Preparation of an immobilized two-enzyme system, Beta-amylase--pullulanase, to an acrylic copolymer for the conversion of starch to maltose. III. Process kinetic studies on continuous reactors

Kinetic studies on the parameters influencing the potential industrial application of an immobilized two-enzyme system of β-amylase and pullulanase for conversion of starch to a product with high maltose content, have been performed. The apparent Michaelis constant, the apparent product inhibitor constant, and the activation energy have been determined for the immobilized preparation and compared to the values for the corresponding soluble enzyme system. The catalytic activity of the immobilized enzymes was studied in a plug-flow reactor and a continuous feed stirred tank reactor. Mathematical models for these reactors have been formulated and adapted to fit the experimental data. Comparisons of the reactor efficiencies were made and the conditions were found to be such as to favor the plug-flow reactor. Results on operational stability tests at different temperatures and substrate concentrations are given.     

Covalent coupling of pullulanase to an acrylic copolymer using a water soluble carbodi-imide

Pullulanase (EC 3.2.1.9) prepared from a culture of Acrobacter aerogeneshas been covalently bound to an inert crosslinked copolymer of aerylamide-acrylic acid by using a water-soluble carbodi-imide. The binding yield based on the amount of added pullulanase was 34%. The residual enzymic activity was 43%, of that of free enzyme. Coupling in the presence of the substrate pullulan gave a 5-fold increase in activity over that obtained when substrate was lacking. The effect of different carbodi-imide concentrations on the coupling has been investigated. The isoelectric point of the pullulanase preparation (3.5–4.0) was determined using isoelectric, focusing, in order to find optimal pH conditions for the coupling procedure. The immobilized pullulanase in a packed bed column was used to debranch amylopeetin to low molecular weight amylose.     

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.     

Preparation of an immobilized two-enzyme system, beta-amylase-pullulanase, to an acrylic copolymer for the conversion of starch to copolymer for the conversion of starch to maltose. I. Preparation and stability of immobilized beta-amylase

β-Amylase (EC 3.2.1.2), obtained from barley, was chemically attached to a crosslinked copolymer of acrylamide-acrylic acid using a water-soluble carbodiimide. The derivative showed 23% β-amylase activity in relation to that of free enzyme with a coupling yield of 40% based on the amount of added β-amylase. In order to find optimal coupling conditions, the effect of pH and different carbodiimide concentrations was investigated. The enzymic activity associated with different β-amylase concentrations was further outlined. A slightly increased operational stability for the enzyme upon immobilization was observed. Markedly improved operational stability has been obtained by coupling in the presence of reduced glutathione of bovine serum albumin.     

Production of maltose and maltotriose from starch and pullulan by a immobilized multienzyme of pullulanase and β-amylase

Pullulanase was immobilized on tannic acid and TEAE-cellulose, and β-amylase was covalently immobilized on p-aminobenzylcellulose. Both the immobilized enzymes showed similar properties in pH and temperature optima and heat stability. On passing the pullulan solution at high temperature (50°C) through a column packed with immobilized pullulanase, only maltotriose was obtained for ten days and the half-life was about 15 days. In a continuous reaction using immobilized multienzyme, starch was completely converted into maltose at 50°C and at a space velocity of 1.2, a comparative longer half-life (20 days) was obtained. It was concluded that starch was smoothly converted into maltose with the aid of α-amylase contaminated in the immobilized pullulanase and the operational stability of the column increased with 2-5mM Ca²⁺.     

Immobilization of Exo-maltotetraohydrolase and Pullulanase

A dual enzyme system of exo-maltotetraohydrolase [EC 3.2.1.60] and pullulanase [EC 3.2.1.41] was studied for the continuous production of maltotetraose. Porous chitosan beads were selected from among many carriers as the best carrier to immobilize both enzymes.

The properties of the immobilized enzymes were examined and compared with those of the native enzymes. For exo-maltotetraohydrolase, the optimum pH of the immobilized enzyme shifted slightly to the acidic side and the pH stability was improved on the alkaline side. The optimum temperature of the immobilized enzyme increased by about 15°C and thermostability was improved by about 10°C. As for pullulanase, very little difference in thermostability was observed.

The effects of operating conditions on the continuous production of maltotetraose using exo- maltotetraohydrolase immobilized on the porous chitosan beads were examined. Porous chitosan beads were recognized to be superior to Diaion HP-50.

The continuous production of maltotetraose was accomplished using the dual immobilized enzyme system. The dual enzyme system proved to be effective to increase the maltotetraose content in the product. A stable operation was successfully continued for more than 60 days.     

Continuous production of maltotetraose using a dual immobilized enzyme system of maltotetraose-forming amylase and pullulanase

In order to produce a product with a high content of maltotetraose, dual-enzyme systems composed of immobilized maltotetraose-forming amylase (G(4)-forming amylase) and pullulanase were studied. The thermostability of individually immobilized enzymes was examined in continuous operation; studies revealed that the enzyme immobilized on "Chitopearl" was much more stable than that immobilized on Diaion HP-50. The effects of operating conditions on the stability of G(4) forming amylase immobilized on "Chitopearl" were examined to confirm that the apparent half-life data could be arranged using the immobilized enzyme stability factor, f(s). As for the dual immobilized enzyme system, six methods of usage were considered, with five yielding a 7-10% (w/w) higher content of maltotetraose product than the single-enzyme system. The effects of operating conditions on the maltotetraose production reaction were examined to confirm that the maltotetraose content of the products could be analyzed using the specific space velocity,SSV. In dual immobilized enzyme systems, pullulanase immobilized on the same carrier as the G(4)-forming amylase was found to be more stable than pullulanase immobilized on separate carriers. The effectiveness of using immobilized pullulanase along with the G(4)-forming amylase was confirmed from constant-conversion operations in which the maltotetraose content in the product was kept at 50% (w/w) in laboratory-scale experimentation.     

Immobilization of enzymes on Spheron: 2. β-Amylase — The development of a column reactor—separator

The titanium-chelation method has been used to immobilize β-amylase (1,4-α-d-glucan maltohydrolase, EC 3.2.1.2) on to Spheron. On various grades of Spheron, protein coupling yields of 56–76% were obtained with barley and sweet-potato β-amylases. The specific enzymic activities of the immobilized enzymes fell in the range 3.7–7.6% of those of the soluble enzymes. The immobilized enzymes were more stable than the soluble, especially in the presence of l-cysteine and serum albumin. The presence of cysteine and serum albumin brought about increases in activity in the preparations, presumably by regenerating essential thiol groups in the enzyme which had been oxidized during the operations. Maltose could be separated from amylopectin and other large polysaccharides by chromatography on Spheron P100, and a system was developed in which maltose, produced by hydrolysis of amylopectin applied in pulses to a column of immobilized β-amylase, was separated from starting material and by-products on a second column of Spheron P100.     

Immobilization of Penicillium funiculosum cellulase on a soluble polymer

The three cellulase [see 1,4-(1,3;1,4)-β-d-glucan 4-glucanohydrolase, EC 3.2.1.4] components of Penicillium funiculosum have been immobilized on a soluble, high molecular weight polymer, poly(vinyl alcohol), using carbodiimide. The immobilized enzyme retained over 90% of cellulase [1,4-(1,3;1,4)-β-d-glucan 4-glucanohydrolase, EC 3.2.1.4], and exo-β-d-glucanase [1,4-β-d-glucan cellobiohydrolase, EC 3.2.1.91] and β-d-glucosidase [β-d-glucoside glucohydrolase, EC 3.2.1.21] activities. The bound enzyme catalysed the hydrolysis of alkali-treated bagasse with a greater efficiency than the free cellulase. The potential for reuse of the immobilized system was studied using membrane filters and the system was found to be active for three cycles.     

Russian Article pp. 191–195

Three cellulase components and one xylanase of Trichoderma sp. M-17 have been immobilzed on a soluble high molecular weight polymer (PVA), using carbodiimide. The immobilized enzymes retained about 80% of the cellulase, cellulose 1,4-β-cellobiosidase, β-glucosidase and 60% endo-1,4-β-xylanase activities. The bound enzymes catalyzed the hydrolysis of alkali-treated cornstalks with a higher efficiency than the free cellulase. The potential for reutilization of the immobilized enzymes was studied using membrane filters and the system was found to be active for three cycles.     

Co-immobilization of amyloglucosidase and pullulanase for enhanced starch hydrolysis

Summary Amyloglucosidase and pullulanase were co-immobilized using a hydrophilic polyurethane foam (Hypol^® 2002). The combined amyloglucosidase and pullulanase activity of the immobilized enzyme was 32.2% ± 1.7% relative to the non-immobilized enzyme. The co-immobilized enzymes were capable of using a variety of glycogen and starch substrates. Co-immobilization of amyloglucosidase and pullulanase increased the glucose yield 1.6-fold over immobilized amyloglucosidase alone. No decrease in activity was observed after 4 months storage for the co-immobilized enzymes. The results suggest that co-immobilization of amyloglucosidase and pullulanase in polyurethane foams is a potentially useful approach for commercial starch hydrolysis. Offprint requests to: K. B. Storey     

Characterization of microbial endo-β-glucanase immobilized in alginate beads

Endo-β-glucanase (endo-β-1,4-glucano-glucanase EC 3.2.1.4), isolated from Trichoderma reesei, was immobilized in calcium alginate beads, retaining 75% of its original activity. The polyanionic moiety surrounding the immobilized enzyme displaced the pH-activity profile to alkaline regions with respect to that of the free enzyme. The enzyme was inhibited by carboxymethylcellulose, but this inhibition appeared to be decreased by immobilizatíon. The enzyme immobilized in alginate beads showed a K_m value (1.02% w/v) lower than that of the enzyme (1.31%). The apparent V_max of immobilized cellulase preparations (238.3 μmol glucose/ml × h) decreased by a factor of 0.59 with respect to that of the soluble enzyme. The optimum temperature (60°C) of the free and entrapped enzymes remained unaltered. In contrast, the half-life of the endoglucanase immobilized in calciumalginate beads was 4.6 h at 55°C and 5.4 h at 60°C, while that of the free enzyme was 3.0 h at 55°C and 1.2 h at 60°C. A technological application of the immobilized enzymes was tested using wheat straw as a source of fermentable sugars. The hydrolytic degradation of straw, by means of a crude extract of free and immobilized cellulases and β-glucosidase, released a large amount of reducing sugars from wheat straw after 48 h (between 250–720 mg glucose/g straw), carrying out more than a 90% saccharification. A mixture of immobilized β-glucosidase and free cellulases maintained 80% of the activity of the soluble counterparts, and the co-immobilization of both types of enzymes reduced by hydrolytic efficiency to half.     

The kinetic behavior of an artificial bienzyme membrane.

Artificial membranes bearing immobilized enzymes can be used to study some effects of membrane structure on enzyme kinetic behavior. The bienzyme system described is a mixture of beta-glucosidase and glucose oxidase. Gluconolactone, the product of thesecond enzyme, is an inhibitor of the first one. The resulting feedback effect has been compared using a mixed two-enzyme membrane, two separated one-enzyme membranes, and astirred bienzyme solution. The feedback effect is quicker and more efficient in the two-enzyme membrane than in solution; it is slower and less efficient in the case of the separated one-enzyme membranes. Effects of enzyme proximity in the structure are discussed. Conclusions are drawn concerning the efficiency of feedback mechanisms when enzymes are embedded within a single structure.     

Application of photochemical reactions of bis-azido compounds to preparation of an enzyme-polymer film.

β-Glucosidase (EC 3.2.1.21) was immobilized in fibroin film by using a photo-crosslinking agent, 4,4′-diazidostilbene-2,2′-disodium sulfonate. Crosslinking and immobilization reactions proceeded by light irradiation for 20 min in air. The immobilized enzyme showed approximately 50% of its native activity with an apparent Michaelis constant of 3.1 mm. The Michaelis constant of the native enzyme was 2.3 mm. Some properties of the immobilized and native enzymes were compared.     

Immobilization of enzymes based on hydrophobic interaction. I. Preparation and properties of a β-amylase adsorbate

Sweet potato β-amylase (α-1,4 glucan maltohydrolase, EC 3.2.1.2) was immobilized through adsorption onto an agarose gel to which nonpolar side chains had been introduced via ether bridges. The adsorbent showed evidence of saturation at an enzyme content of 35 mg per milliliter of packed gel. The adsorption was rapid and yielded a product whose operational stability depended on the initial content of β-amylase. Activity leakage was low. The relative activity of immobilized enzyme was inversely related to the amount of enzyme adsorbed to a given gel volume, having a maximal value of around 50% at low enzyme contents.     

Immobilization of pancreatic lipase on polyvinyl alcohol by cyanuric chloride

Porcine pancreatic lipase (EC 3.1.1.3) was covalently immobilized onto 2,4,6-trichloro-s-triazine (cyanuric chloride) activated polyvinyl alcohol (PVA). The influence of activating agent and enzyme concentration on the immobilization process were evaluated.Hydrolytic activities of free and immobilized enzyme were determined and the immobilization yield was estimated by measuring the quantity of protein, both in free enzyme solution and in washing solutions after immobilization. After the optimization of immobilization process, the physical and chemical characterization of immobilized enzyme was performed. Additionally, the thermal, pH, storage, and operational stability of the immobilized and free enzymes were tested. Obtained data showed that the immobilized enzyme seemed better and offered some advantages in comparison with free enzyme.     

Thermal and Operational Characteristics of Glutaryl-7-aminocephalosporanic acid Acylase Immobilized on Silica Gel Modified by Epoxide Silanization

Summary In this study, an investigation was performed into the thermal and operational characteristics of glutaryl-7-aminocephalosporanic acid (GL-7-ACA) acylase (EC 3.5.1.-) immobilized on silica gel that had been modified by epoxide silanization. The pH values for the optimum activity of free and immobilized GL-7-ACA acylase were almost the same. However, the pH-dependent activity profile for the immobilized GL-7-ACA acylase is considerably expanded. Both free and immobilized enzymes generally had the highest activity at 50 °C. In thermodynamic studies, it was found that immobilization using epoxide silanization made GL-7-ACA acylase thermodynamically stable. In the results of repeated batch production of 7-ACA, 89.0 and 83.5% of the 7-ACA produced at the initial cycle were maintained after 20 times of recycle at 25 °C and 30 °C, respectively. Hence it was suggested that mass production of 7-ACA at 25 °C using immobilized GL-7-ACA acylase by epoxide silanization would be possible on a large scale.     

Surface immobilization and entrapping of enzymes on glutaraldehyde crosslinked gelatin particles

A mild and reproducible method has been developed for the surface-immobilization of enzymes on glutaraldehyde crosslinked gelatin beads. In this method glutaraldehyde is used in a dual capacity, as crosslinking agent and as the enzyme coupling agent. Glucoamylase (exo-α-1,4-d-glucosidase, EC 3.2.1.3), β-d-fructofuranosidase (invertase, EC 3.2.1.26) and β-d-glucoside (cellobiase, β-d-glucoside glucohydrolase, EC 3.2.1.21) have been successfully immobilized by this method, on the surface of the crosslinked gelatin particles. The method can be combined with the existing technology for the production of gelatin-entrapped enzymes. Thus, dual immobilized enzyme conjugates of glucoamylase and invertase have been prepared using this method, by entrapment of one enzyme in, and surface-binding of the other to, the gelatin matrix. The coupling of glucoamylase onto cross-linked gelatin particles by precipitation with poly(hexamethylenebiguanide hydrochloride) was also tested.     

Partially deacetylated chitin as an acid-stable support for enzyme immobilization

Partially deacetylated chitin (PDAC) obtained by boiling chitin in 28.6% (w/w) sodium hydroxide was not dissolved when it was suspended in 2% acetic acid (pH 2.6) at 60°C for 12 h or autoclaved in acetate buffer (pH 5.0) for 20 min. The enzyme binding ability of the PDAC with glutaraldehyde was similar to that of chitosan. Immobilized pullulanase had low enzyme activity for high-molecular-weight material such as pullulan, but its activity for maltosyl β-cyclodextrin was almost the same as that of the free enzyme. The immobilized enzyme produced branched cyclodextrin through a reverse reaction in acetate buffer of pH 3.75 at 53°C.     

Covalent immobilization of pullulanase on alginate and study of its hydrolysis of pullulan

The immobilization of pullulanase from Klebsiella pneumoniae by grafting was investigated. Pullulanase was linked after activation of alginate via a covalent bond between the amine groups of the enzyme and the carboxylic acid groups of alginate. The immobilization yield was 60%. The activity of free pullulanase and immobilized pullulanase was followed by the quantification of reducing ends by colorimetric assay and the determination of the molar masses of the hydrolyzed pullulan by SEC/MALS/DRI. Compared to free pullulanase, the kinetics is largely slowed. The evolution of the weight average molar mass of pullulan leading to high production of shorter oligosaccharides during hydrolysis is not the same as that obtained with free enzyme. Immobilized pullulanase retained 75% and 30% of its initial activity after 24 h and 14 days of incubation at 60°C, respectively while free pullulanase lost its activity after 5 h of hydrolysis at the same temperature. The kinetic parameters of immobilized pullulanase were also investigated by isothermal titration calorimetry (ITC). The affinity of immobilized enzyme to its substrate was reduced compared to the free pullulanase due to steric hindrance and chemical links. © 2015 American Institute of Chemical Engineers Biotechnol. Prog., 31:883–889, 2015