodoacetate, fluoropyruvate, and malonate were inhibitory. A. brasiliense Sp7 could not transport [14C]glucose and alpha-[14C]ketoglutarate into its cells.     

Kinetics of Bifidobacterium longum ATCC 15707 fermentations: effect of the dilution rate and carbon source

The effect of the dilution rate on biomass and product synthesis in fermentations of glucose, fructose and a commercial mixture of fructooligosaccharides (FOS) by Bifidobacterium longum ATCC 15707 was studied. Kinetic parameters (maximum specific growth rate, Monod constant, maintenance, and yield coefficients) in the mathematical model of the fermentation were estimated from experimental data. In the FOS mixture fermentations, approximately 12% of the total reducing sugars (mainly fructose) in the feed were not metabolized by the bacterium. In fermentations of fructose and the FOS mixture, biomass concentration increased as the dilution rate increased and, once maximum values were reached [3.90 (D=0.20 h^–1) and 2.54 g l^–1 (D=0.15 h^–1), respectively], decreased rapidly as the culture was washed out. Formic acid was detected at low dilution rates in glucose and fructose fermentations. The main products in fermentations of the three carbon sources were lactic and acetic acids. Average values of the molar ratio between acetic and lactic acids of 1.18, 1.21 and 0.83 mol mol^–1 were obtained in glucose, fructose and FOS mixture fermentations, respectively. In batch fermentations carried out without pH control this molar ratio was lower than 1.5 only when fructose was used as the carbon source.     

Production of high fructo-oligosaccharide syrup with two enzyme system of fructosyltransferase and glucose oxidase

Summary A novel two enzyme system of fructosyltransferase and glucose oxidase to enhance the content of the net fructo—oligosaccharide (FOS) fractions in the industrial production of FOS syrup from sucrose was devised. The net FOS content in the commercial FOS syrup has been limited only to 55–60 % due to the accumulation of glucose which acts as a feedback inhibitor of the fructosyltransferase. By supplementing glucose oxidase to the conventional FOS reaction system, we could convert the glucose to gluconic acid readily separable from neutral sugars by simple ion exchange operation in the next step. The simultaneous removal of glucose was proved effective in proceeding the reaction by fructosyltransferase further by relieving the product inhibition caused by glucose. By this way, we could raise the net FOS content as high as 90 %.     

Fermentations of fructo-oligosaccharides and their components by Bifidobacterium infantis ATCC 15697 on batch culture in semi-synthetic medium

AIMS: To compare the physiological behaviour of Bifidobacterium infantis ATCC 15697 growing on synthetic oligofructose or its components. METHODS AND RESULTS: The studies were carried out in regulated or non-regulated batch cultures on semi-synthetic media. Differences between the carbohydrate utilization patterns with glucose, fructose, sucrose and fructo-oligosaccharides (FOS) were determined. Glucose was the preferred substrate for growth and biomass production, whereas fructose was the best for lactate and acetate production. With sucrose, biomass production reached the level obtained with glucose, whereas with FOS, more metabolites were produced, as with fructose. In a mixture of FOS, the shorter saccharides were used first and fructose was released in the medium. Fructofuranosidase, an enzyme necessary to hydrolyse FOS, was inducible by fructose. CONCLUSION: Glucose contained in FOS and sucrose might sustain growth and cell production, while fructose might enable the production of major metabolites. SIGNIFICANCE AND IMPACT OF THE STUDY: A better understanding of the bifidogenic nature of oligofructose has been gained.     

The kinetics and physiology of stipitatic acid and gluconate production by carbon sufficient cultures of Penicillium stipitatum growing in continuous culture

The yield from glucose of ammonia-grown carbon-limited continuous cultures of Penicillium stipitatum was ca. 20% higher than that of nitrate-grown cultures at all growth rates examined. However, the yield from oxygen was similar during growth on both nitrogen sources. Under phosphate limitation the specific rate of gluconic acid and stipitatic acid production increased with growth rate, but the former product accounted for virtually 100% of the excreted carbon. Stipitatic acid was not produced under nitrogen limitation, and glucose supplied to the culture in excess of that required for growth was virtually quantatively converted into gluconic acid. Productivities of 11.4 g gluconic acid/L/h were stably maintained in continuous culture. Under conditions of glucose excess the enzyme glucose oxidase was excreted into the culture. The specific activity of this extracellular enzyme increased when the input glucose concentration to the culture was progressively increased. The excretion of a protein under nitrogen limitation suggests that this enzyme plays an important role under these conditions. Indeed, it was demonstrated that nitrogen-limited cultures did not overmetabolize gluconate at either pH 6.5 or 3.5, although up to 29 g/L gluconate was present in the culture. The Y(gluconate) and YO(2) of C- and N-limited gluconate-grown cultures were similar indicating that the rapid conversion of glucose to gluconate probably affords a means of regulating carbon flow in this organism. Nitrogen-limited cultures of P. stipitatum overmetabolized glucose to a much greater extent than acetate, fructose, or gluconate.     

Gluconate Catabolism in Rhizobium japonicum

Gluconate catabolism in Rhizobium japonicum ATCC 10324 was investigated by the radiorespirometric method and by assaying for key enzymes of the major energy-yielding pathways. Specifically labeled gluconate gave the following results for growing cells, with values expressed as per cent (14)CO(2) evolution: C-1 = 93%, C-2 = 57%, C-3 = 30%, C-4 = 70%, C-6 = 39%. The preferential release of (14)CO(2) from C-1 and C-4 indicate that gluconate is degraded primarily by the Entner-Doudoroff pathway but the inequalities between C-1 and C-4 and between C-3 and C-6 indicate that another pathway(s) also participates. The presence of gluconokinase and a system for converting 6-phosphogluconate to pyruvate also indicate a role for the Entner-Doudoroff pathway. The extraordinarily high yield of (14)CO(2) from C-1 labeled gluconate suggests that the other participating pathway is a C-1 decarboxylative pathway. The key enzyme of the pentose phosphate pathway, 6-phosphogluconate dehydrogenase, could not be demonstrated. Specifically labeled 2-ketogluconate and 2,5-diketogluconate were oxidized by gluconate grown cells and gave ratios of C-1 to C-6 of 2.73 and 2.61, respectively. These compare with a ratio of 2.39 obtained with specifically labeled gluconate. Gluconate dehydrogenase, the first enzyme in the ketogluconate pathway found in acetic acid bacteria, was found. Oxidation of specifically labeled pyruvate, acetate, succinate, and glutamate by gluconate-grown cells yielded the preferential rates of (14)CO(2) evolution expected from the operation of the tricarboxylic acid cycle. These data are consistent with the operation of the Entner-Doudoroff pathway and tricarboxylic acid cycle as the primary pathways of gluconate oxidation in R. japonicum. An ancillary pathway for the initial breakdown of gluconate would appear to be the ketogluconate pathway which enters the tricarboxylic acid cycle at alpha-ketoglutarate.