Immobilization of enzymes on activated carbon: Properties of immobilized glucoamylase,glucose oxidase,and gluconolactonase

Apparent kinetics and pH–activity relationships have been determined for glucoamylase and glucose oxidase immobilized on activated carbon using a diimide method. Reaction rate expressions of Michaelis–Menten form adequately approximate the observed kinetics for both enzyme preparations over the ranges of substrate concentrations considered. Influences of external mass transfer as well as substrate and product adsorption on interpretation of the experimental data have been examined. Immobilization of a glucose oxidase–gluconolactonase enzyme mixture has been found to increase substantially the ratio of gluconolactonase to glucose oxidase activities compared to the corresponding activity ratio for these enzymes in solution.     

Enzyme immobilization on a low-cost magnetic support: kinetic studies on immobilized and coimmobilized glucose oxidase and glucoamylase.

Glucose oxidase (GOx) and glucoamylase (GA) were immobilized and coimmobilized through their carbohydrate moieties onto polyethyleneimine-coated magnetite crosslinked with glutaraldehyde and derivatized with adipic dihydrazide. The carbohydrates were oxidized with sodium periodate, and at optimal concentration, their Vm increased up to 18% for GOx and up to 16% for GA. After immobilization, a remaining activity as high as 88% and 70% for GA with maltose and maltodextrin respectively as substrates was obtained, independently of the particle loading. On the contrary, the remaining activity of GOx strongly decreased at high particle loading. Nevertheless, half of its initial activity was recovered at low loading and was not significantly affected when GA was coimmobilized by saturating the reactive groups left on the particle. The Vm of both immobilized enzymes was improved by crosslinking their carbohydrates with adipic dihydrazide, a treatment which allows further coimmobilization of the other enzyme on a second layer.     

Immobilization of glycoenzymes through carbohydrate side chains.

Glucoamylase, peroxidase, glucose oxidase, and carboxypeptidase Y were covalently bound to water-insoluble supports through their carbohydrate side chains. Two approaches were used. First, the carbohydrate portions of the enzymes were oxidized with periodate to generate aldehyde groups. Treatment with amines (ethylenediamine or glycyltyrosine) and borohydride provided groups through which the protein could be immobilized. Ethylenediamine was attached to glucoamylase, peroxidase, glucose oxidase, and carboxypeptidase Y to the extent of 24, 20, 30, and 15 mol/mol of enzyme, respectively. These derivatives were coupled to an aminocaproate adduct of CL-Sepharose via an N-hydroxysuccinimide ester or to CNBr-activated Sepharose. Coupling yields were in the range of 37–50%. Retained activities of the bound aminoalkyl-enzymes were 41% (glucoamylase), 79% (peroxidase), 71% (glucose oxidase), 83% (carboxypeptidase Y). A glycyltyrosine derivative of carboxypeptidase Y was bound to diazotized arylamine-glass. Coupling yield was 42% and retained esterase activity was 84%. In the second approach, the enzyme was adsorbed to immobilized concanavalin A and the complex was crosslinked. Adsorption of carboxypeptidase Y on immobilized concanavalin A followed by crosslinking with glutaraldehyde was also effective. The bound enzyme retained 96% of the native esterase activity and showed very good operational stability.     

Immobilization of enzymes in porous supports: Effects of support-enzyme solution contacting

Proteins have been immobilized in porous support particles held in a fixed-bed reactor through which protein solution is continuously circulated. Changing the recirculation flow rate alters the observed immobilization kinetics and the maximum enzyme loading which can be achieved for glucose oxidase and glucoamylase on carbodiimide-treated activated carbon and for glucoamylase immobilized on CNBr-Sepharose 4B. Direct microscopic examination of FITC-labelled protein in sectioned Sepharose particles and indirect activity-loading studies with activated carbon-enzyme conjugates all indicate that immobilized enzyme is increasingly localized near the outer surface of the support particles at larger recirculation flow rates. Restricted diffusion of enzymes may be implicated in this phenomenon. These contacting effects may be significant considerations in the scaleup of processes for protein impregnation in porous supports, since apparent activity and stability of the final preparation depend on internal protein distribution.     

The effect of methylacrylate on the activity of glucomylase immobilized on granular polyacrylonitrile

Glucoamylase was immobilized on granular polyacrylonitrile (PAN) and the optimum condition in its immobilization reaction was determined. The effect of the ratio of the imidoester and methylester to the total cyanogen on the activity of the immobilized enzyme was studied. The activity of the immobilized enzyme increased in proportion to the molar number of imidoester and decreased with that of methylester. The K(m) and V(m) values of immobilized glucoamylase which were prepared at various conditions of immobilization were determined. There were opposite trends in K(m)S between glucoamylase immobilized on imidoester-rich support and immobilized on methylester in the support, evidenced as functions of temperature. This suggests that opposite charges in the support, produced by heat deformation of PAN by hydrolysis of methylester, were an influence on the apparent K(m) of immobilized glucoamylase, besides the diffusional limitation.     

Preparation and properties of proteases immobilized on anion exchange resin with glutaraldehyde

High activity alkaline protease was obtained when the enzyme was immobilized on Dowex MWA-1 (mesh 20–50) with 10% glutaraldehyde in chilled phosphate buffer (M/15, pH 6.5). Activity yields of the protease and rennet were 27 and 29, respectively. The highest activities appeared at 60°C, pH 10 for alkaline protease and 50°C, pH 4.0 for rennet. The properties of both proteases were not essentially changed by the immobilization except that the K_m values of both enzymes were increased about tenfold as a result of immobilization. Both proteases in the immobilized state were more stable than those in the free state at 60°C. Other peptide hydrolases, β-galactosidase, invertase, and glucoamylase, were successfully immobilized with high activities, but lipase, hexokinase, glucose-6-phosphate dehydrogenase, and xanthine oxidase became inactive.     

Immobilization of enzymes on chitin and chitosan

During the last few years, d-glucose isomerase, glucoamylase, β-d-galactosidase (lactase), β-d-glucosidase, d-glucose oxidase, AMP deaminase, urease, pronase, subtilisin, trypsin, papain, alkaline phosphatase, acid phosphatase, pepsin, chymotrypsin and lysozyme have been immobilized on chitin and on some of its derivatives, mainly with glutaraldehyde. The preparation and performances of the immobilized enzymes are described.     

Immobilization of glucoamylase and glucose oxidase in activated carbon: effects of particle size and immobilization conditions on enzyme activity and effectiveness

Glucoamylase and glucose oxidase have been immobilized on carbodiimide-treated activated carbon particles of various sizes. Loading data indicate nonuniform distribution of immobilized enzyme within the porous support particles. Catalysts with different enzyme loading and overall activities have been prepared by varying enzyme concentration in the immobilizing solution. Analysis of these results by a new method based entirely upon experimentally observable catalyst properties indicates that intrinsic catalytic activity is reduced by immobilization of both enzymes. Immobilized glucoamylase intrinsic activity decreases with increasing enzyme loading, and similar behavior is suggested by immobilized glucose oxidase data analysis. The overall activity data interpretation method should prove useful in other immobilized enzyme characterization research, especially in situations where the intraparticle distribution of immobilized enzyme is nonuniform and unknown.     

Immobilization of enzymes by radiopolymerization of acrylamide

A new and simple method for immobilization of enzymes by the aerobic radio-polymerization of acrylamide was developed. Irradiation treatment of acrylamide in the frozen state produces a spongy immobilized enzyme membrane without the addition of carriers. Aerobic polymerization yields of acrylamide in the frozen state were increased by the addition of starch and also by lyophilization. Glucose oxidase (activity recovery was 12.3–33.7%), invertase (69.2%), D -amono acid oxidase (25.0–70.5%), aminoacylase (39.2–43.7%), mold α-amylase (18.0%), malt β-amylase (4.1%), glucoamylase (6.5%), alkaline protease (5.3%), and neutral protease (10.5%) were immobilized by this method. Invertase entrapped by this method had a wider optium pH range and was active at higher temperatures.     

Enhancement of starch conversion efficiency with free and immobilized pullulanase and alpha-1,4-glucosidase

Glucoamylase and pullulanase were immobilized on reconstituted bovine-hide collagen membranes using the covalent azide linkage method. A pretanning step was incorporated into the immobilization procedure to enable the support matrix to resist proteolytic activity while accommodating an operating temperature of 50 degrees C. The immobilized glucoamylase and pullulanase activities were 0.91 and 0.022 mg dextrose equivalent (DE) min(-1) cm(-2) of membrane, respectively. Immobilized glucoamylase had a half-life of 50 days while the immobilized pullulanase had a half-life of 7 days. This is a considerably improved stability over that reported by other researchers. The enzymes were studied in their free and immobilized forms on a variety of starch substrates including waxy maize, a material which contains 80% alpha-1-6-glucosidic linkages. Substrate concentrations ranged from 1% to a typical commercial concentration of 30%. Conversion efficiencies of 90-92% DE were obtained with free and immobilized glucoamylase preparations. Conversion enhancements of 4-5 mg of DE above this level were obtained by the use of pullulanase in its free or immobilized forms. Close examination of free pullulanase stability as a function of pH indicated improved thermal stability at higher pH values. At 50 degrees C and pH 5.0, the free enzyme was inactivated after 24 h. At pH 7.0, the enzyme still possessed one-half its activity after 72 h. Studies were conducted in both batch and continuous total recycle reactors. All experiments were conducted at 50 degrees C. Experiments conducted with coimmobilized enzymes proved quite promising. Levels of conversion equivalent to those obtained with the individually immobilized enzymes were realized.     

Thermal Stability of Immobilized Glucoamylase Entrapped in Polyacrylamide Gels and Bound to SP-Sephadex C–50

Glucoamylase[α-1,4: 1,6-glucan-4: 6-glucohydroease, EC 3.2.1.3] from Rhizopus niveus was entrapped in polyacrylamide gels and adsorbed onto SP-Sephadex C–50 to elucidate the thermostability mechanism of immobilized enzymes. The thermal stability of immobilized glucoamylase entrapped in polyacrylamide gels was enhanced slightly compared with glucoamylase in free solution, and was independent of the acrylamide monomer concentration and N, N′-methylene-bis (acrylamide) content. To explain this phenomenon, the cellular structure of polyacrylamide gel was taken into consideration in addition to interactions between glucoamylase and gel, and a decrease in dielectric constant in the gel [S. Moriyama et al., Agric. Biol. Chem., 41, 1985 (1977)¹⁾]. On the other hand, immobilized glucoamylase bound to SP-Sephadex by ionic interaction showed lower stability than free glucoamylase, and much greater stability than glucoamylase in the presence of dextran sulfate, a constituent of SP-Sephadex. Thermal stabilities for the free and immobilized enzymes were also compared at the pH not in the bulk solution, but in the SP-Sephadex.     

Enzymatic processes for the purification of trehalose

A dual‐enzyme process aiming at facilitating the purification of trehalose from maltose is reported in this study. Enzymatic conversion of maltose to trehalose usually leads to the presence of significant amount of glucose, by‐product of the reaction, and unreacted maltose. To facilitate the separation of trehalose from glucose and unreacted maltose, sequential conversion of maltose to glucose and glucose to gluconic acid under the catalysis of glucoamylase and glucose oxidase, respectively, is studied. This study focuses on the hydrolysis of maltose with immobilized glucoamylase on Eupergit® C and CM Sepharose. CM Sepharose exhibited a higher protein adsorption capacity, 49.35 ± 1.43 mg/g, and was thus selected as carrier for the immobilization of glucoamylase. The optimal reaction temperature and reaction pH of the immobilized glucoamylase for maltose hydrolysis were identified as 40°C and 4.0, respectively. Under such conditions, the unreacted maltose in the product stream of trehalose synthase‐catalyzed reaction was completely converted to glucose within 35 min, without detectable trehalose degradation. The conversion of maltose to glucose could be maintained at 0.92 even after 80 cycles in repeated‐batch operations. It was also demonstrated that glucose thus generated could be readily oxidized into gluconic acid, which can be easily separated from trehalose. We thus believe the proposed process of maltose hydrolysis with immobilized glucoamylase, in conjunction with trehalose synthase‐catalyzed isomerization and glucose oxidase‐catalyzed oxidation, is promising for the production and purification of trehalose on industrial scales. © 2012 American Institute of Chemical Engineers Biotechnol. Prog., 2013     

Substrate thermostabilization of soluble and immobilized glucoamylase]

A new kinetic approach to the study of enzyme thermal inactivation in the presence of a substrate, which influences the rate of inactivation has been developed. The method was applied to investigation of inactivation kinetics of soluble and porous silica-immobilized glucoamylase. It was found that the binding of a substrate (maltose or maltodextrines Star-Dri 24-R) increases the thermal stability of glucoamylase, the stabilizing effect being more pronounced in the case of the soluble enzyme (40-fold stabilization) as compared to the immobilized one (15-fold stabilization). The stabilizing effect does not depend on the length of the substrate (maltose, d. p. 2 or dextrines, d. p. 7). Glucose, a product of the enzymatic hydrolysis, has a much lower stabilizing effect. It was concluded that the main role in the glucoamylase thermostabilization is played by the substrate stabilization rather than by the immobilization itself (3-fold stabilization). However, a combined effect of thermostabilization of glucoamylase due to both immobilization and/or substrate stabilization is restricted by the same limit of value for immobilized and soluble enzymes, which is equal to 40--50-fold in comparison with the soluble enzyme in the absence of the substrate.     

A two‐enzyme immobilization approach using carbon nanotubes/silica as support

Multiple enzyme mixtures are attractive for the production of many compounds at an industrial level. We report a practical and novel approach for coimmobilization of two enzymes. The system consists of a silica microsphere core coated with two layers of individually immobilized enzymes. The model enzymes α‐amylase (AA) and glucoamylase (GluA) were individually immobilized on carbon nanotubes (CNTs). A CNT‐GluA layer was formed by adsorbing CNT‐GluA onto silica microsphere. A sol‐gel layer with entrapped CNT‐AA was then formed outside the CNT‐GluA/silica microsphere conjugate. The coimmobilized α‐amylase and glucoamylase exhibited 95.1% of the activity of the mixture of free α‐amylase and glucoamylase. The consecutive use exhibited a good stability of the coimmobilized enzymes. The developed approach demonstrates advantages, including controlling the ratio of coimmobilized enzymes in an easy way, facilitating diffusion of small molecules in and out of the matrix, and preventing the leaching of enzymes. © 2014 American Institute of Chemical Engineers Biotechnol. Prog., 31:42–47, 2015     

Immobilization of glucoamylase by adsorption on carbon supports and its application for heterogeneous hydrolysis of dextrin

Glucoamylase (GA) was immobilized by adsorption on carbon support: on Sibunit, on bulk catalytic filamentous carbon (bulk CFC) and on activated carbon (AC). This was used to prepare heterogeneous biocatalysts for the hydrolysis of starch dextrin. The effect of the texture characteristics and chemical properties of the support surface on the enhancement of the thermal stability of the immobilized enzyme was studied, and the rates of the biocatalyst's thermal inactivation at 65-80 degrees C were determined. The thermal stability of glucoamylase immobilized on different carbon supports was found to increase by 2-3 orders of magnitude in comparison with the soluble enzyme, and decrease in the following order: GA on Sibunit>GA on bulk CFC>GA on AC. The presence of the substrate (dextrin) was found to have a significant stabilizing effect. The thermal stability of the immobilized enzyme was found to increase linearly when the concentration of dextrin was increased from 10 wt/vol % to 50 wt/vol %. The total stabilization effect for glucoamylase immobilized on Sibunit in concentrated dextrin solutions was about 10(5) in comparison with the enzyme in a buffer solution. The developed biocatalyst, 'Glucoamylase on Sibunit' was found to have high operational stability during the continuous hydrolysis of 30-35 wt/vol % dextrin at 60 degrees C, its inactivation half-time (t1/2) exceeding 350 h. To improve the starch saccharification productivity, an immersed vortex reactor (IVR) was designed and tested in the heterogeneous process with the biocatalyst 'Glucoamylase on Sibunit'. The dextrin hydrolysis rate, as well as the process productivity in the vortex reactor, was found to increase by a factor of 1.2-1.5 in comparison with the packed-bed reactor.     

An immobilized two-enzyme system (fungal alpha-amylase/glucoamylase) and its use in the continuous production of high conversion maltose-containing corn syrups

Fungal alpha-amylase (E.C. 3.2.1.1) and glucoamylase (E.C. 3.2.1.3) were chemically attached to separate reactor modules made from Microporous Plastic Sheet (MPS). Immobilization of enzymes and subsequent chemical reactions were accomplished by pumping reactants through the sheet, i.e., perpendicular to the surface. The expressed activity of the reactor modules was ca. 800 U/g for both fungal alpha-amylase and glucoamylase. The kinetics and short-term effects of pH and temperature on the expressed activity of the immobilized enzymes were investigated. Using commercially available DE-42 corn syrup at 50% dissolved solids, half-lives of 2000 and 5000 h were achieved for glucoamylase and fungal alpha-amylase, respectively. The reactors were operated at 50 degrees C and at pH 4.3 for glucoamylase and 5.5 for fungal alpha-amylase. A typical DE-62 corn syrup product was continuously produced in a two-stage reactor system by pumping the feedstock through the glycoamylase reactor and then through the fungal alpha-amylase reactor. Saccharide distributions at each stage were controllable to +/-0.2%.     

Pretreatment of starch raw materials and their enzymatic hydrolysis by immobilized glucoamylase

The pretreatment of starch raw materials such as sweet potato, potato and cassava has been carried out using various types of crusher, viz juice mixer, homogenizer and high-speed planetary mill. The effect of pretreatment of the materials on their enzymatic hydrolysis was studied. High-speed planetary mill treatment was the most effective and comparable with heat treatment (pasting). Various crushing times were used to examine the effect of crushing by mill treatment on the enzymatic hydrolysis. In the enzymatic hydrolysis of cassava, the use of both cellulase [1,4-(1,3; 1,4)-β-d-glucan 4-glucanohydrolase, EC 3.2.1.4] and glucoamylase [1,4-α-d-glucan glucohydrolase, EC 3.2.1.3] enhanced the d-glucose yield. The immobilization of glucoamylase was studied by radiation polymerization of hydrophilic monomers at low temperature, and it was found that enzymatic activity of the immobilized glucoamylase particles varied with monomer concentration and particle size. Starchy raw materials pretreated with the mill can be efficiently hydrolysed by immobilized glucoamylase.     

Immobilization of enzymes on porous silica supports

Four silica supports differing in pore dimensions were activated by treatment with SiCl₄ and then with ethylenediamine to obtain alkylamine groups on the silica surface. Three enzymes, peroxidase from cabbage, glucoamylase from Aspergillus niger C and urease from soybean were immobilized on these supports using glutaraldehyde as coupling agent. It was found that the protein content, the retained enzymatic activity and the storage stability of the silica supported enzymes were considerably affected by support pore size and enzyme molecular weight, the factors which are supposed to alter protein distribution inside the support pores. The highest activity was found for peroxidase and glucoamylase attached to the silica with the widest pores, but their loss in activity during storage was considerable. The urease retained less activity after immobilization, but its storage stability was excellent.     

Continuous conversion of starch to glucose with immobilized glucoamylase

Partially purified glucoamylase from Aspergillus awamori NRRL 3112 was immobilized on diethylaminoethyl cellulose in the presence of low ionic-strength acetate buffers at pH 4.2. The active enzyme–cellulose complex was used to convert starch substrates continuously to glucose in stirred reactors. Substrate concentrations as high as 30% could be quantitatively converted to glucose at a rate of more than 25 mg/min/liter at 55°C for periods of 3 to 4 weeks in a 4-liter reactor. Shutdowns were due to mechanical problems and not to loss of enzymes, which could be recovered with no appreciable loss of specific activity. Transfer products, such as isomaltose and panose, were present in immobilized enzyme-produced syrups but to no greater degree than in soluble glucoamylase digests of starch.     

Immobilization of glucoamylase on ceramic membrane surfaces modified with a new method of treatment utilizing SPCP-CVD

Glucoamylase, as a model enzyme, was immobilized on a ceramic membrane modified by surface corona discharge induced plasma chemical process-chemical vapor deposition (SPCP-CVD). Characterizations of the immobilized enzyme were then discussed. Three kinds of ceramic membranes with different amounts of amino groups on the surface were prepared utilizing the SPCP-CVD method. Each with 1-time, 3-times and 5-times surface modification treatments and used for supports in glucoamylase immobilization. The amount of immobilized glucoamylase increased with the increase in the number of surface modification treatments and saturated to a certain maximum value estimated by a two-dimensional random packing. The operational stability of the immobilized glucoamylase also increased with the increase in the number of the surface treatment. It was almost the same as the conventional method, while the activity of immobilized enzyme was higher. The results indicated the possibility of designing the performance of the immobilized enzyme by controlling the amount of amino groups. The above results showed that the completely new surface modification method using SPCP was effective in modifying ceramic membranes for enzyme immobilization.