Immobilization of cellulase onto electrospun polyacrylonitrile (PAN) nanofibrous membranes and its application to the reducing sugar production from microalgae

This study demonstrates a method to prepare an immobilized cellulase by using an electrospun polyacrylonitrile (PAN) nanofibrous membrane as the support. To obtain an immobilized cellulase with high hydrolytic activity, the immobilization conditions including activation time, enzyme concentration, immobilization time, and temperature were optimized. Under those conditions, the immobilized cellulase possessed a protein loading of 30 mg/g-support and a specific activity of 3.2 U/mg-protein. After immobilization, the enzymatic stability of cellulase against pH and thermal stresses was improved. Fourier transform infrared spectroscopy (FTIR) measurements also revealed that the cellulase was covalently bonded to the supports. The immobilized cellulase was then used to hydrolyze cell wall of microalgae for the production of reducing sugars. Analyses using response surface methodology (RSM) show that the hydrolysis yield was affected by the reaction temperature, pH, and substrate/cellulase mass ratio, and a hydrolysis yield of 60.86% could be obtained at 47.85 °C, pH 5.82, and a substrate/cellulase mass ratio of 40 g-substrate/g-cellulase. This result suggests that the proposed scheme for the cellulase immobilization has great potential for the application to the reducing sugar production.     

Kinetic study of sphingomyelin hydrolysis for ceramide production

Kinetic study of sphingomyelin hydrolysis catalyzed by Clostridium perfringens phospholipase C was, at the first time, conducted for ceramide production. Ceramide has the major role in maintaining the water-retaining properties of the epidermis. Hence, it is of great commercial potential in cosmetic and pharmaceutical industries such as in hair and skin care products. The enzymatic hydrolysis of sphingomyelin has been proved to be a feasible method to produce ceramide. The kinetic performance of sphingomyelin hydrolysis in the optimal two-phase (water:organic solvent) reaction system was investigated to elucidate the possible reaction mechanism and also to further improve the hydrolysis performance. Enzyme in solution had less thermal stability than the enzyme powder and the immobilized enzyme. The thermal inactivation of phospholipase C in all the three forms did not follow the first order reaction at 65 °C. The reactions for both the soluble and immobilized enzymes followed Michaelis–Menten kinetics. K_m's for the soluble and immobilized enzymes were 1.07 ± 0.32 and 1.26 ± 0.19 mM, respectively. The value of V_max was markedly decreased by the immobilization without much change in K_m, as if the immobilization functioned as the non-competitive inhibition. Ceramide as product activated the hydrolysis reaction, however, and its addition mainly caused the increase in the affinity of the enzyme–substrate complex.     

Biotechnology for the production of nutraceuticals enriched in conjugated linoleic acid: I. Uniresponse kinetics of the hydrolysis of corn oil by a Pseudomonas sp. lipase immobilized in a hollow fiber reactor

The kinetics of the hydrolysis of corn oil in the presence of a lipase from Pseudomonas sp. immobilized within the walls of a hollow fiber reactor can be modeled in terms of a three‐parameter rate expression. This rate expression consists of the product of a two‐parameter rate expression for the hydrolysis reaction itself (which is of the general Michaelis–Menten form) and a first‐order rate expression for deactivation of the enzyme. Optimum operating conditions correspond to 30°C and buffer pH values of 7.0 during both immobilization of the enzyme and the hydrolysis reaction. Under these conditions, the total fatty acid concentration in the effluent oil stream for a fluid residence time of 4 h is approximately 1.6 M. This concentration corresponds to hydrolysis of approximately 50% of the glyceride bonds present in the feedstock corn oil. The fatty acid of primary interest in the effluent stream is linoleic acid. © 1999 John Wiley & Sons, Inc. Biotechnol Bioeng 64: 568–579, 1999.     

Immobilization of α-amylase on gum acacia stabilized magnetite nanoparticles,an easily recoverable and reusable support

In this work, α-amylase is immobilized, using glutaraldehyde, onto magnetite nanoparticles prepared using gum acacia as the steric stabilizer (GA-MN), for the first time. The immobilization of amylase to GA-MN is very fast and the synthesis of GA-MN is very simple. The use of GA enables higher immobilization of α-amylase (60%), in contrast to the unmodified magnetite nanoparticles (∼20%). The optimum pH and temperature for maximum enzyme activity for the immobilized amylase are identified to be 7.0 and 40 °C, respectively, for the hydrolysis of starch. The kinetic studies confirm the Michaelis–Menten behavior and suggests overall enhancement in the performance of the immobilized enzyme with reference to the free enzyme. Similarly the thermal stability of the enzyme is found to increase after the immobilization. The GA-MN bound amylase has also been demonstrated to be capable of being reused for at least six cycles while retaining ∼70% of the initial activity. By using a magnetically active support, quick separation of amylase from reaction mixture is enabled. The catalytic rate of amylase is actually found to enhance by twofold after the immobilization, which is extremely advantageous in industry. At higher temperature, the immobilized enzyme exhibits higher enzyme activity than that of the free enzyme.     

Immobilization of enzymes in liquid membranes for enantioselective hydrolysis

Summary The enantioselective hydrolysis of racemic 4-acetoxy-cyclopentenone by immobilized enzymes is described. Liquid membrane emulsions were used to encapsulate the enzyme. This technique combines the specific enzymatic reaction with a selective transport through the organic phase. The product (–)-4-hydroxy-cyclopentenone was produced with an enantiomeric excess of 82%. The immobilization techniques and all reaction steps, as well as a mathematical model for the complete process are discussed in this report.     

Immobilization of Lipase from Mucor Miehei Onto Poly (Ethylene) Based Graft Copolymers

Lipase from Mucor miehei was immobilized covalently onto hydrolyzed poly(ethylene)-g.co-hydroxyethyl methacrylate (PE-HEMA). This hydrolysis of the copolymer was achieved using 0.1 M NaOH over different periods of time, under controlled conditions. The graft copolymers and their hydrolyzed equivalents were characterized by scanning electron microscopy (SEM) and by differential scanning calorimetry analysis (DSC). Water sorption studies were undertaken to provide a measure of relative hydrophobicity of the samples.

The lipase immobilization reaction was studied in order to assess the effects of controlling various important parameters. These include the nature of the buffering medium, the time over which the immobilization was allowed to occur, the concentration of the activating and coupling agent used (CMC) and the concentration of enzyme employed during attempts at effective immobilization. The immobilized lipase was used in the hydrolysis of triolein (glycerol trioleate). From this study, the apparent K_M, the optimum pH for hydrolysis and the optimum temperature for hydrolysis were revealed.

The suitability of hydrolyzed poly(ethylene)-g.co-HEMA as a support in the immobilization of lipase was assessed by determination of the amount of lipase coupled to the support and by assessment of the retention of activity of the immobilized lipase after its exposure to the immobilization reagents, procedure and conditions.     

Immobilization of glucose oxidase on polymer membranes treated by low-temperature plasma

Low-temperature plasma was employed for activation of polymer membranes as a carrier for enzyme immobilization. Glucose oxidase was immobilized on polypropylene (PP), polyvinylidene fluoride (PVDF), or polytetrafluoroethylene (PTFE) membrane surfaces treated by nitrogen or ammonia gas plasma using glutaraldehyde as a linking agent. Enzyme activity was evaluated by the response of glucose sensor composed of the immobilized enzyme membrane and a dissolved oxygen electrode. The sensor response was found to depend on the kind of carrier membrane and to become maximum at suitable conditions of plasma treatment.     

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.     

Catalytic properties of glucoamylase immobilized on synthetic carbon material Sibunit

Glucoamylase (commercial preparation Glucavamorin) was immobilized by sorption on a carbon support Sibunit. Starch saccharification by the resulting biocatalyst (dextrin hydrolysis) was studied. Investigation of the effect of adsorptional immobilization on kinetic parameters of glucoamylase, including the rate constant of thermal inactivation, showed that immobilization of Glucavamorin on Sibunit resulted in a thousand-fold increase in glucoamylase stability in comparison with the dissolved enzyme. Presence of the substrate (dextrins) in the reaction mixture had a considerable stabilizing effect. Increase in dextrin concentration increases the thermostability of the immobilized enzyme. The overall factor of glucoamylase stabilization adsorbed on Sibunit with the presence of 53% dextrin solutions in comparison with the dissolved enzyme approximated 10⁵. The biocatalyst for starch saccharification made on the base of Subunit-adsorbed Glucavamorin had a high operational stability. Its half-inactivation time at 60°C exceeded 30 days.     

Properties of immobilized β-d-galactosidase from Bacillus circulans

Partially purified β-d-galactosidase (β-d-galactoside galactohydrolase, EC 3.2.1.23) from Bacillus circulans showed high activity towards both pure lactose and lactose in skim milk, and a better thermal stability than the enzyme from yeast or Escherichia coli. During the course of hydrolysis of lactose catalysed by the enzyme, considerable amounts of oligosaccharides were produced. β-d-Galactosidase from B. circulans was immobilized onto Duolite ES-762, Dowex MWA-1 and sintered alumina by adsorption with glutaraldehyde treatment. The highest activity for hydrolysis of lactose was obtained with immobilization onto Duolite ES-762. During a continuous hydrolysis of lactose, the immobilized enzyme was reversibly inactivated, probably due to oligosaccharides accumulating in the gel. The inactivation was reduced when a continuous reaction was operated at a high percent conversion of lactose in a continuous stirred tank reactor (CSTR). The half-life of the immobilized enzyme was estimated to be 50 and 15 days at 50 and 55°C, respectively, when the reaction was carried out in a CSTR with a percent conversion of lactose >70%.     

Immobilization of lipase on hydrophobic nano-sized magnetite particles

As a tool for the stable enzyme reuse, enzyme immobilization has been studied for several decades. Surface-modified nano-sized magnetite (S-NSM) particles have been suggested as a support for the immobilization of enzyme in this study. Based on the finding that a lipase is strongly adsorbed onto a hydrophobic surface, NSM particles (8–12 nm) were made hydrophobic by binding of sodium dodecyl sulfate via a sulfate ester bond. Various types of measurements, such as transmission electron microscopy, X-ray diffraction, infrared spectroscopy, vibration sample magnetometer, and thermo gravimetric analysis, were conducted in characterizing S-NSM nanoparticles. S-NSM particles were used for the adsorption of porcine pancreas lipase (PPL). A dodecyl carbon chain is expected to form a spacer between the surface of the NSM and the lipase adsorbed. The immobilized PPL showed the higher specific activity of oil hydrolysis than that of free one. Immobilized PPL could be recovered by magnetic separation, and showed the constant activity during the recycles.     

Catalytic properties of endoxylanase fusion proteins from Neocallimastix frontalis and effect of immobilization onto metal-chelate matrix

The production of hybrid enzymes with novel properties and the research for new methods for enzyme immobilization in bioreactors are of major interest in biotechnology. We report here the second part of a study concerning the improvement of the properties of the endoxylanase XYN3A4 from the anaerobic fungi Neocallimastix frontalis. The effects of gene fusion and immobilization on metal-chelate matrix are also compared for the reference enzymes XYN3, XYN3A, XYN4 used for the construction of the fusion protein XYN3A4. The influence of the metal ion in the immobilization process was first investigated and best immobilization yields were obtained with the Cu(II) ion whereas best coupling efficiencies were reached with the Ni(II) ion. It was also observed that XYN3, XYN3A and XYN34 had a lower rate of hydrolysis when immobilized on Ni(II)-IDA and more difficulties to accomodate small substrates than the soluble enzymes. Nevertheless, a major difference was noted during the hydrolysis of birchwood xylan and it appears that the reaction using the immobilized XYN3A4 chimeric enzyme leads to the accumulation of a specific product.     

Immobilization of maltogenase onto polyurethane microparticles from poly(vinyl alcohol) and hexamethylene diisocyanate

A series of porous polyurethane (PU) microparticles from poly(vinyl alcohol) (PVA) and hexamethylene diisocyanate (HMDI) using different ratios of components were obtained by one step method. Molar compositions of PU microparticles were estimated by determination of nitrogen, isocyanate and hydroxyl groups. PU carriers which were synthesized using optimal initial molar ratios of PVA and HMDI were applied for immobilization of maltogenase (MG) from Bacillus stearothermophilus. Immobilized enzyme exhibited higher catalytic activity and enhanced temperature stability in comparison with the native MG. Maximal loading 7.78 mg/g wet carrier was reached when PU microparticles with initial molar ratio of PVA and HMDI = 1:3 was used as a carrier for immobilization. The high efficiency of immobilization (EI) was obtained using PU microparticles when initial molar ratio of HMDI and PVA was 1:1–1:10. High stability of MG immobilized onto PU microparticles during storage was demonstrated. Immobilized starch hydrolyzing enzyme was successfully tested in batch and column type reactors for hydrolysis of potato starch. MG immobilized onto PU enables easy separation from the reaction medium and reuse of the immobilized preparation over seven reaction cycles in bath operation and at least three cycles in column type reactor.     

Characterization and optimization of β-galactosidase immobilization process on a mixed-matrix membrane

β-Galactosidase is an important enzyme catalyzing not only the hydrolysis of lactose to the monosaccharides glucose and galactose but also the transgalactosylation reaction to produce galacto-oligosaccharides (GOS). In this study, β-galactosidase was immobilized by adsorption on a mixed-matrix membrane containing zirconium dioxide. The maximum β-galactosidase adsorbed on these membranes was 1.6 g/m², however, maximal activity was achieved at an enzyme concentration of around 0.5 g/m². The tests conducted to investigate the optimal immobilization parameters suggested that higher immobilization can be achieved under extreme parameters (pH and temperature) but the activity was not retained at such extreme operational parameters. The investigations on immobilized enzymes indicated that no real shift occurred in its optimal temperature after immobilization though the activity in case of immobilized enzyme was better retained at lower temperature (5 °C). A shift of 0.5 unit was observed in optimal pH after immobilization (pH 6.5 to 7). Perhaps the most striking results are the kinetic parameters of the immobilized enzyme; while the Michaelis constant (K_m) value increased almost eight times compared to the free enzyme, the maximum enzyme velocity (V_max) remained almost constant.     

Application of immobilized bovine enterokinase in repetitive fusion protein cleavage for the production of mucin 1

Bovine enterokinase is a serine protease that catalyzes the hydrolysis of peptide bonds and plays a key role in mammalian metabolism. Because of its high specificity towards the amino acid sequence (Asp)₄-Lys, enterokinase is a potential tool for the cleavage of fusion proteins, which are gaining more importance in biopharmaceutical production. A candidate for adaptive cancer immunotherapy is mucin 1, which is produced recombinantly as a fusion protein in CHO cells. Here, we present the first repetitive application of immobilized enterokinase for the cleavage of the mucin fusion protein. The immobilization enables a facile biocatalytic process due to simplified separation of the biocatalyst and the target protein. Immobilized enterokinase was applied in a maximum of 18 repetitive reactions. The enzyme utilization (total turnover number) was increased significantly 419-fold compared to unbound enzyme by both immobilization and optimization of process conditions. Slight enzyme inactivation throughout the reaction cycles was observed, but was compensated by adjusting the process time accordingly. Thus, complete fusion protein cleavage was achieved. Furthermore, we obtained isolated mucin 1 with a purity of more than 90% by applying a simple and efficient purification process. The presented results demonstrate enterokinase to be an attractive tool for fusion protein cleavage.     

Improvement of the functional properties of a thermostable lipase from alcaligenes sp. via strong adsorption on hydrophobic supports

Lipase QL from Alcaligenes sp. is a quite thermostable enzyme. For example, it retains 75% of catalytic activity after incubation for 100 h at 55 °C and pH 7.0. Nevertheless, an improvement of the enzyme properties was intended via immobilization by covalent attachment to different activated supports and by adsorption on hydrophobic supports (octadecyl-sepabeads). This latter immobilization technique promotes the most interesting improvement of enzyme properties: (a) the enzyme is hyperactivated after immobilization: the immobilized preparation exhibits a 135% of catalytic activity for the hydrolysis of p-nitrophenyl propionate as compared to the soluble enzyme; (b) the thermal stability of the immobilized enzyme is highly improved: the immobilized preparation exhibits a half-life time of 12 h when incubated at 80 °C, pH 8.5 (a 25-fold stabilizing factor regarding to the soluble enzyme); (c) the optimal temperature was increased from 50 °C (soluble enzyme) up to 70 °C (hydrophobic support enzyme immobilized preparations); (d) the enantioselectivity of the enzyme for the hydrolysis of glycidyl butyrate and its dependence on the experimental conditions was significantly altered. Moreover, because the enzyme becomes reversibly but very strongly adsorbed on these highly hydrophobic supports, the lipase may be desorbed after its inactivation and the support may be reused. Very likely, adsorption occurs via interfacial activation of the lipase on the hydrophobic supports at very low ionic strength. On the other hand, all the covalent immobilization protocols used to immobilize the enzyme hardly improved the properties of the lipase.     

Thermodynamic and kinetic aspects of the hydrolysis of ethyl(R)-2- (benzyloxycarbonylamino)-3-sulfamoylpropionate in the presence of free and immobilized alpha-chymotrypsin

The hydrolysis of ethyl (R)-2-(benzyloxycarbonylamino)-3-sulfamoylpropionate (blocked cysteic acid S-amide) by native and immobilized alpha-chymotrypsin was studied. The experiments were performed using a constant enzyme/substrate ratio of 1:8 and at a temperature of 10-40 degrees C; the immobilized enzyme was bound to a dialdehyde cellulose matrix. A kinetic equation (Eq.10) was found to be applicable which confirms that the mechanism of the enzyme reaction consists of several stages, irrespective of the enzyme state. The temperature dependence of the reaction velocity was investigated and applied using the Arrhenius equation. The constant value thus obtained for the activating energy showed that the active centres retained their character during immobilization. The differences between the velocities of the reaction with immobilized and with native enzyme corresponded to the different number of active centres during the reaction time. Based on these results a kinetic model of the mechanism of the studied reaction is presented which includes an initial balanced stage of the chemosorption type.     

Immobilization conditions of ketoreductase on enantioselective reduction in a gas-solid bioreactor

The immobilization conditions of commercial ketoreductase for continuous enantioselective reduction in the gas-phase reaction were investigated with respect to the immobilization efficiency (residual activity and protein loading) and the gas-phase reaction efficiency (initial reaction rate, half-life, and enantioselectivity). For the analyses, ketoreductase was first immobilized by physical deposition on glass supports and the reduction of 2-butanone to (S)-2-butanol with the concomitant regeneration of NADH by 2-propanol was used as a model reaction. The optimal conditions of enzyme immobilization were obtained using an absolute pressure of 100 hPa for drying, a pH between 6.5 and 7.0, and a buffer concentration of 50 mM. The buffer concentration in particular had a strong effect on both the enzyme activity and enantioselectivity. Under optimal immobilization conditions, the thermostability of ketoreductase in the gas-phase system was enhanced compared to the aqueous-phase system, while the enantioselectivity was successfully maintained at a level identical to that of the native enzyme. These results indicate that the gas-phase reaction has a great potential for industrial production of chiral compounds, but requires careful optimization of immobilization conditions for the reaction to progress effectively.     

Production of xylobiose from the autohydrolysis explosion liquor of corncob using Thermotoga maritima xylanase B (XynB) immobilized on nickel-chelated Eupergit C

In this study, a thermostable recombinant xylanase B (XynB) from Thermotoga maritima MSB8 was immobilized on nickel-chelated Eupergit C 250L. This immobilized XynB was then used to hydrolyze the autohydrolysis explosion liquor of corncob (AELC) in a packed-bed enzyme reactor for continuous production of xylooligosaccharides, especially xylobiose. When tested in batch hydrolysis of AELC, the immobilized XynB still retained its relative activity of 92.5% after 10 cycles of hydrolysis at 90 degrees C. The immobilized XynB retained 83.6% of its initial hydrolysis activity even after 168 h of hydrolysis reaction at 90 degrees C and demonstrated a half-life time of 577.6 h (24 days) for continuous hydrolysis. HPLC showed that xylobiose (49.8%) and xylose (22.6%) were the main hydrolysis products yielded during continuous hydrolysis. Xylobiose was adsorbed on an activated charcoal column and eluted with a linear gradient of 15% (v/v) ethanol to yield xylobiose with 84.7% of recovery. Also, the purity of xylobiose was up to 97.2% as determined by HPLC. Therefore, the immobilized XynB was suitable for the efficient production of xylobiose from AELC. This is the first report on the immobilization of xylanase for xylobiose production.     

Use of polyelectrolyte complex-stabilized calcium alginate gel for entrapment of beta-amylase

Calcium alginate gel stabilized with a polyelectrolyte complex (PEC) consisting of potassium poly(vinyl alcohol) sulfate (KPVS) and trimethylammonium glycol chitosan iodide (TGCI) was used for the immobilization of beta-amylase. The immobilization was made by gelling aqueous droplets of enzyme solution including both sodium alginate and KPVS in a CaCl(2) solution containing TGCI. The activity of the enzyme entrapped into the stabilized gel beads was evaluated by studying the batch reaction kinetics of enzyme-catalyzed hydrolysis of maltotetraose. Repeated kinetic measurements, totaling 18, were carried out at fixed time intervals. After each measurement the beads were stirred for 1 day in a freshly prepared 10 mM NaCl solution at 3 degrees C. It was found that the immobilized system remained stable without leading to a serious loss of the activity or to a large leakage of the enzyme from the support. This was explained as being due to a PEC-crosslinked contracted network structure of the stabilized gel matrix.