A comparative study of immobilized amyloglucosidase in a packed bed reactor and a continuous feed stirred tank reactor

The catalytic activity of amyloglucosidase covalently attached to DEAE-cellulose was studied in a packed bed reactor and a continuous feed stirred tank reactor (CSTR) for the reaction maltose → glucose. At low flow rates mass-transfer limitations in the bed reactor lead to lower conversions for this reactor compared to the CSTR. Simple theoretical expressions for these reactors were compared with the experimental results. There are significant differences between the kinetic parameters and pH profile of the immobilized and free enzyme. The immobilized enzyme also showed greater stability at 50°C than did free amyloglucosidase. The temperature dependence of the reaction rate was the same for immobilized and free enzyme.     

A new method for cell immobilization.

A new method for producing particles and membranes containing immobilized bacteria is presented. These immobilized bacteria display good stability over time making them well suited for use in a packed-bed reactor. Such a reactor is tested as a function of the different parameters of the system. The results are qualitatively similar to those obtained with purified enzyme reactors, but some discrepancies with the plug-flow model are noted. It is necessary to use a more sophisticated model in order to fit the experimental data.     

Limited modifications of soya proteins by immobilized subtilisin: comparison of products from different reactor types

A comparison of different immobilized enzyme reactors has been made for the limited modification of soya storage proteins and the products compared with those from action of the soluble enzyme. Clarified total water extracts of soya protein were subjected to the action of subtilisin in a soluble and immobilized form. The sodium dodecyl sulfate (SDS) electrophoresis patterns of soya proteins modified by enzyme in the two forms differed for unbuffered soya protein at the same pH of 8.0. However, identical patterns could be obtained by a downward adjustment of the pH of soya protein treated with immobilized enzyme. The same SDS electrophoresis pattern could be obtained for a packed column of immobilized enzyme and a well-mixed vessel by buffering. Operation of the column reactor at higher superficial linear velocities (above 1.47 cm/min), higher protein concentrations (8.8% w/v), and prolonged periods (24 h) led to a bed compression attributed to the protein coating of the support.     

Scale-up of flat-plate reactors for enzymatic hydrolysis of fats and oils

To determine the feasibility of continuous enzymatic fat-splitting, immobilized lipase reactors were constructed from alternating layers of enzyme support material and separator screens. Partially purified lipase from Thermomyces lanuginosus was loaded onto the support material at pH 5.5 by irreversible adsorption. Melted edible tallow at 51°C was pumped through the immobilized enzyme layers and swept from the downstream separator screens by buffer recycled from a continuous oil/water separator. Results from continuous operation of 10-layer reactors were compared with data from single-layer reactors. The activity per square centimeter of 10-layer reactors was nearly as much as that of single-layer reactors at the same enzyme loading and oil feed rate. Data were fitted to an empirical mathematical model.     

Kinetic studies on urea hydrolysis by immobilized urease in a batch squeezer and flow reactor

The immobilization of urease on the reticulated polyurethane foam, and the kinetic phenomenon of urea hydrolysis by the resulting immobilized urease in both batch squeezer and circulated flow reactors were studied. Urease was immobilized with bovine serum albumin and glutaraldehyde on polyurethane foam support of 7 to 15 mum thickness. The residual apparent activity of urease after immobilization was about 50%. The good hydrodynamic property and flexibility of polyurethane foam were retained in solution after immobilization. A modified biofilm reactor model was used to describe the kinetic phenomenon of urea hydrolysis in both batch squeezer and circulated flow reactors. The characteristic parameters of the reactor model for both bioreactors were obtained by combining the Rosenbrock optimization method, the Rungs-Kutta method, and the Newton-Raphson method. The best-fit results were in good agreement with the experimental data. This study suggests another application of polyurethane foam in enzyme immobilization and immobilized enzyme reactors, which offers potential for practical applications in various bioreactors. (c) 1992 John Wiley & Sons, Inc.     

On-line determination of glucose and lactate concentrations in animal cell culture based on fibre optic detection of oxygen in flow-injection analysis.

A flow-injection analysis (FIA) system based on fibre optic detection of oxygen consumption using immobilized glucose oxidase (GOD) and lactate oxidase (LOD) is described for the on-line monitoring of glucose and lactate concentrations in animal cell cultures. The consumption of oxygen was determined via dynamic quenching by molecular oxygen of the fluorescence of an indicator. GOD and LOD were immobilized on controlled pore glass (CPG) in enzyme reactors which were directly linked to a specially designed fibre optic flow-through cell covering the oxygen optrode. The system is linear for 0-30 mM glucose, with an r.s.d. of 5% at 30 mM (five measurements) and for 0-30 mM lactate, with an r.s.d. of 5% at 30 mM (five measurements). The enzyme reactors used were stable for more than 4 weeks in continuous operation, and it was possible to analyse up to 20 samples per hour. The system has been successfully applied to the on-line monitoring of glucose and lactate concentrations of an animal cell culture designed for the production of recombinant human antithrombine III (AT-III). Results of the on-line measurement obtained by the FIA system were compared with the off-line results obtained by a glucose and lactate analyser from Yellow Springs Instrument Company (YSI).     

Enzymes immobilized on magnetic carriers: efficient and selective system for protein modification

In order to obtain an economical, efficient and selective system for glycoprotein modification we prepared reactors with immobilized neuraminidase or (and) galactose oxidase. High storage and operational stability of the enzyme reactors was obtained by their immobilization through the carbohydrate parts of the enzyme molecules to hydrazide-modified supports. Magnetic and non-magnetic forms of bead cellulose and poly(HEMA-co-EDMA) microspheres were used for immobilization. These reactors can be used almost universally for the activation of ligands and for labelling of substances having a carbohydrate moiety.     

Flow system for fish freshness determination based on double multi-enzyme reactor electrodes

A double reactor system for the determination of fish and shellfish freshness using the freshness indicator, K-value (K=[(HxR+Hx)/(ATP+ADP+AMP+IMP+HxR+Hx)]x100), was developed, where ATP, ADP, AMP, IMP, HxR and Hx are adenosine triphosphate, adenosine diphosphate, adenosine monophosphate, inosine monophosphate, inosine and hypoxanthine, respectively. The system consisted of a pair of enzyme reactors with an oxygen electrode positioned close to the respective reactor. The enzyme reactor (I) was packed with nucleoside phosphorylase and xanthine oxidase immobilized simultaneously on chitosan beads (immobilized enzyme A). Similarly, the enzyme reactor (II) was packed with immobilized enzyme A and immobilized enzyme B (co-immobilized alkaline phosphatase and adenosine deaminase). Moreover, this reactor consisted of two layers, the enzyme A and enzyme B (1:1). A good correlation was obtained between K values, which were determination by the proposed system and by the HPLC method. One assay could be completed within 5 min. The signal for the determination of K value of fish and shellfish was reproducible within 2.3%. The long-term stability of the enzyme reactors was evaluated at 30 degrees C for 28 days.     

Enzyme activity maintenance in packed-bed reactors via continuous enzyme addition

An operational scheme for using immobilized enzymes in packed-bed reactors that permits operation at a constant throughput rate and constant product quality is described. The scheme used columns operated in series with continuous enzyme addition to compensate for enzyme decay. A mathematical technique was developed to determine the enzyme addition rate, enzyme usage, and enzyme volume in the column system. Operation of columns in series is compared to operation where the flow rate is decreased to compensate for a loss of enzyme activity for both zero-and first-order decay. The analyses indicated that columns in series resulted in better enzyme utilization but larger reactor volumes than parallel reactors with decreasing flow rate.     

Comparative study of controlled pore glass, silica gel and poraver for the immobilization of urease to determine urea in a flow injection conductimetric biosensor system

This study compared the responses of three enzyme reactors containing urease immobilized on three types of solid support, controlled pore glass (CPG), silica gel and Poraver. The evaluation of each enzyme reactor column was done in a flow injection conductimetric system. When urea in the sample solution passed though the enzyme reactor, urease catalysed the hydrolysis of urea into charged products. A lab-built conductivity meter was used to measure the increase in conductivity of the solution. The responses of the enzyme reactor column with urease immobilized on CPG and silica gel were similar and were much higher than that of Poraver. Both CPG and silica gel reactor columns gave the same limit of detection, 0.5 mM, and the response was still linear up to 150mM. The analysis time was 4-5 min per sample. The enzyme reactor column with urease immobilized on CPG gave a slightly better sensitivity, 4% higher than the reactor with silica gel. The life time of the immobilized urease on CPG and silica gel were more than 310h operation time (used intermittently over 7 months). Good agreement was obtained when urea concentrations of human serum samples determined by the flow injection conductimetric biosensor system was compared to the conventional methods (Fearon and Berthelot reactions). These were statistically shown using the regression line and Wilcoxon signed rank tests. The results showed that the reactor with urease immobilized on silica gel had the same efficiency as the reactor with urease immobilized on CPG.     

Effect of immobilized enzyme deactivation in fixed- and fluid-bed reactors

A two-parameter theoretical model is developed to evaluate the effect of immobilized enzyme deactivation on substrate conversion in fixed- and fluid-bed reactors under diffusion-free conditions. The method describes a simple reaction in which three different immobilized enzyme deactivation forms are considered, and an expression is developed to evaluate the effect of immobilized enzyme deactivation on yield in a consecutive reaction. Comparison of reactor performances for the two reactor types reduces to a comparison of the appropriate dimensionless parameters. The practical implications of the development are illustrated through an example.     

Countercurrent multistage fluidized bed reactor for immobilized biocatalysts: I. Modeling and simulation

For the application of immobilized enzymes, fixed bed reactors are used almost exclusively. Fixed bed reactors have specific disadvantages, especially for processes with a deactivating catalyst. Therefore, we have studied a novel reactor type with continuous transport of the immobilized biocatalyst. Flow of biocatalyst is countercurrent to the substrate solution. Because of a stagewise reactor design, back-mixing of biocatalyst is very limited and transport is nearly plug flow. The reactor operates at a constant flow rate and conversion, due to constant holdup of catalytic activity. The reactor performance is compared with a configuration of fixed bed reactors. For reactions in the first-order regime, enzyme requirements in this new reactor are slightly less than for fixed bed processes. The multistage fluidized bed appears to be an attractive reactor design to use biocatalyst to a low residual activity. However, nonuniformity of the particles might affect plug flow transport of the biocatalyst. A laboratory scale reactor and experiments are described in Part II(1) of this series. Hydrodynamic design aspects of a multistage fluidized bed are discussed in more detail in Part III.(2).     

The performance of immobilized glucose isomerase supported by shrimp chitin in various types of reactors

Five different types of reactors were employed for glucose isomerization using shrimp shell as the support on which to immobilize the glucose isomerase. The Michaelis-Menten constants and effective diffusivity of glucose in the immobilized enzyme bed were experimentally determined and used in a theoretical analysis of the radial-flow reactor. The fractional conversions of the radial-flow, fluidizedbed, and packed-bed reactors with the same -residence time were found experimentally to be almost the same. This result reveals that the use of radial-flow and fluidized-bed reactors for this immobilized enzyme system is highly feasible.     

Design of immobilized enzyme reactors for the continuous production of fructose syrup from whey permeate

Biocatalyst inactivation is inherent to continuous operation of immobilized enzyme reactors, meaning that a strategy must exist to ensure a production of uniform quality and constant throughput. Flow rate can be profiled to compensate for enzyme inactivation maintaining substrate conversion constant. Throughput can be maintained within specified margins of variation by using several reactors operating in parallel but displaced in time. Enzyme inactivation has been usually modeled under non-reactive conditions, leaving aside the effect of substrate and products on enzyme stability. Results are presented for the design of enzyme reactors under the above operational strategy, considering first-order biocatalyst inactivation kinetics modulated by substrate and products. The continuous production of hydrolyzed-isomerized whey permeate with immobilized lactase and glucose isomerase in sequential packed-bed reactors is used as a case study. Kinetic and inactivation parameters for immobilized lactase have been determined by the authors; those for glucose isomerase were taken from the literature. Except for lactose, all other substrates and products were positive modulators of enzyme stability. Reactor design was done by iteration since it depends on enzyme inactivation kinetics. Reactor performance was determined based on a preliminary design considering non-modulated first-order inactivation kinetics and confronted to such pattern. The new pattern of inactivation was then used to redesign the reactor and the process repeated until reactor performance (considering modulation) matched the assumed pattern of inactivation. Convergence was very fast and only two iterations were needed.     

Tyrosine hydroxylase activity of immobilized tyrosinase on enzacryl-AA and CPG-AA supports: Stabilization and properties

Frog epidermis tyrosinase has been immobilized on Enzacryl-AA (a polyacrylamide-based support) and CPG(zirclad)-Arylamine (a controlled pore glass support) in order to stabilize the tyrosine hydroxylase activity of the enzyme; in this way, the immobilized enzyme could be used to synthesize L-dopa from L-tyrosine. The activity immobilization yield Y(IME) (act) (higher than 86%), coupling efficiency (up to 90%), storage stability (no loss in 120 days), and reaction stability (t(1/2) was higher than 20 h in column reactors) were measured for tyrosinase after its immobilization. The results showed a noticeable improvement (in immobilization yield, coupling efficiency, and storage and operational stabilities) over previous reports in which tyrosinase was immobilized for L-dopa production. The activity and stability of immobilized enzyme preparations working in three different reactor types have been compared when used in equivalent conditions with respect to a new proposed parameter of the reactor (R(p)), which allows different reactor configurations to be related to the productivity of the reactor during its useful life time. The characteristic reaction inactivation which soluble tyrosinase shows after a short reaction time has been avoided by immobilization, and the stabilization was enhanced by the presence of ascorbate. However, another inactivation process appeared after a prolonged use of the immobilized enzyme. The effects of reactor type and operating conditions on immobilized enzyme activity and stability are discussed.     

Diffusion and chemical reaction rates with nonuniform enzyme distribution: an experimental approach

The study of the effects of nonuniform distributions of immobilized beta-galactosidase on the overall reaction rate of the hydrolysis of lactose are presented. Diffusion inside the particles has been characterized by measuring the diffusion rates of two beta-galactosidase substrates: lactose and ONPG in a commercial silica-alumina support. Effective diffusivities have been determined by the chromatographic method under inert conditions. The results obtained for tortuosity can be explained assuming that the transport only takes place in the macropores. The distribution of the immobilized enzyme has been measured by means of confocal microscopy technique. The enzyme has been tagged with FITC and immobilized in particles of different diameters, the internal local concentrations of the enzyme have been determined with the aid of an image computer program. As expected, a more nonuniform internal profile of the enzyme was found when the particle diameter was bigger. Experiments under reaction conditions were carried out in batch reactors using lactose and ONPG as substrates and particles of the immobilized beta-galactosidase of different diameter (1 x 10(-4) to 5 x 10(-3) m) as catalyst, employing a temperature of 40 degrees C for lactose and 25 and 40 degrees C for ONPG, respectively. The mass balance inside the particle for the substrates has been solved for the internal profiles of the immobilized enzyme inside particles of different size and the enzymatic reactions considered. The calculated and the experimental effectiveness factor values were similar when particles under 2.75 x 10(-3) m in diameter were employed. For the same Thiele modulus, a particle with nonuniform distribution of enzyme showed a higher effectiveness as a catalyst than particles with a more uniform distribution.     

Characterization of CIM monoliths as enzyme reactors

The immobilization of the enzymes citrate lyase, malate dehydrogenase, isocitrate dehydrogenase and lactate dehydrogenase to CIM monolithic supports was performed. The long-term stability, reproducibility, and linear response range of the immobilized enzyme reactors were investigated along with the determination of the kinetic behavior of the enzymes immobilized on the CIM monoliths. The Michaelis-Menten constant K(m) and the turnover number k(3) of the immobilized enzymes were found to be flow-unaffected. Furthermore, the K(m) values of the soluble and immobilized enzyme were found to be comparable. Both facts indicate the absence of a diffusional limitation in immobilized CIM enzyme reactors.     

Use of monoclonal anti-enzyme antibodies for analytical purposes.

This review discusses the analytical applications of monoclonal antibodies specific for enzymes. One important, but not well-studied, application of these monoclonal antibodies is their use in immobilizing enzymes on solid supports. This method is based on binding the enzymes to an immobilized antibody through the antigen binding site of the antibody. Enzymes immobilized this way retain much of their activity. The utility of immobilized enzyme reactors prepared by immobilizing the enzymes through antibodies is demonstrated by using them in the determination of acetylcholine and choline in brain tissue extracts. Currently available methods for immobilizing antibodies and enzymes are reviewed. Other issues discussed in this review include the problems and advantages of immobilized enzyme reactors, especially when used in conjunction with HPLC. In addition, the applications of monoclonal antibodies for the detection and measurement of enzymes and their isoforms are summarized.     

Solubilization and concentration of carbon dioxide: novel spray reactors with immobilized carbonic anhydrase

Novel spray reactors are described that employ immobilized biocatalyst (carbonic anhydrase), enabling concentration and solubilization of emitted CO(2) by allowing catalytic contact with water spray. The reactors were fed with simulated emission gas. The performance of the reactors was investigated with respect to operation variable: emission flow rate; gas composition in the emission stream; water flow rate; area-to-volume ratio of immobilized reactor core; and the enzyme load within the core. The reactors were also investigated for pressure drop and extractability of CO(2) from the emission with single vs. multiple reactors (of combined equal volume). The biotechnological process of solubilization and concentration of CO(2) from emission exhausts or streams occurring in the spray reactors could be coupled for further biochemical/chemical conversion of the concentrated CO(2).     

A simple kinetic model for the hydrolysis of α-d-glucans using glucoamylase immobilized on titanium (IV) activated porous silica

A simple kinetic model which describes the hydrolysis of α-d-glucans by immobilized glucoamylase (exo-1,4-d-glucosidase, EC 3.2.1.3) is reported. The hydrolysis of starch, amylose, amylopectin, maltose and 40DE starch hydrolysates using glucoamylase immobilized on alkylamine derivatives of titanium(IV) activated porous silica are described by a kinetic model based on Langmuir-Hinshelwood kinetics. This model involves enzyme kinetics with or without product inhibition and reverse reactions as well as mass transfer and diffusion effects in immobilized enzyme reactors. The results of other authors are also interpreted by the model developed in this article.