Comparison of the kinetics and factors affecting the stabilities of chitin-immobilized naringinases from two fungal sources

Naringinases from both Penicillium sp. and Aspergillus niger were compared for their enzyme kinetics and the effects of sugars on the enzyme activities. Lineweaver-Burk plots showed that glucose, fructose and rhamnose were all competitive inhibitors for α-rhamnosidase of naringinase from Penicillium sp. and non-competitive inhibitors for the same enzyme from A. niger, When naringinase from Penicillium sp. was immobilized on chitin and used successively for the hydrolysis of p-nitrophenyl-α-rhamnoside or naringin in a simulated fruit juice system or grapefruit juice, it was observed that the enzyme column was very stable. Such results are in contrast to what has bee observed for naringinase fron A. niger. Therefore, it is quite possible that the sugars in the fruit juice which play a role as competitive or non-competitive inhibitors on naringinase may account for the stability of the enzyme column during successive debittering of grapefruits juice.     

Comparative studies on immobilized laccase behaviour in packed-bed and batch reactors

Extracellular laccase produced by the wood-rotting fungus Cerrena unicolor was immobilized covalently via glutaraldehyde to cellulose-based carrier Granocel. Laccase was partially purified by membrane concentration and diafiltration followed by precipitation with acetone. Five-fold increase in the measured activity of immobilized enzyme was obtained when six times purer laccase was used for immobilization. For the best preparation, with very high activity of 2053 U per 1 mL of the carrier, thermal- and pH-stability, and activity profiles were determined. Experiments carried out in a batch reactor showed that k_cat/K_m for immobilized enzyme (0.65) is three times lower than the value obtained for the native laccase (2.19) whereas k_cat/K_m estimated from continuous reactor (1.50) is notably closer to that for the native enzyme. Continuous process probably reflects more precisely kinetics of the reaction accompanied by simultaneous product precipitation on the carrier’s surface. Operational stability of immobilized laccase was tested in continuous mode operation with ABTS, guaiacol and trichlorophenol as substrates and showed that packed-bed reactor is unprofitable system for laccase immobilized on Granocel carrier due to the high bed compaction. However, excellent stability of the preparation was noted under 20 successive runs in the well mixed tank reactor and better ability towards trichlorophenol biotransformation was observed in the case of immobilized laccase.     

Soybean hull peroxidase immobilization on macroporous glycidyl methacrylates with different surface characteristics

Soybean hull peroxidase (SHP, E.C. 1.11.1.7) was immobilized by a glutaraldehyde and periodate method onto series of macroporous copolymers of glycidyl methacrylate (GMA) and ethylene glycol dimethacrylate (EGDMA), poly(GMA-co-EGDMA) with various surface characteristics and pore size diameters ranging from 44 to 200 nm. Glutaraldehyde immobilization method and poly(GMA-co-EGDMA) named SGE 20/12 with pore sizes of 120 nm gave immobilized enzyme with highest specific activity of 25 U/g. Deactivation studies showed that immobilization increased stability of SHP and that surface characteristics of the used copolymer had a major influence on a stability of immobilized enzyme at high temperatures and in an organic solvent. The highest thermostability was obtained using the copolymer SGE 20/12 with pore size of 120 nm, while the highest stability in dioxane had SHP immobilized onto copolymer SGE 10/4 with pore size of 44 nm. Immobilized SHP showed a wider pH optimum as compared to the native enzyme especially at alkaline pH values and 3.2 times increased K _m value for pyrogallol. After 6 cycles of repeated use in batch reactor, immobilized SHP retained 25 % of its original activity. Macroporous copolymers with different surface characteristics can be used for fine tuning of activity and stability of immobilized SHP to obtain a biocatalyst suitable for phenol oxidation or polymer synthesis in organic solvents.     

Purification, Immobilization, and Some Properties of Glucose Isomerase from Streptomyces flavogriseus

Glucose isomerase (EC 5.3.1.5) produced from Streptomyces flavogriseus was purified by fractionation with (NH₄)₂SO₄ and chromatography on diethylaminoethyl (DEAE)-cellulose and DEAE-Sephadex A-50 columns. The purified enzyme was homogeneous as shown by ultracentrifugation and sodium dodecyl sulfate-polyacrylamide gel electrophoresis. Benzyl DEAE-cellulose, triethylaminoethyl-cellulose, and DEAE-cellulose were effective in the immobilization of partially purified glucose isomerase. Several differences in properties were found between purified soluble enzyme, immobilized enzyme (DEAE-cellulose-glucose isomerase), and heat-treated whole cells. Glucose and xylose served as substrate for the enzyme. Whole cells had the highest K_m values for glucose and xylose; the soluble enzyme had the lowest values. The optimum temperature for activity of the soluble and immobilized enzymes was 70°C; that for whole cells was 75°C. The pH optimum for the three enzyme preparations was 7.5. Magnesium ion or Co²⁺ was required for enzyme activity; an addition effect resulted from the presence of both Mg²⁺ and Co²⁺. The enzyme activity was inhibited by Hg²⁺, Ag⁺, or Cu²⁺. The conversion ratio of the enzyme for isomerization was about 50%. The soluble and immobilized enzymes showed a greater heat stability than whole cells. The soluble enzyme was stable over a slightly wider pH (5.0 to 9.0) range than the immobilized enzyme and whole cells (pH 5.5 to 9.0). The molecular weight of the enzyme determined by the sedimentation equilibrium method was 171,000. A tetrameric structure for the enzyme was also indicated. After operating at 70°C for 5 days, the remaining enzyme activity of the immobilized enzyme and whole cells, which were used for the continuous isomerization of glucose in a plug-flow type of column in the presence of Mg²⁺ and Co²⁺, was 75 and 55%, respectively. Elimination of Co²⁺ decreased operational stability.     

Development of Bed Reactor Using Brick Dust Immobilized CIVI-Cellulase from Seeds of Cowpea (Vigna sinensis L)

Cellulase extracted from seeds of Cowpea (Vigna sinensis L var VITA-4) was partially purified and immobilized on brick dust as solid support via glutaraldehyde. The percentage retention of the enzyme activity on brick dust was nearly 85%. After immobilization specific activity of the enzyme increased from 0.275 to 0.557 U mg^?1 protein with about 2 fold enrichment. The optimum pH and temperature of soluble enzyme were determined as pH 4.6 and WC, respectively whereas immobilized enzyme showed at pH 5.0 and 37°C, respectively. The V_max values for soluble and immobilized enzyme were determined as 6.67 and 1.25 mg min^?1, respectively whereas K_m values were 4.35 and 4.76 mg ml^?1, respectively. The immobilized enzyme displayed higher thermal stability than soluble enzyme and retained about 50% of its initial activity after 12 reuses. Immobilized enzyme was packed in an indigenously designed double walled glass bed reactor for continuous production of reducing sugars.     

Continuous production of L-aspartic acid by immobilized aspartase

Various methods were tried for the immobilization of aspartase, and the preparation having the highest activity was obtained when partially purified aspartase from Escherichia coli was entrapped into polyacrylamide gel Iattice. Enzymatic properties of the immobilized aspartase were investigated and compared with those of the native aspartase. With regard to optimum pH, temperature, concentration of Mn⁺⁺, kinetic constants and heat stability, no marked difference was observed between the native and immobilized aspartases. By employing an enzyme column packed with the immobilized aspartase, conditions for continuous production of L -aspartic acid from ammonium fumarate were investigated. When a solution of 1M ammonium fumarate (pH 8.5, containing 1mM MnCl₂) was passed through the aspartase column at the flow rate of SV = 0.08 at 37°C, the highest rate of reaction was attained. From the column effluents, L-aspartic acid was obtained in a good yield.     

Characterization of molecular-sieve-bound inulinase

The enzyme inulinase (2,1-β-d-fructan fructanohydrolase, EC 3.2.1.7), prepared from Kluyveromyces marxianus has been immobilized using an inorganic solid support, molecular sieve 4A via the metal link method. The immobilized enzyme had around 22 units of inulinase activity per g of the support with retention of 72% of the original activity. The optimum protein to molecular sieve ratio for the maximum retention of inulinase activity was 9 mg/g molecular sieve. The properties of soluble and immobilized enzyme differed in many respects. The optimum pH of the enzyme shifted from 6 to 5 and the optimum temperature of enzyme activity changed from 50 to 55°C. K_m values were 6.7 mM for soluble enzyme and 10 mM for immobilized enzyme. The heat stability of the enzyme was improved by immobilization. Immobilized enzyme retained about 76% of the original activity after 40 days of storage at room temperature (30±2°C).     

Recycling of textile bleaching effluents for dyeing using immobilized catalase

Catalase was immobilized on alumina carrier and crosslinked with glutaraldehyde. Storing stability, temperature and pH profiles of enzyme activity were studied in a column reactor with recirculation and in a batch stirred-tank reactor. The immobilized enzyme retained 44% of its activity at pH 11, 30 °C and 90% at 80 °C, pH 7. The half-life time of the immobilized catalase was increased to 2 h at pH 12, and 60 °C. Acceptable results were achieved when the residual water from the washing process of H₂O₂-bleached fabrics was treated with the immobilized enzyme and then reused for dyeing.     

Immobilization of Bacillus licheniformis 5A1 milk-clotting enzyme and characterization of its enzyme properties

Milk-clotting enzyme from Bacillus licheniformis 5A1 was immobilized on Amberlite IR-120 by ionic binding. Almost all the enzyme activity was retained on the support. The immobilized milk-clotting enzyme was repeatedly used to produce cheese in a batch reactor. The production of cheese was repeated 5 times with no loss of activity. The specific activity calculated on a bound-protein basis was slightly higher than that of free enzyme. The free and immobilized enzyme were highly tolerant to repeated freezing and thawing. The optimum temperature for milk-clotting activity was 70 °C with the free enzyme whereas, it was ranged from 70 to 80 °C with the immobilized milk-clotting enzyme. The activation energy (E _A) of the immobilized milk-clotting enzyme was lower than the free enzyme (E _A = 1.59 and 1.99 Kcal mol⁻¹ respectively). The immobilized milk-clotting enzyme exhibited great thermal stability. The milk-clotting optimum pH was 7.0 for both free and immobilized enzyme. The Michaelis constant K _m of the immobilized milk-clotting enzyme was slightly lower than the free enzyme.     

Hydrolysis of inulin from Jerusalem artichoke by inulinase immobilized on aminoethylcellulose

Purified inulinase (inulase, 2,1-β-d-fructan fructanohydrolase, EC 3.2.1.7) of Kluyveromyces fragilis has been immobilized on 2-aminoethyl-cellulose by treatment with 2% glutaraldehyde in 0.05 m phosphate buffer, pH 7.0, for 2 h at room temperature. The immobilized enzyme preparation had 39.3 units inulinase activity per gram dried matrix, with 53.4% recovery yield of activity, and showed good operational stability in the presence of substrate, inulin or the tuber extract of Jerusalem artichoke. Optimum pH and temperature were 5.5 and 45°C, respectively. In a batch reactor, the conversion was 90% ($\text{d}\text{-fructose/}\text{d}\text{-glucose}\text{= 76/24}$) and 34 mg d-fructose per ml was produced from the artichoke tuber extract by the immobilized inulinase in 20 h. In column reactor packed with 28 ml immobilized enzyme, the following conditions were found to be optimal: height/diameter ratio of column, 10.3; space time, 3.8 h; temperature, 40°C. Operation under these conditions gave 90% conversion of a 7% inulin solution and the productivity was 102 mmol l^?1 h^?1.     

Purification and characterization of methanol dehydrogenase of Methylobacterium nodulans rhizosphere phytosymbionts

Methanol dehydrogenase (MDH) of the facultative methylotrophic phytosymbiont Methylobacterium nodulans has been purified for the first time to an electrophoretically homogeneous state and characterized. The native protein with a molecular mass of 70 kDa consists of large (60 kDa) and small (6.5 kDa) subunits. The purified protein displayed a spectrum identical to that of pyrroloquinoline quinone (PQQ)-containing MDH, pI 8.7, pH optimum in the range 9–10. The enzyme was inactive in the absence of ammonium or methylamine and exhibited a wide substrate specificity with regard to C₁–C₅ alcohols with the high-est affinity to methanol (K _M = 70 μM), but it did not oxidize benzyl and secondary alcohols. The apparent K _M values to primary alcohols increased with the length of the carbon chain. The enzyme was characterized by a high stability level even in the absence of a substrate. An immobilized enzyme was used for amperometric methanol detection.     

Glutathione S-transferase from the diamond back moth (Plutella xylostella linnaeus)

Glutathione S-transferase was present in all the developmental stages of Plutella xylostella. The enzyme levels increased rapidly and reached a maximum at the pupal stage and then declined towards adulthood. The resistant strain was found to contain between 3–4 times more glutathione S-transferase than the susceptible strain. However, the enzyme from both the strains had similar K_m values for GSH and DNCB, respectively. The crude enzyme had an optimum pH of 8.3 and its activity was affected by buffer molarity. The enzyme was completely inactivated on dialysis and the stability of the enzyme in the crude supernatant could be maintained in the presence of 1 mM concentrations of either GSH, 2-mercaptoethanol or cysteine. Metal ions had no effect on the stability of the enzyme. Data from Arrhenius plots, column chromatographic techniques and isoelectric focusing suggested the presence of a single form of the enzyme. The enzyme had an isoelectric point of 9.26 and a molecular weight of 36,400.     

Studies on nucleotidases in plants: Fluorescence and kinetic properties of nucleotide pyrophosphatase from mung bean (Phaseolus aureus) seedlings

Nucleotide pyrophosphatase of mung bean seedlings has earlier been isolated in our laboratory in a dimeric form (M_r 65,000) and has been shown to be converted to a tetramer by AMP and to a monomer by p-hydroxymercuribenzoate. All the molecular forms were enzymatically active with different kinetic properties. By a modified procedure using blue-Sepharose affinity chromatography, we have now obtained a dimeric form of the enzyme which is desensitized to AMP interaction. The molecular weight of the desensitized form of the enzyme was found to be the same as that of the native dimeric enzyme. However, the desensitized enzyme functioned with a linear time course, contrary to the biphasic time course exhibited by the native enzyme. In addition, it was not converted to a tetramer on the addition of AMP, had only one binding site for adenine nucleotides, and p-hydroxy-mercuribenzoate had no effect on the time course of the reaction or on the molecular weight of the enzyme. The temperature optimum of the desensitized enzyme was found to be 67 °C in contrast to the optimum of 49 °C for the native dimer. Fifty percent of the tryptophan residues of the desensitized enzyme were not accessible for quenching by iodide. Fluorescence studies gave K_d values of 0.34, 2.2, and 0.8 mm for AMP, ADP, and ATP, which were close to the K_i values of 0.12, 2.2, and 0.9 mm, respectively, for these nucleotides. The binding and inhibition studies with AMP and its analogs showed that the 6-amino group and the 5′-phosphate group were essential for the inhibition of the enzyme activity.     

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.     

Immobilization of chloroperoxidase onto highly hydrophilic polyethylene chains via bio-conjugation: Catalytic properties and stabilities

Chloroperoxidase (CPO) was covalently immobilized on poly(hydroxypropyl methacrylate-co-polyethyleneglycole-methacrylate) membranes, which were characterized, by swelling test, FT-IR spectroscopy, scanning electron microscopy, and contact angle measurement. The K_m and V_max values for free and immobilized CPO were found to be 34.6 and 47.2 μM, and 287.5 and 245.2 U/mg protein, respectively. The optimum pH for both the free and immobilized enzyme was observed at 3.0. The immobilized enzyme showed wide pH and temperature profiles. Most importantly, the increased thermal, storage and operational stability of immobilized CPO should depend on the creation of a comfortable strong hydrophilic microenvironment on the designed support to the host enzyme molecule.     

Immobilization of glucoamylase on DEAE-cellulose activated with chloride compounds

Partially purified glucoamylase (1,4-α-d-glucan glucohydrolase, EC 3.2.1.3) from Aspergillus niger NRRL 330 has been immobilized on DEAE-cellulose activated with cyanuric chloride in 0.2 m acetate buffer, pH 4.2. In the matrix-bound glucoamylase, enzyme yield was 20 mg g^?1 of support, corresponding to 40 200 units g^?1 of DEAE support. Binding of the enzyme narrows the pH optimum from 3.8–5.2 to 3.6. Thermal stability of the bound glucoamylase enzyme was decreased although it showed a higher temperature optimum (70°C) than the free form (55°C). The rate of reaction of glucoamylase was also changed after immobilization. V_max values for free and bound enzyme were 36.6 and 22.6 μmol d-glucose ml^?1 min^?1 and corresponding K_m values were 3.73 and 4.8 g l^?1 respectively. Free and immobilized enzyme when used in the saccharification process gave 84 and 56% conversion of starch to d-glucose, respectively. The bound enzyme was quite stable and in the batch process it was able to operate for about five cycles without any loss of activity.     

Investigation of the operational stabilities and kinetics of glucoamylase immobilized on alkylamine derivatives of titanium(IV)-activated porous inorganic supports

Glucoamylase (exo-1,4-α-d-glucosidase, EC 3.2.3.1) was coupled to several porous silica matrices by an improved metal-link/chelation process using alkylamine derivatives of titanium(IV)-activated supports. In order to select the titanium activation procedure which gave stable enzyme preparations, long-term stability tests were performed. The immobilized glucoamylase preparations, in which the carrier was activated to dryness with a 15% w/v TiCl₄ solution, displayed very stable behaviour, with half-lives of ～60 days. The optimum operating conditions were determined for these preparations. There are significant differences between the behaviour of the immobilized enzyme and the free enzyme. The apparent K_m increased on immobilization due to diffusional resistances. The pH optimum for the immobilized preparation showed a slight shift to acid pH relative to that of the soluble enzyme. Also, the optimum temperature descreased to 60°C after immobilization. In order to test Michaelis-Menten kinetics at high degrees of conversion, time-course analysis of soluble starch hydrolysis was performed. It was observed that simple Michaelis-Menten kinetics are not applicable to the free/immobilized glucoamylase-starch system at high degrees of conversion.     

Immobilization and characterization of human carbonic anhydrase I on amine functionalized magnetic nanoparticles

In this study, we synthesized magnetic nanoparticles (MNPs) by co-precipitation method. After that, silica coating with tetraethyl orthosilicate (TEOS) (SMNPs), amine functionalization of silica coated MNPs (ASMNPs) by using 3-aminopropyltriethoxysilane (APTES) were performed, respectively. After activation with glutaraldehyde (GA) of ASMNPs, human carbonic anhydrase (hCA I) was immobilized on ASMNPs. The characterization of nanoparticles was performed by transmission electron microscopy (TEM), fourier transform infrared spectroscopy (FT-IR), X-ray powder diffraction (XRD) and vibrating sample magnetometer (VSM). The immobilization conditions such as GA concentration, activation time of support with GA, enzyme amount, enzyme immobilization time were optimized. In addition of that, optimum conditions for activity, kinetic parameters (K_m, V_max, k_cat, kcat/K_m), thermal stability, storage stability and reusability of immobilized enzyme were determined.The immobilized enzyme activity was optimum at pH 8.0 and 25 °C. The K_m value of the immobilized enzyme (1.02 mM) was higher than the free hCA I (0.48 mM). After 40 days incubation at 4 °C and 25 °C, the immobilized hCA I sustained 89% and 85% of its activity, respectively. Also, it sustained 61% of its initial activity after 13 cycles. Such results revealed good potential of immobilized enzyme for various applications.     

Characterization of functionally active immobilized carbonic anhydrase purified from sheep blood lysates

Carbonic anhydrase (CA) catalyzes the reversible reaction of hydration of CO₂ to bicarbonate and the dehydration of bicarbonate back to CO₂. Sequestration of CO₂ from industrial processes or breathing air may require a large amount of highly active and stable CA. Therefore, the objectives of the present study were to purify large amounts of CA from a cheap and easily accessible source of the enzyme and to characterize the enzymatic and kinetic properties of soluble and immobilized enzyme. We recovered 80% of pure enzyme with a specific activity of 4870 EU/mg protein in a single step using sheep blood lysates from slaughter house waste products and CA specific inhibitor affinity chromatography. Since affinity pure CA showed both anhydrase and esterase activities, we measured the esterase activities for enzymology. The Michaelis–Menten constant, K_M, pH optimum, activation energy, and thermal stability of soluble enzymes were 8 × 10^?2 M, 7.3 pH, 7.3 kcal/mol and 70 °C, respectively.The immobilization of the enzyme to Affigel-10 was very efficient and 83% of purified enzyme was immobilized. The immobilized enzyme showed a K_M of 5 × 10^?2 M and activation energy of 8.9 kcal/mol, suggesting a better preference of substrate for immobilized enzyme in comparison to soluble enzyme. In contrast to soluble enzyme, immobilized enzyme showed relatively higher activity at pH 6–8. From these results, we concluded that a shift in pH profile toward acidic pH is due to modification of lysine residues involved in the immobilization process. The immobilized enzyme was stable at higher temperatures and showed highest activity at 80 °C. The activity of immobilized enzyme in a flow reactor at 0.5–2.2 ml/min flow rate was unaffected. Collectively, results from the present study suggested the application of blood lysate waste from animal slaughterhouses for purification of homogeneous enzyme for CO₂ capture in a flow reactor.     

Hen egg white as a feeder protein for lipase immobilization

Enzyme stabilization via immobilization is one of the preferred processes as it provides the advantages of recovery and reusability. In this study, Thermomyces lanuginosus lipase has been immobilized through crosslinking using 2% glutaraldehyde and hen egg white, as an approach towards CLEA preparation. The immobilization efficiency and the properties of the immobilized enzyme in terms of stability to pH, temperature, and denaturants was studied and compared with the free enzyme. Immobilization efficiency of 56% was achieved with hen egg white. The immobilized enzyme displayed a shift in optimum pH towards the acidic side with an optimum at pH 4.0 whereas the pH optimum for free enzyme was at pH 6.0. The immobilized enzyme was stable at higher temperature retaining about 83% of its maximum activity as compared to the free enzyme retaining only 41% activity at 70 °C. The denaturation of lipase in free form was rapid with a half-life of 2 h at 60 °C and 58 min at 70 °C as compared to 12 h at 60 °C and 2 h at 70 °C for the immobilized enzyme. The effect of denaturants, urea and guanidine hydrochloride on the free and immobilized enzyme was studied and the immobilized enzyme was found to be more stable towards denaturants retaining 74% activity in 8 M urea and 98% in 6 M GndHCl as compared to 42% and 33% respectively in the case of free enzyme. The apparent K_m (2.08 mM) and apparent V_max (0.95 μmol/min) of immobilized enzyme was lower as compared to free enzyme; K_m (8.0 mM) and V_max (2.857 μmol/min). The immobilized enzyme was reused several times for the hydrolysis of olive oil.