Production of catalase and glucose oxidase by Aspergillus niger using unconventional oxygenation of culture

A novel method for increasing dissolved oxygen concentration in culture media has been developed. It involves adding hydrogen peroxide (H2O2) to the medium which is then decomposed to oxygen and water by catalase. Some factors affecting oxygenation of culture were investigated. Maximal oxygen concentration occurred in 50 ml of the medium containing 0-2 g wet mycelium and 0.2% glucose at pH 5.0. A new apparatus for automated addition of H2O2 to the bioreactor to keep the dissolved oxygen concentration constant over the range 1-100% +/- 2% was tested. A significant increase (over sixfold) of intracellular catalase activity was obtained while the dissolved oxygen concentration remained stable (30% +/- 2%).     

Effects of metal ions on simultaneous production of glucose oxidase and catalase by Aspergillus niger

The effects of various metal ions on the simultaneous production of glucose oxidase and catalase by Aspergillus niger were investigated. Calcium carbonate induced synthesis of both enzymes. The induction of calcium carbonate was accompanied by a metabolic shift from the glycolytic pathway (EMP, Embden-Meyerhof-Parnas) to direct oxidation of glucose by glucose oxidase. The time course of the biosynthesis of both enzymes is reported. The logistic model was in good agreement with the experimental growth results. The production of both enzymes was growth-associated. Finally, a model of growth and product formation was also proposed.     

Simultaneous production of catalase, glucose oxidase and gluconic acid by Aspergillus niger mutant.

The production of gluconic acid, extracellular glucose oxidase and catalase in submerged culture by a number of biochemical mutants has been evaluated. Optimization of stirrer speed, time cultivation and buffering action of some chemicals on glucose oxidase, catalase and gluconic acid production by the most active mutant, AM-11, grown in a 3-L glass bioreactor was investigated. Three hundred rpm appeared to be optimum to ensure good growth and best glucose oxidase production, but gluconic acid or catalase activity obtained maximal value at 500 or 900 rpm, respectively. Significant increase of dissolved oxygen concentration in culture (16-21%) and extracellular catalase activity were obtained when the traditional aeration was employed together with automatic dosed hydrogen peroxide.     

Kinetics of glucose oxidase excretion by recombinant Aspergillus niger

The kinetics of glucose oxidase (GOD) excretion by recombinant Aspergillus niger NRRL-3 (GOD3-18) were investigated using enzymatic activity measurements as well as gel electrophoresis techniques. The majority of GOD was produced during rapid growth in the first phase of the cultivation. The high excretion rate during this phase did not prevent the endocellular accumulation of GOD up to 40% of the total soluble cell protein demonstrating that the production rate exceeded the excretion rate of the enzyme into the culture medium. During the second phase of the cultivation, excretion of GOD occurred at a slower rate, although the majority of GOD produced during the first phase was excreted during the second phase of the cultivation. At the end, about 90% of the total GOD produced was recovered from the culture medium. Two-dimensional gel electrophoresis provided evidence that endo- and exocellular GOD were indistinguishable, revealing identical posttranslational modifications (e.g., signal sequence cleavage, glycosylation pattern). The results demonstrate that the initial steps of the secretory pathway are fast and that the excretion of the enzyme into the culture fluid was most likely delayed due to retention by the cell wall. (c) 1996 John Wiley & Sons, Inc.     

Location of glucose oxidase during production by Aspergillus niger

The production of the enzyme glucose oxidase by Aspergillus niger is well documented. However, its distribution within the fungal culture is less well defined. Since the enzyme location impacts significantly on enzyme recovery, this study quantifies the enzyme distribution between the extracellular fluid, cell wall, cytoplasm and slime mucilage fractions in an A. niger NRRL-3. The culture was separated into the individual fractions and the glucose oxidase activity was determined in each. The extracellular fluid contained 38% of the total activity. The remaining 62% was associated with the mycelia and was distributed between the cell wall, cytoplasm and slime mucilage in the proportions of 34, 12 and 16%, respectively. Intracellular cytoplasmic and cell wall sites were confirmed using immunocytochemical labelling of the mycelia. In the non-viable cell, the mycelial-associated enzyme was distributed between these sites, whereas in the viable cell, it was predominantly associated with the cell wall. The distribution of the enzyme activity indicates that recovery from the solids would result in a 38% loss, whereas recovery from the extracellular fluid would result in a 62% loss. The results also suggest, however, that this 62% loss could be reduced to around 34% by disintegrating the solids prior to separation due to the contribution of the enzyme in the cytoplasm and slime mucilage. This was confirmed by independently establishing the percentage activity in the liquid and solid portions of a disintegrated culture as 62 and 38%, respectively.     

Expression and overproduction of glucose oxidase in Aspergillus niger

Summary This report describes the expression of cloned glucose oxidase gene (god) in glucose-oxidase-deficient mutants (God^–) of Aspergillus niger NRRL-3, the use of this gene for the elevation of glucose oxidase (GOD) productivity in the parental strain, and the further improvement of GOD production by subjecting the transformants to nitrous acid mutagenesis.Correspondence to: F. A. Sharif     

Aspergillus niger mutants with increased glucose oxidase production

Summary Aspergillus niger NRRL-3, an organism used for the industrial scale production of d-gluconic acid and glucose oxidase (EC 1.1.3.4), was subjected to mutagenesis and selection for acid production on diagnostic media containing methyl red. The plates contained 0.1 M d-glucose, a concentration that does not produce a color change in the medium surrounding mycelia of the parental strain under the conditions employed. Mutagenized spores yielded occasional colonies which were able to grow rapidly and were surrounded by a reddish zone. A number of such presumptive mutants were selected and isolated. Twenty-six such strains were grown in shaken cultures with liquid media containing 0.01, 0.1 or 0.5 M d-glucose, harvested, disrupted and the specific activity of d-glucose oxidase determined. Seven of the mutant strains had glucose oxidase specific activities markedly higher than the parental strain.Paper No. 8393, Nebraska Agricultural Research Division.     

Cytochemical localization of glucose oxidase in peroxisomes of Aspergillus niger

Summary The subcellular localization of glucose oxidase (E.C. 1.1.3.4) in mycelia of Aspergillus niger has been investigated using cytochemical staining techniques. Mycelia from fermenter cultures, which produced gluconic acid from glucose, contained elevated levels of glucose oxidase and catalase. Both enzymes were located in microbodies. In addition, when the organism was grown on glucose with methylamine as a nitrogen source, amine oxidase activity was detected in the microbodies. These organelles can therefore be designated as peroxisomes.     

Optimization of an Aspergillus niger glucose oxidase production process

The purpose of the present study was to ascertain the optimal concentration of dissolved oxygen in order to maximize the intracellular glucose oxidase formation in Aspergillus niger. Cultivations performed in a 3.5 l laboratory reactor showed that a dissolved oxygen concentration at 3% of saturation at a total pressure of 1.2 bar was optimal for maximizing intracellular glucose oxidase activity. Cultivations performed at higher dissolved oxygen concentrations did not produce as much glucose oxidase as those performed at 3%, although the formation rate was high. Experiments revealed that maximal intracellular glucose oxidase formation for the A. niger strain used, is accomplished by limiting the gluconic acid production rate by means of maintaining a low dissolved oxygen concentration. Several attempts to achieve higher intracellular glucose oxidase activity were also made by manipulating the glucose concentration at a 3% dissolved oxygen concentration. However, no enhancement in glucose oxidase activity was observed.     

Optimization of glucose oxidase production by Aspergillus niger using genetic-and process-engineering techniques

Wild-type Aspergillus niger NRRL-3 was transformed with multiple copies of the glucose oxidase structural gene (god). The gene was placed under the control of the gpd A promoter of A. nidulans. For more efficient secretion the -amylase signal peptide from A oryzae was inserted in front of god. Compared to the wild type, the recombinant strain NRRL-3 (GOD3-18) produced up to four times more extracellular glucose oxidase under identical culture conditions. Addition of yeast extract (2 g l^–1) to a mineral salts medium containing only glucose as carbon source increased volumetric and specific extracellular glucose oxidase activities by 130% and 50% respectively. With the same medium composition and inoculum size, volumetric and specific extracellular glucose oxidase activities increased more than ten times in bioreactor cultivations compared to shake-flask cultures.     

Production of glucose oxidase using Aspergillus niger and corn steep liquor

Glucose oxidase production was optimized using an isolated strain of Aspergillus niger and an economical nutrient source, corn steep liquor (CSL). The culture produced 580 +/- 30 units/ml of the enzyme using 70 g/l sucrose as the carbon source. Using CSL as the sole nutrient source enzyme synthesis was increased to 640 +/- 36 units/ml. None of the nitrogen sources (nitrates of calcium, sodium, ammonium, potassium and yeast extract, malt extract, and peptone) was beneficial to the enzyme synthesis. Aeration and agitation enhanced enzyme synthesis to 850 +/- 45 units/ml. Glucose oxidase has numerous applications in food industry and clinical fields.     

Purification of glucose oxidase from Aspergillus niger by liquid-liquid cationic reversed micelles extraction

The aim of this work was to select the operating conditions for the extraction and recovery of glucose oxidase (GOX) by reversed micelles from mixtures of commercial enzyme and Aspergillus niger homogenates. For this purpose, the influence of the main operating parameters (pH, surfactant concentration, and presence of cell debris or not) on GOX extraction was investigated at 25 degrees C. Without cell debris, the highest yield of GOX activity recovery (90.8%) was obtained performing (a) the forward extraction in isooctane as solvent and hexanol and butanol as cosolvents at 76/6/18 ratio, pH 7.0, 0.2 M cetyl trimethylammonium bromide as cationic surfactant, and electric conductivity of 5.0 mS cm(-1) and (b) the backward extraction at pH 5.5. Forward and backward extractions furnished comparable results when using raw homogenate, which demonstrates a negligible impact of the presence of cell debris on the process. The highest extraction yield (94%) was obtained under the same forward and backward conditions adopted without cell debris. The promising results of this work suggest that the proposed methodology could be profitably exploited at an industrial level.     

The chemical mechanism of action of glucose oxidase from Aspergillus niger

Glucose oxidase from Aspergillus niger (EC 1.1.3.4) is able to catalyze the oxidation of -D-glucose with p-benzoquinone, methyl-1,4-benzoquinone, 1,2-naphthoquinone, 1,2-naphthoquinone-4-sulfonic acid, potassium ferricyanide, phenazine methosulfate, and 2,6-dichloroindophenol. In this work, the steady-state kinetic parameters, V ₁/K _B , for reactions of these substrates were collected from pH 2.5–8. Further, the molecular models of the enzyme's active site were constructed for the free enzyme in the oxidized state, the complex of -D-glucose with the oxidized enzyme, the complex of reduced enzyme with methyl-1,4-benzoquinone, the reduced enzyme plus 1,2-naphthoquinone-4-sulfonic acid, oxidized enzyme plus reduced 1,2-naphthoquinone-4-sulfonic acid (hydroquinone anion), and oxidized enzyme plus fully reduced 1,2-naphthoquinone-4-sulfonic acid.Combining the steady-state kinetic and structural data, it was concluded that Glu412 bound to His559, in the active site of enzyme, modulates powerfully its catalytic activity by affecting all the rate constants in the reductive and the oxidative half-reaction of the catalytic cycle. His516 is the catalytic base in the oxidative and the reductive part of the catalytic cycle. It was estimated that the pK _a of Glu412 (bound to His559) in the free reduced enzyme is 3.4, and the pK _a of His516 in the free reduced enzyme is 6.9.