Preparation of a very stable immobilized biocatalyst of glucose oxidase from Aspergillus niger

Glucose oxidase (GOX) has been immobilized on different activated supports, including glyoxyl agarose, epoxy sepabeads and glutaraldehyde-activated supports. Immobilization onto supports pre-activated with glutaraldehyde rendered the most thermo-stable preparation of GOX. Therefore, as the glutaraldehyde chemistry gave a high stabilization of the enzyme, we proposed another technique for improving the multipoint attachment through glutaraldehyde: the enzyme was ionically adsorbed on cationic supports with primary amino groups and then the immobilized preparation was treated with a glutaraldehyde solution. The decrease on enzyme activity was <20%. Following this methodology, we achieved the highest stability of all the immobilization systems analyzed, showing a half-life 100 times higher than the soluble enzyme. Moreover, this derivative showed a higher stability in the presence of organic solvents (for instance methanol) or hydrogen epoxide than the ionically adsorbed enzyme or the soluble one. Therefore, the adsorption of GOX on aminated cationic support and subsequent treatment with glutaraldehyde was presented as a very successful methodology for achieving a very stable biocatalyst.     

Immobilization of lipase from Candida rugosa on Sepabeads(®): the effect of lipase oxidation by periodates

The objective of this paper was the investigation of a suitable Sepabeads^? support and method for immobilization of lipase from Candida rugosa. Three different supports were used, two with amino groups, (Sepabeads^? EC-EA and Sepabeads^? EC-HA), differing in spacer length (two and six carbons, respectively) and one with epoxy group (Sepabeads^? EC-EP). Lipase immobilization was carried out by two conventional methods (via epoxy groups and via glutaraldehyde), and with periodate method for modification of lipase. The results of activity assays showed that lipase retained 94.8% or 87.6% of activity after immobilization via epoxy groups or with periodate method, respectively, while glutaraldehyde method was inferior with only 12.7% of retention. The immobilization of lipase, previously modified by periodate oxidation, via amino groups has proven to be more efficient than direct immobilization of lipase via epoxy groups. In such a way immobilized enzyme exhibited higher activity at high reaction temperatures and higher thermal stability.     

Improvement of covalent immobilization procedure of β‐galactosidase from Kluyveromyces lactis for galactooligosaccharides production: Modeling and kinetic study

Galactooligosaccharides (GOS) are prebiotics produced from lactose through an enzymatic reaction. Employing an immobilized enzyme may result in cost reductions; however, the changes in its kinetics due to immobilization has not been studied. This study experimentally determined the optimal reaction conditions for the production of GOS from lactose by β‐galactosidase (EC 3.2.1.23) from Kluyveromyces lactis covalently immobilized to a polysiloxane‐polyvinyl alcohol (POS‐PVA) polymer activated with glutaraldehyde (GA), and to study the transgalactosylation kinetics. Yield immobilization was 99 ± 1.1% with 78.5 ± 2.4% enzyme activity recovery. An experimental design 24 with 1 center point and 2 replicates was used. Factors were lactose [L], enzyme concentration [E], pH and temperature (T). Response variables were glucose and galactose as monosaccharides [G1], residual lactose [Lac]r and GOS as disaccharides [G2] and trisaccharides [G3]. Best conditions were pH 7.1, 40 °C, 270 gL^?1 initial lactose concentration and 6 U mL^?1 enzyme concentration, obtaining 25.46 ± 0.01 gL^?1 yield of trisaccharides. Although below the HPLC‐IR detection limit, tetrasaccharides were also identified after 115 min of reaction. The immobilization protocol was then optimized by diminishing total reactant volumes : support ratio, resulting in improved enzyme activity synthesizing 43.53 ± 0.02 gL^?1 of trisaccharides and 13.79 ± 0.21 gL^?1 of tetrasaccharides, and after four cycles remaining relative activity was 94%. A reaction mechanism was proposed through which a mathematical model was developed and rate constants were estimated, considering a pseudo steady‐state hypothesis for two concomitant reactions, and from this simplified analysis, the reaction yield could eventually be improved. © 2017 American Institute of Chemical Engineers Biotechnol. Prog., 33:1568–1578, 2017     

Hydrolysis of lactose in whey permeate by immobilized β-galactosidase from Penicillium notatum

A new low-cost β-galactosidase (lactase) preparation for whey permeate saccharification was developed and characterized. A biocatalyst with a lactase activity of 10 U/mg, a low transgalactosylase activity and a protein content of 0.22 mg protein/mg was obtained from a fermenter culture of the fungus Penicillium notatum. Factors influencing the enzymatic hydrolysis of lactose, such as reaction time, pH, temperature and enzyme and substrate concentration were standardized to maximize sugar yield from whey permeate. Thus, a 98.1% conversion of 5% lactose in whey permeate to sweet (glucose-galactose) syrup was reached in 48 h using 650 β-galactosidase units/g hydrolyzed substrate. After the immobilization of the acid β-galactosidase from Penicillium notatum on silanized porous glass modified by glutaraldehyde binding, more than 90% of the activity was retained. The marked shifts in the pH value (from 4.0 to 5.0) and optimum temperatures (from 50°C to 60°C) of the solid-phase enzyme were observed and discussed. The immobilized preparation showed high catalytic activity and stability at wider pH and temperature ranges than those of the free enzyme, and under the best operating conditions (lactose, 5%; β-galactosidase, 610–650 U/g lactose; pH 5.0; temperature 55°C), a high efficiency of lactose saccharification (84–88%) in whey permeate was achieved when lactolysis was performed both in a batch process and in a recycling packed-bed bioreactor. It seems that the promising results obtained during the assays performed on a laboratory scale make this immobilizate a new and very viable preparation of β-galactosidase for application in the processing of whey and whey permeates.     

Improved Properties of Bacillus coagulans β‐Galactosidase through Immobilization

Thermostable β‐galactosidase from Bacillus coagulans RCS3 was purified by successive column chromatography using DEAE‐cellulose and Sephadex G‐50. Immobilization of the purified enzyme was studied with DEAE‐cellulose and calcium alginate. The efficiency of β‐galactosidase retention was 87 % with DEAE‐cellulose (17 mg protein/mL of matrix) and 80 % with calcium alginate (2.2 mg protein/g bead). Comparative studies of immobilization displayed a shift in the optimum temperature from 65 °C to 70 °C provoked by DEAE‐cellulose, although no effect was observed with calcium alginate. The heat inactivation curve revealed an improvement in the stability (t_1/2 of 14.5 h for the immobilized enzyme as compared to 2 h for the free enzyme at 65 °C) in a calcium alginate system. This immobilized enzyme has a wide pH stability range (6.5–11). β‐Galactosidase immobilized by DEAE‐cellulose and calcium alginate allowed a 57 and 70 % lactose hydrolysis, respectively, to be achieved within 48 h after repeated use for twenty times.     

Novel and efficient method for immobilization and stabilization of β-d-galactosidase by covalent attachment onto magnetic Fe3O4–chitosan nanoparticles

A novel and efficient immobilization of β-d-galactosidase from Aspergillus oryzae has been developed by using magnetic Fe₃O₄–chitosan (Fe₃O₄–CS) nanoparticles as support. The magnetic Fe₃O₄–CS nanoparticles were prepared by electrostatic adsorption of chitosan onto the surface of Fe₃O₄ nanoparticles made through co-precipitation of Fe²⁺ and Fe³⁺. The resultant material was characterized by transmission electron microscopy, X-ray diffraction, Fourier transform infrared spectroscopy, vibrating sample magnetometry and thermogravimetric analysis. β-d-Galactosidase was covalently immobilized onto the nanocomposites using glutaraldehyde as activating agent. The immobilization process was optimized by examining immobilized time, cross-linking time, enzyme concentration, glutaraldehyde concentration, the initial pH values of glutaraldehyde and the enzyme solution. As a result, the immobilized enzyme presented a higher storage, pH and thermal stability than the soluble enzyme. Galactooligosaccharide was formed with lactose as substrate by using the immobilized enzyme as biocatalyst, and a maximum yield of 15.5% (w/v) was achieved when about 50% lactose was hydrolyzed. Hence, the magnetic Fe₃O₄–chitosan nanoparticles are proved to be an effective support for the immobilization of β-d-galactosidase.     

Design of β‐galactosidase/silica biocatalysts: Impact of the enzyme properties and immobilization pathways on their catalytic performance

The use of heterogeneous biocatalysis in industrial applications is advantageous and the enzyme stability improvement is a continuous challenge. Therefore, we designed β‐galactosidase heterogeneous biocatalysts by immobilization, involving the support synthesis and enzyme selection (from Bacillus circulans, Kluyveromyces lactis, and Aspergillus oryzae). The underivatized, tailored, macro‐mesoporous silica exhibited high surface area, offered high enzyme immobilization yields and activity. Its chemical activation with glyoxyl groups bound the enzyme covalently, which suppressed lixiviation and conferred higher pH and thermal stability (120‐fold than for the soluble enzyme), without observable reduction of activity/stability due to the presence of silica. The best balance between the immobilization yield (68%), activity (48%), and stability was achieved for Bacillus circulans β‐galactosidase immobilized on glyoxyl‐activated silica, without using stabilizing agents or modifying the enzyme. The enzyme stabilization after immobilization in glyoxyl‐activated silica was similar to that observed in macroporous agarose‐glyoxyl support, with the reported microbiological and mechanical advantages of inorganic supports. The whey lactolysis at pH 6.0 and 25°C by using this catalyst (1 mg ml^?1, 290 UI g^?1) was still 90%, even after 10 cycles of 10 min, in batch process but it could be also implemented on continuous processes at industrial level with similar results.     

Covalent immobilization of antibodies on finally inert support surfaces through their surface regions having the highest densities in carboxyl groups

The correct immobilization of antibodies is one of the most critical steps in the preparation of immunosensors and immunochromatography matrices. In addition, the final support has to be chemical and physically inert to avoid the unspecific adsorption of proteins that can reduce the sensitivity of the biosensor or the purification achieved by the chromatography. The solution to both problems is one of the major challenges in the field. Here, we have presented two different novel and simple alternatives to have the unmodified antibody anionically exchanged to a support, further covalently immobilized with more than 90% of the antibodies bonded to the support by the four subunits, retaining a high functionality and giving a final "inert" surface. The first solution was the use of supports having a low superficial density of amino groups activated with glutaraldehyde. Here, the inertness was achieved by the use of a very low density of amino groups, unable to adsorb proteins at 100 mM sodium phosphate, while immobilization proceeds mainly via a first adsorption of the antibody and a further reaction with the glutaraldehyde groups. The second solution implies the design of a novel support (amino-epoxy). This support again produces a first ionic exchange of the antibody on the support and a further reaction with the epoxy groups, but because the epoxy groups can be finally blocked with aspartic groups (annulling the charge), the initial density of amino-epoxy groups can be as high as possible. Both systems permitted the correct and oriented immobilization of IgG. The immobilized antibody showed high-functionality (65-75%) and a final inert support surface. This immobilized antibody (antiperoxidase) was able to capture fully specifically HRP contaminating a protein crude extract from E. coli.     

Enhanced activity and stability of <Emphasis Type="SmallCaps">l</Emphasis>-arabinose isomerase by immobilization on aminopropyl glass

Immobilization of Bacillus licheniformis l-arabinose isomerase (BLAI) on aminopropyl glass modified with glutaraldehyde (4 mg protein g support⁻¹) was found to enhance the enzyme activity. The immobilization yield of BLAI was proportional to the quantity of amino groups on the surface of support. Reducing particle size increased the adsorption capacity (q _m) and affinity (k _a). The pH and temperature for immobilization were optimized to be pH 7.1 and 33°C using response surface methodology (RSM). The immobilized enzyme was characterized and compared to the free enzyme. There is no change in optimal pH and temperature before and after immobilization. However, the immobilized BLAI enzyme achieved 145% of the activity of the free enzyme. Correspondingly, the catalytic efficiency (k _cat/K _m) was improved 1.47-fold after immobilization compared to the free enzyme. The thermal stability was improved 138-fold (t _1/2 increased from 2 to 275 h) at 50°C following immobilization.     

Kinetic resolution of drug intermediates catalyzed by lipase B from Candida antarctica immobilized on immobead‐350

Novozyme 435, which is a commercial immobilized lipase B from Candida antarctica (CALB), has been proven to be inadequate for the kinetic resolution of rac‐indanyl acetate. As it has been previously described that different immobilization protocols may greatly alter lipase features, in this work, CALB was covalently immobilized on epoxy Immobead‐350 (IB‐350) and on glyoxyl‐agarose to ascertain if better kinetic resolution would result. Afterwards, all CALB biocatalysts were utilized in the hydrolytic resolution of rac‐indanyl acetate and rac‐(chloromethyl)‐2‐(o‐methoxyphenoxy) ethyl acetate. After optimization of the immobilization protocol on IB‐350, its loading capacity was 150 mg protein/g dried support. Furthermore, the CALB‐IB‐350 thermal and solvent stabilities were higher than that of the soluble enzyme (e.g., by a 14‐fold factor at pH 5–70°C and by a 11‐fold factor in dioxane 30%–65°C) and that of the glyoxyl‐agarose‐CALB (e.g., by a 12‐fold factor at pH 10–50°C and by a 21‐fold factor in dioxane 30%–65°C). The CALB‐IB‐350 preparation (with 98% immobilization yield and activity versus p‐nitrophenyl butyrate of 6.26 ± 0.2 U/g) was used in the hydrolysis of rac‐indanyl acetate using a biocatalyst/substrate ratio of 2:1 and a pH value of 7.0 at 30°C for 24 h. The conversion obtained was 48% and the enantiomeric excess of the product (e.e._p) was 97%. These values were much higher than the ones obtained with Novozyme 435, 13% and 26% of conversion and e.e.p, respectively. © 2018 American Institute of Chemical Engineers Biotechnol. Prog., 34:878–889, 2018     

Heterofunctional Magnetic Metal‐Chelate‐Epoxy Supports for the Purification and Covalent Immobilization of Benzoylformate Decarboxylase From Pseudomonas Putida and Its Carboligation Reactivity

In this study, the combined use of the selectivity of metal chelate affinity chromatography with the capacity of epoxy supports to immobilize poly‐His‐tagged recombinant benzoylformate decarboxylase from Pseudomonas putida (BFD, E.C. 4.1.1.7) via covalent attachment is shown. This was achieved by designing tailor‐made magnetic chelate–epoxy supports. In order to selectively adsorb and then covalently immobilize the poly‐His‐tagged BFD, the epoxy groups (300 µmol epoxy groups/g support) and a very small density of Co²⁺‐chelate groups (38 µmol Co²⁺/g support) was introduced onto magnetic supports. That is, it was possible to accomplish, in a simple manner, the purification and covalent immobilization of a histidine‐tagged recombinant BFD. The magnetically responsive biocatalyst was tested to catalyze the carboligation reactions. The benzoin condensation reactions were performed with this simple and convenient heterogeneous biocatalyst and were comparable to that of a free‐enzyme‐catalyzed reaction. The enantiomeric excess (ee) of (R)‐benzoin was obtained at 99 ± 2% for the free enzyme and 96 ± 3% for the immobilized enzyme. To test the stability of the covalently immobilized enzyme, the immobilized enzyme was reused in five reaction cycles for the formation of chiral 2‐hydroxypropiophenone (2‐HPP) from benzaldehyde and acetaldehyde, and it retained 96% of its original activity after five reaction cycles. Chirality 27:635–642, 2015. © 2015 Wiley Periodicals, Inc.     

Laccase immobilization on the tailored cellulose-based Granocel carriers

Extracellular laccase produced by Cerrena unicolor was immobilized by adsorption or covalent bonds formation on the cellulose-based carrier Granocel. Immobilization was optimized by changing the anchor groups and the methods of activation/immobilization. On the base of measured activity and stability of immobilized preparations, the covalent method was selected. It was shown that coupling of the enzyme to the carrier via divinyl sulfone or glutaraldehyde yielded an enzyme-carrier preparation of high activity and storage stability. Further optimization of the carrier's superstructure consisted in changing pore diameters and amount of functional groups on the carriers surface. Three-fold higher activity was noted when the enzyme was immobilized on NH2-modified Granocel with the highest size exclusion limit and amino group content. Relatively low products sorption was observed on the carrier surface. The effects of protein concentration and pH-value of the coupling mixture on immobilization efficiency were evaluated also.     

Composition and oligosaccharides of a milk sample of the giant panda,Ailuropoda melanoleuca

A milk sample from a captive giant panda (Ailuropoda melanoleuca), obtained at 13 days postpartum, contained 7.1% protein, 1.6% carbohydrate, 10.4% lipid and 0.9% ash. The ratio of casein to whey proteins was 5.0:2.1. Sodium dodecyl sulfate polyacrylamide electrophoresis (SDS-PAGE) of the whey protein fraction showed the presence of at least two major proteins other than alpha-lactalbumin and beta-lactoglobulin. SDS-PAGE and urea-gel electrophoresis showed that alphas-casein is not a major component. The proportions of triacylglycerol, cholesterol, cholesterol esters and phospholipid were 90.5, 5.3, 0.96 and 3.1%, of the total lipid, respectively. The dominant saccharide in the panda milk was Gal(alpha1-3)Gal(beta1-4)Glc (isoglobotriose). The milk contained, in addition, lesser amounts of lactose, Gal(alpha1-3)Gal(beta1-4)[Fuc(alpha1-3)]Glc (fucosyl isoglobotriose), Neu5Ac(alpha2-3)Gal(beta1-4)Glc (3'-N-acetylneuraminyl-lactose), Neu5Ac(alpha2-6)Gal(beta1-4)Glc (6'-N-acetylneuraminyl-lactose) and Neu5Ac(alpha2-3)Gal(beta1-4)[Fuc(alpha1-3)]Glc.     

Immobilization of enzymes on heterofunctional epoxy supports

Immobilization of enzymes and proteins on activated supports permits the simplification of the reactor design and may be used to improve some enzyme properties. In this sense, supports containing epoxy groups seem to be useful to generate very intense multipoint covalent attachment with different nucleophiles placed on the surface of enzyme molecules (e.g., amino, thiol, hydroxyl groups). However, the intermolecular reaction between epoxy groups and soluble enzymes is extremely slow. To solve this problem, we have designed "tailor-made" heterofunctional epoxy supports. Using these, immobilization of enzymes is performed via a two-step process: (i) an initial physical or chemical intermolecular interaction of the enzyme surface with the new functional groups introduced on the support surface and (ii) a subsequent intense intramolecular multipoint covalent reaction between the nucleophiles of the already immobilized enzyme and the epoxy groups of the supports. The first immobilization may involve different enzyme regions, which will be further rigidified by multipoint covalent attachment. The design of some heterofunctional epoxy supports and the performance of the immobilization protocols are described here. The whole protocol to have an immobilized and stabilized enzyme could take from 3 days to 1 week.     

In situ immobilization of β‐galactosidase from Bacillus circulans in silica by sol‐gel process: Application in prebiotic synthesis

The enzyme encapsulation is a very well‐known stabilization pathway. However, there are some challenges in order to avoid the enzyme denaturation under encapsulation conditions. The β‐galactosidase from Bacillus circulans was immobilized through sol‐gel encapsulation route assisted by Triton X‐100 surfactant and sugars. The effects of sugar presence in the immobilization process and the gelation time on the biocatalyst activity/stability were explained taking into account the characteristics of the formed silica matrix and the changes of the enzyme environment. The enzyme was effectively immobilized by this strategy, with high immobilization yield in terms of activity (29%) and expressed activity (47 IU/g). The immobilization through silica sol‐gel in the presence of 1×10^?3 M Triton X‐100 and fructose conferred 28.4‐fold higher stability to the enzyme compared with the soluble form. This is an advantage for its use in the synthesis of the galacto‐oligosaccharides at 50ºC. The total lactose conversion to galacto‐oligosaccharides was 26%wt, which is comparable with that reported in the literature. The obtained biocatalyst is useful for the synthesis of galacto‐oligosaccharides and its catalytic behavior is rationalized in this work.     

Immobilization of thermostable β-glucosidase from Sulfolobus shibatae by cross-linking with transglutaminase

Thermostable β-glucosidase from Sulfolobus shibatae was immobilized on silica gel modified or not modified with 3-aminopropyl-triethoxysilane using transglutaminase as a cross-linking factor. Obtained preparations had specific activity of 3883 U/g of the support, when measured at 70 °C using o-nitrophenyl β-d-galactopyranoside (GalβoNp) as substrate. The highest immobilization yield of the enzyme was achieved at pH 5.0 in reaction media. The most active preparations of immobilized β-glucosidase were obtained at a transglutaminase concentration of 40 mg/ml at 50 °C. The immobilization was almost completely terminated after 100 min of the reaction and prolonged time of this process did not cause considerable changes of the activity of the preparations. The immobilization did not influence considerably on optimum pH and temperature of GalβoNp hydrolysis catalyzed by the investigated enzyme (98 °C, pH 5.5). The broad substrate specifity and properties of the thermostable β-glucosidase from S. shibatae immobilized on silica-gel indicate its suitability for hydrolysis of lactose during whey processing.     

Optimization of an industrial biocatalyst of glutaryl acylase: stabilization of the enzyme by multipoint covalent attachment onto new amino-epoxy Sepabeads

Glutaryl-7-aminocephalosporanic acid acylase (GA), an industrially relevant enzyme, has been immobilized onto very different supports, including glyoxyl agarose, heterofunctional epoxy Sepabeads, glutaraldehyde and cyanogen bromide (CNBr) activated supports. Immobilization onto amino-epoxy Sepabeads rendered the most thermo stable preparation of GA, with a half-life time eight times higher than the soluble enzyme, keeping 80% of the enzyme activity. Several parameters that affect the enzyme-support interaction (pH and incubation time) were studied. It was found that after immobilization onto amino-epoxy Sepabeads, incubation at alkaline pH and low temperature exerted dramatic stabilizing effects, increasing the half-life time of the derivative 130 times with respect to the soluble enzyme, while keeping unaltered its intrinsic activity. The loading capacity of the amino-epoxy Sepabeads proved to be very good with a maximum load of 62 mg of protein per g of support with 85 IU/g at 25 degrees C and 200 IU/g at 37 degrees C which makes it a biocatalyst of possible industrial application.     

Epoxy-amino groups: a new tool for improved immobilization of proteins by the epoxy method

The properties of a new commercially available amino-epoxy support (amino-epoxy-Sepabeads) for immobilizing enzymes have been compared to those of conventional epoxy supports. The new support has a layer of epoxy groups over a layer of ethylenediamine that is covalently bound to the support. Thus, this support has a great anionic exchanger power and a high number of epoxy groups. We have found a number of advantages to this new heterofunctional support. Immobilization proceeds at low ionic strength using amino epoxy Sepabeads while requiring high ionic strength using conventional monofunctional epoxy supports. Immobilization is much more rapid using amino-epoxy supports than employing conventional epoxy supports. The possibility of achieving immobilized preparations in which the enzyme orientation may be different to that obtained using the traditional hydrophobic supports (with likely effects in terms of activity or stability). Stability of the immobilized enzyme has been found to be much higher using the new support than in preparations using the conventional ones in many cases. Here we show some examples of these advantages using different enzymes (beta-galactosidases, lipase, glutaryl acylase, invertase, and glucoamylase).     

One-step purification,covalent immobilization,and additional stabilization of a thermophilic poly-His-tagged beta-galactosidase from Thermus sp. strain T2 by using novel heterofunctional chelate-epoxy Sepabeads

Using the poly-His-tagged-beta-galactosidase from Thermus sp. strain T2 overexpressed in Escherichia coli (MC1116) as a model enzyme, we have developed a strategy to purify and immobilize proteins in a single step, combining the excellent properties of epoxy groups for enzyme immobilization with the good performance of immobilized metal-chelate affinity chromatography for protein purification. The aforementioned enzyme could not be immobilized onto standard epoxy supports with good yields, and after purification and storage, it exhibited a strong trend to yield very large aggregates as shown by ultracentrifugation experiments. That preparation could not be immobilized in any support, very likely because the pores of the solid became clogged by the large aggregates. These novel epoxy-metal chelate heterofunctional supports contain a low concentration of Co(2+) chelated in IDA groups and a high density of epoxy groups. This enabled the selective adsorption of poly-His-tagged enzymes, and as this adsorption step is necessary for the covalent immobilization procedure, the selective covalent immobilization of the target enzyme could take place. This strategy allowed similar maximum loadings of the target enzyme using either pure or crude preparations of the enzyme. The enzyme derivative presented a very high activity at 70 degrees C (over 1000 IU in the hydrolysis of lactose) and very high stability and stabilization when compared to its soluble counterpart (activity remained unaltered after several days of incubation at 50 degrees C). In fact, this preparation was much more stable than when the same enzyme was immobilized onto standard epoxy Sepabeads.     

Immobilization of Papain on the Mesoporous Molecular Sieve MCM‐48

The immobilization of papain on the mesoporous molecular sieve MCM‐48 (with a pore size of 6.2 nm in diameter) with the aid of glutaraldehyde, and the characteristics of this immobilized papain are described. The optimum conditions for immobilization were as follows: 20 mg native free enzyme/g of the MCM‐48 and 0.75 % glutaraldehyde, 2 h at 10–20 °C and pH 7.0. Under these optimum conditions for immobilization, the activity yield [%] of the immobilized enzyme was around 70 %. The influence of the pH on the activity of the immobilized enzyme was much lower compared to the free enzyme. The thermostability of the immobilized enzyme, whose half‐life was more than 2500 min, was greatly improved and was found to be significantly higher than that of the free enzyme (about 80 min). The immobilized enzyme also showed good operational stability, and the activity of the immobilized enzyme continued to maintain 76.5 % of the initial activity even after a 12‐day continuous operation. Moreover, the immobilized enzyme still exhibited good storage stability. From these results, papain immobilized on the MCM‐48 with the aid of glutaraldehyde, can be used as a high‐performance biocatalyst in biotechnological processing, in particular in industrial and medical applications.