Macrokinetics and operational stability of immobilized glucose oxidase and catalase

Glucose oxidation by immobilized glucose oxidase (GlO) and catalase (Cat) has been investigated in batch and continuous reactions for operational studies. The macrokinetics of the process depend on coupled reaction steps and diffusion rates. The problem may be approximated by a simple pseudohomogeneous model taking into account both substrates of glucose oxidase and the intermediate reaction product H₂O₂. The effectiveness of both enzymes is enhanced in the coupled reaction path, the overall effectiveness nevertheless is very low. H₂O₂ causes the inactivation of both GlO and Cat. The rates of deactivation depend on the oxidation rates of glucose that give different quasistationary levels of H₂O₂ concentration. As a first approximation, the deactivation rates may be described by first-order reactions with respect to H₂O₂.     

Deactivation studies of immobilized glucose oxidase

Studies have been performed in a tubular flow reactor to characterize the deactivation of immobilized glucose oxidase. The effects of oxygen concentration in the range of 0.09 to 0.467mM and hydrogen peroxide concentrations in the range of 0.1 to 10mM were studied. A simple mathematical model assuming first-order reaction and deactivation was found to describe the deactivation behavior adequately. The deactivation rate constant was found to increase with increasing levels of feed oxygen. Hydrogen peroxide was found to deactivate the enzyme severely and the deactivation rate constants were higher than those for oxygen deactivation. The influence of external and internal diffusion effects on the deactivation rate constant were examined. Although diffusional restrictions were negligible for oxygen transfer to the pellet, they were significant for transfer of hydrogen peroxide to the bulk stream. Increasing deactivation rates. Severe internal diffusion limitations were observed for the glucose oxidase system. However, for particle sizes in the range of 500 to 2000 μm, no effect on the rate of deactivation of the enzyme was observed.     

Performance of rotating packed disk reactor with immobilized glucose oxidase

Summary Reactor performance was studied to investigate whether a rotating packed disk reactor (RPDR) can be used for the enzymatic oxidation of biochemicals. The disks were packed with calcium alginate beads with immobilized glucose oxidase and catalase, which catalyze the reaction of glucose and oxygen. The production rate of gluconic acid increased with the speed of rotation and the bulk flow rate. An optimum submergence for maximum productivity existed.     

A new method to determine active enzyme distribution, effective diffusivity, rate constant for main reaction and rate constant for deactivation

A new method is presented to determine (1) the rate constant for the main reaction, (2) the rate constant for deactivation, (3) the effective diffusivity, and (4) the active enzyme distribution within a porous solid support by utilizing data of bulk substrate concentration versus time in a continuous stirred basket reactor. The method relies on an assumption of parallel deactivation mechanism with strong pore diffusional resistance with respect to substrate species. The data of hydrogen peroxide-immobilized catalase published in the literature are used to demonstrate the theory. A parameter determination procedure is also presented.     

Effect of enzyme-matrix composition on potentiometric response to glucose using glucose oxidase immobilized on platinum

Glucose oxidase (beta-D-glucose:oxygen 1-oxidoreductase, EC 1.1.3.4) was immobilized in a crosslinked matrix of bovine serum albumin, catalase, glucose oxidase and glutaraldehyde on platinum foil. When placed in glucose solution, this enzyme-electrode elicited a potentiometric response that varied with the changes in glucose concentration. The immobilized glucose oxidase was present at 7.4-10.1 micrograms enzyme protein/ml of matrix, as determined with 125I-labelled enzyme. The coupled enzyme activity was stable over 120 h; however, the apparent activity of the immobilized glucose oxidase was markedly less than that for the same amount of enzyme free in solution. This indicated a significant level of diffusional resistance within the enzyme-matrix. The potentiometric response to glucose increased significantly as either the thickness of the enzyme-matrix or the glutaraldehyde content was reduced; this also was attributed to diffusional effects. Several enzyme-electrodes, constructed without exogenous catalase and with different amounts of glucose oxidase, showed greater sensitivity in potentiometric response at low glucose oxidase loadings. These results are consistent with the hypothesis that the potentiometric response arises from an interfacial reaction involving a hydrogen peroxide redox couple at a platinum surface. The data also suggest that an optimum range of hydrogen peroxide concentration exists for maximum electrode sensitivity.     

General theory of determining intraparticle active immobilized enzyme distribution and rate parameters

A general theory is presented in this article for determining the intrinsic rate constants for the main reaction and deactivation reaction, the effective diffusivity of the substrate, and the active enzyme distribution within porous solid supports from deactivation study of a continuous stirred-basket reactor (CSBR). For the parallel deactivation five reaction kinetics are considered: (a) Michaelis-Menten, (b) substrate inhibition, (c) product inhibition (competitive), (d) product inhibition (anticompetitive), and (e) zero-order kinetics. The experimental results of the system of hydrogen-peroxide-immobilized catalase on controlled-pore glass particles are analyzed to demonstrate the application of the theory developed for parallel deactivation of active immobilized enzyme (IME). For series deactivation only first-order kinetics is treated, and a numerical procedure is proposed to deter mine the rate parameters and the internal active enzyme distribution. The experimental data of the system of glucose-immobilized glucose oxidase on silica-alumina and controlled-pore glass particles are used to verify the theory.     

Immobilized Enzyme Three-Phase Reactors for Oxidation of Cephalosporin C

The enzymatic oxidation of Cephalosporin C (CEPHC) was catalyzed by D-aminoacid oxidase, from the red yeast Trigonopsis variabilis, immobilized on Duolite A365. The study was performed in two different three phase bioreactors, gas-liquid-solid (immobilized enzyme): the fluidized-bed batch reactor, fed continuously with oxygen and discontinuously with CEPHC, and the UF-membrane reactor continuously fed with both substrates. Only the first reactor allowed significant product yield (>70%) while the second was a very useful tool for laboratory investigation of both bioconversion kinetics and enzyme stability.

Optimum reaction temperature was 15d`C for the control of CEPHC spontaneous degradation (roughly 15% in 30 h), and enzyme deactivation (half-life greater than 30 h). Immobilization improved (one order of magnitude longer half-life) enzyme resistance to mechanical stresses induced by liquid stirring and gas bubbling. Roughly 0.04g of CEPHC was adsorbed per gram of enzyme carrier. The limiting step in oxygen transfer was the gas to liquid transport. In order to attain kinetic control of the bioconversion the mildest conditions were atmospheric gas pressure and oxygen flow rate equal to 2 × 10 ²NmL/s per mL of liquid phase.     

Application of the theory of oxygen transfer: determination of the Michaelis constant of glucose oxidase with respect to oxygen]

The oxidation of beta-D-glucose with glucose oxidase generally requires oxygen, which, under normal conditions is present at low concentrations in the reaction medium. Experiments show that glucose oxidase is no longer saturated by oxygen at enzyme concentrations greater than 0.4 mg.ml1. This is due to the decrease in the oxygen concentration of the solution. The value of the oxygen mass transfer coefficients and dissolved oxygen concentrations are determined. These dissolved oxygen concentrations are found to correlate with direct measurements with an oxygen electrode. From this, the Michaelis constant of glucose oxidase for oxygen is calculated. These experiments also show that oxygen is a limiting factor for this reaction.     

Continuous steroid biotransformations in microchannel reactors

The use of microchannel reactor based technologies within the scope of bioprocesses as process intensification and production platforms is gaining momentum. Such trend can be ascribed a particular set of characteristics of microchannel reactors, namely the enhanced mass and heat transfer, combined with easier handling and smaller volumes required, as compared to traditional reactors. In the present work, a continuous production process of 4-cholesten-3-one by the enzymatic oxidation of cholesterol without the formation of any by-product was assessed. The production was carried out within Y-shaped microchannel reactors in an aqueous-organic two-phase system. Substrate was delivered from the organic phase to aqueous phase containing cholesterol oxidase and the product formed partitions back to the organic phase. The aqueous phase was then forced through a plug-flow reactor, containing immobilized catalase. This step aimed at the reduction of hydrogen peroxide formed as a by-product during cholesterol oxidation, to avoid cholesterol oxidase deactivation due to said by-product. This setup was compared with traditional reactors and modes of operation. The results showed that microchannel reactor geometry outperformed traditional stirred tank and plug-flow reactors reaching similar conversion yields at reduced residence time. Coupling the plug-flow reactor containing catalase enabled aqueous phase reuse with maintenance of 30% catalytic activity of cholesterol oxidase while eliminating hydrogen peroxide. A final production of 36 m of cholestenone was reached after 300 hours of operation.     

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.     

Oxidation of lactose to lactobionic acid by a Microdochium nivale carbohydrate oxidase: kinetics and operational stability

Oxidation of lactose to lactobionic acid by a Microdochium nivale carbohydrate oxidase was studied. The K(m)-value for lactose, obtained by a traditional enzymatic assay, was 0.066 mM at pH 6.4 and 38 degrees C. The effect of oxygen on the enzymatic rate of reaction as well as the operational stability of the enzyme was studied by performing reactions at constant pH and temperature in a stirred tank reactor. Catalase was included in all reactions to avoid inhibition and deactivation of the oxidase by hydrogen peroxide. At pH 6.4 and 38 degrees C, K(m) for oxygen was 0.97 mM, while the catalytical rate constant, k(cat), was 94 s(-1). Furthermore, we found that the operational stability of the oxidase was dependent on the type of base used for neutralization of the acid produced. Thus, when 2 M NaOH was used for neutralization of a reaction medium containing 50 mM phosphate buffer, significant deactivation of the oxidase was observed. Also, we found that the oxidase was protected against deactivation by base at high lactose concentrations. A simple model is proposed to explain the obtained results.     

Gluconic acid production by an mobilized glucose oxidase reactor with electrochemical regeneration of an artificial electron acceptor

A reactor, using the enzymatic electrocatalysis scheme, was developed on a laboratory preparative scale for the catalytic oxidation of glucose into gluconic acid. Glucose oxidase was directly immobilized on the surface of a carbon felt electrode and a solution of glucose and benzo-quinone passed through the electrode in order to regenerate the electron acceptor. The reactor was able to produce continuously 1.5 g gluconate/h with a catalytic current of 0.4 A. This gave a high productivity ca. 100 g/h/L reactor. A one-dimensional model was developed which demonstrated the efficiency of coupling between enzymatic and electrochemical reactions due to the proximity of the two reaction sites. For example the catalytic current was practically independent of mass transfer parameters. The operational stability of immobilized glucose oxidase was increased 50 times at least when electroregenerated benzoquinone was used as oxidant instead of oxygen.     

Batch production of high-content fructo-oligosaccharides from sucrose by the mixed-enzyme system of β-fructofuranosidase and glucose oxidase

The production of high-content fructo-oligosaccharides from sucrose by the mixed-enzyme system of β-fructofuranosidase and glucose oxidase was investigated. The mixed-enzyme reaction was carried out in a stirred tank reactor containing 0.7 l of sucrose solution with coupled β-fructofuranosidase and glucose oxidase for 25 h. The optimum conditions for the mixed-enzyme reaction were as follows: pH, 5.5; temperature, 40°C; sucrose concentration, 400 g/l; agitation speed, 550 rpm; oxygen flow rate, 0.7 l/min; enzyme dosage, 10 units of β-fructofuranosidase with the combination of 15 units of glucose oxidase per gram sucrose. Under optimum conditions, high-content fructo-oligosaccharides up to 98% were obtained with complete consumption of sucrose and glucose by the mixed-enzyme system. Compared with the fructo-oligosaccharides produced by the β-fructofuranosidase, the high-content fructo-oligosaccharides produced by the mixed-enzyme system showed a significant difference with respect to sugar composition; i.e., a higher content of nystose was accumulated and only a trace amount of fructofuranosyl nystose was detected.     

Analysis of the coupled transport, reaction, and deactivation phenomena in the immobilized glucose oxidase and catalase system.

In a previous paper, the overall or macrokinetics of the immobilized glucose oxidase--catalase system has been presented. In this paper a detailed analysis of the interaction of diffusion and reaction in this system will be presented. The mathematical treatment includes two consecutive reactions with two-substrate kinetics. Furthermore, the deactivation of both enzymes due to the intermediate product peroxide is taken into account. The predicted results suggest that the efficiency of the glucose oxidase reaction depends on the concentration ranges of the two substrates. Furthermore, the external mass-transfer rate may cause a shift from glucose limitation to oxygen limitation. The efficiency of the coupled system is always higher than that predicted for the uncoupled reaction path. The calculations show that the economics of the coupled system depend a great deal on the deactivation of the enzymes.     

Efficient Expression of Peroxidatic Activity of Catalase in the Coupled System with Glucose Oxidase—a model of Yeast Peroxisomes

Catalase functioned exclusively to degrade hydrogen peroxide in a reaction mixture containing methanol and hydrogen peroxide, while, when the enzyme was coupled with glucose oxidase, successful conversion of methanol to formaldehyde occurred at the optimized ratio of glucose oxidase to catalase: activity, 1.0 × 10 ^-3; number of molecules, 1.3; protein content, 1. These values in the coupled system were very similar to the ratio of alcohol oxidase to catalase in peroxisomes, one of the subcellular organelles from a methanol-assimilating yeast, Kloeckera sp. 2201, in which these enzymes were coupled to metabolize methanol efficiently. The presence of the optimum ratio in the coupled system in vitro was confirmed by the kinetic analysis of the expression of the peroxidatic activity of catalase coupled with glucose oxidase. Construction of the immobilized system of the coupled enzymes at the optimum ratio demonstrated that the oxidation of methanol through the peroxidatic function of catalase could be continuously and stably operated, the results indicating the usefulness of the system as a model of yeast peroxisomes. Thus, the coupled reaction with glucose oxidase brought out the latent function of catalase, which could not be expected in the system including only catalase.     

Enzymatic method for measuring the absolute value of oxygen concentration

An enzymatic method for measuring the absolute concentration of oxygen in aqueous solutions, using 4-hydroxybenzoate 3-monooxygenase and glucose oxidase, is described. The monooxygenase is used for quantitative oxidation of 4-hydroxybenzoate and NADPH with oxygen into 3,4-dihydroxybenzoate and NADP+; the amount of oxygen can be measured as the amount of NADPH decreased by the reaction. The monooxygenase reaction is performed in a syringe, a closed system. After the completion of the monooxygenase reaction, glucose oxidase is added to the assay solution to consume the oxygen from the atmosphere; this enables us to measure the NADPH concentration in the solution spectrophotometrically in an open system and to check the anaerobicity of closed systems. The oxygen concentrations at 25 degrees C of oxygen-saturated and air-saturated water were 1.10 and 0.23 mM, respectively. The value for argon-bubbled water was zero within the experimental error; this justifies the assay system. Thus, it is shown that a sample containing 8 microM-1.1 mM oxygen can be measured by this method.     

ON THE INACTIVATION OF ASCORBIC ACID OXIDASE

1. In the absence of protective agents, highly purified ascorbic acid oxidase is rapidly inactivated during the enzymatic oxidation of ascorbic acid under optimum experimental conditions. This inactivation, called reaction inactivation to distinguish it from the loss in enzyme activity that frequently occurs in diluted solutions of the oxidase prior to the reaction, is indicated by incomplete oxidation of the ascorbic acid as measured by oxygen uptake; i.e., "inactivation totals." 2. A minor portion of the reaction inactivation appears to be due to environmental factors such as rate of shaking of the manometers, pH of the system, substrate concentration, and oxidase concentration. The presence of inert protein (gelatin) in the system ameliorates the environmental inactivation to a considerable extent, and variation of the above factors in the presence of gelatin has much less effect on the inactivation totals than in the absence of gelatin. 3. A major portion of the reaction inactivation of the oxidase appears to be due to some factor inherent in the ascorbic acid-ascorbic acid oxidase-oxygen system, possibly a highly reactive "redox" form of oxygen other than H₂O₂ or H₂O. The inactivation cannot be attributed to dehydroascorbic acid, the oxidation product of ascorbic acid. 4. Small amounts of native catalase, native peroxidase, native or denatured methemoglobin, and hemin when added to the system, markedly protect the oxidase against inactivation. Cytochrome c has no such protective action. Likewise proteins such as egg albumin, gelatin, denatured catalase, or denatured peroxidase show no such protective action. 5. None of the protective agents mentioned above affect the initial rate of oxygen uptake or change the total oxygen absorbed for complete oxidation of the ascorbic acid, and hence do not act by removal of hydrogen peroxide, per se. 6. Sodium azide and hydroxylamine hydrochloride which inhibit catalase and peroxidase activity also inhibit the protective action of these iron-porphyrin enzymes.     

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.     

An immobilised catalase peroxidase from the alkalothermophilic Bacillus SF for the treatment of textile-bleaching effluents

A catalase peroxidase (CP) from the newly isolated Bacillus SF was used to treat textile-bleaching effluents. The enzyme was stable at high pH values and temperatures, but was more sensitive to deactivation by hydrogen peroxide than monofunctional catalases. Based on the Michaelis-Menten kinetics of the CP, a model was developed to describe its deactivation characteristics. The enzyme was immobilised on various alumina-based carrier materials with different shapes and the specific activity increased with the porosity of the carrier. The shape of the carrier had an important influence on the release of oxygen formed during the catalase reaction from the packed-bed reactor and Novalox saddles were found to be the most suitable shape. Bleaching effluent was treated in a horizontal packed-bed reactor containing 10 kg of the immobilised CP at a textile-finishing company. The treated liquid (500 l) was reused within the company for dyeing fabrics with various dyes, resulting in acceptable colour differences of below Delta E*=1.0 for all dyes.