A novel method for the immobilization of glucoamylase onto polyglutaraldehyde-activated gelatin

A novel method was developed for the immobilization of glucoamylase from Aspergillus niger. The enzyme was immobilized onto polyglutaraldehyde-activated gelatin particles in the presence of polyethylene glycol and soluble gelatin, resulting in 85% immobilization yield. The immobilized enzyme has been fully active for 30 days. In addition, the immobilized enzyme retained 90 and 75% of its activity in 60 and 90 days, respectively. The enzyme optimum conditions were not affected by immobilization and the optimum pH and temperature for free and immobilized enzyme were 4 and 65 °C, respectively. The kinetic parameters for the hydrolysis of maltodextrin by free and immobilized glucoamylase were also determined. The K_m values for free and immobilized enzyme were 7.5 and 10.1 g maltodextrin/l, respectively. The V_max values for free and immobilized enzyme were estimated as 20 and 16 μmol glucose/(min μl enzyme), respectively. The newly developed method is simple yet effective and could be used for the immobilization of some other enzymes.     

Immobilization of phytase on epoxy-activated Sepabead EC-EP for the hydrolysis of soymilk phytate

In this work, an active phytase concentrated extract from soybean sprout was immobilized on a polymethacrylate-based polymer Sepabead EC-EP which is activated with epoxy groups. The immobilized enzyme exhibited an activity of 0.1 U/g of carrier and activity yield of 64.7%. The optimum temperature and pH for the activity of both free and immobilized enzymes were found as 60 °C and pH 5.0, respectively. The immobilized enzyme was more stable than free enzyme in the range of pH 3.0–8.0 and more than 70% of the original activity was recovered. Both the enzymes completely retained nearly about 84% of their original activity at 65 °C. The K_m and V_max values were measured as 5 mM and 0.63 U/mg for free enzyme and 12.5 mM and 0.71 U/mg for immobilized enzyme, respectively. Free and immobilized soybean sprout phytase enzymes were also used in the biodegradation of soymilk phytate. The immobilized enzyme hydrolysed 92.5% of soymilk phytate in 7 h at 60 °C, as compared with 98% hydrolysis observed for the native enzyme over the same period of time. The immobilization procedure on Sepabead EC-EP is very cheap and also easy to carry out, and the features of the immobilized enzyme are very attractive that the potential for practical application is considerable.     

Immobilization of Bacillus circulans β-galactosidase and its application in the synthesis of galacto-oligosaccharides under repeated-batch operation

A highly active and stable derivate of immobilized Bacillus circulans β-galactosidase was prepared for the synthesis of galacto-oligosaccharides (GOS) under repeated-batch operation. B. circulans β-galactosidase was immobilized on monofunctional glyoxyl agarose and three heterofunctional supports: amino-, carboxy-, and chelate-glyoxyl agarose. Glyoxyl agarose was the support with highest immobilization yield and stability being selected for the optimization of immobilization conditions and application in GOS synthesis. A central composite rotatable design was conducted to optimize contacted protein and immobilization time, using maximum catalytic potential as the objective function. Optimal conditions of immobilization were 28.9 mg/g and 36.4 h of contact, resulting in a biocatalyst with 595 IU/g and a half-life 89-fold higher than soluble enzyme. Immobilization process did not alter the synthetic capacity of β-galactosidase, obtaining the same GOS yield and product profile than the free enzyme. GOS yield and productivity remained unchanged along 10 repeated batches, with values of 39% (w/w) and 5.7 g GOS/g of biocatalyst·batch. Total product obtained after 10 batches of reaction was 56.5 g GOS/g of biocatalyst (1956 g GOS/g protein). Cumulative productivity in terms of mass of contacted protein was higher for the immobilized enzyme than for its soluble counterpart from the second batch of synthesis onwards.     

Influence of whole microalgal cell immobilization and organic solvent on the bioconversion of androst-4-en-3,17-dione to testosterone by Nostoc muscorum

The use of free, immobilized and reused immobilized cells of the microalga Nostoc muscorum was studied for bioconversion of androst-4-en-3,17-dione (AD) to testosterone in hexadecane. Among polymers such as agar, agarose, κ-carrageenan, polyacrylamide, polyvinyl alcohol, and sodium alginate that were examined for cell entrapment, sodium alginate with a concentration of 2% (w/v) proved to be the proper matrix for N. muscorum cells immobilization. The bioconversion characteristics of immobilized whole algal cells at ranges of temperatures, substrate concentrations, and shaking speeds were studied followed by a comparison with those of free cells. The conditions were 30 °C, 0.5 g/L, and 100 rpm, respectively. The immobilized N. muscorum showed higher yield (72 ± 2.3%) than the free form (24 ± 1.3%) at the mentioned conditions. The bioconversion yield did not decrease during reuse of immobilized cells and remained high even after 5 batches of bioreactions while Na-alginate 3% was used; however, reuse of alginate 2% beads did not give a satisfactory result.     

Continuous production of oligoglucuronans by immobilized glucuronan lyase

A glucuronan lyase was incubated with sepharose matrices pre-activated with N-hydroxysuccinimide (NHS), cyanogen bromide (CNBr) or epoxy. The CNBr- and NHS-activated gels showed satisfactory immobilization yields whereas no enzyme could be immobilized using the epoxy coupling group. Glucuronan lyase immobilized on CNBr-gel ensured rapid conversion of several glucuronans into oligomers with an enzymatic activity identical to that of the free enzyme. As classically observed when using free enzymes, the acetylation degree of glucuronan limited enzyme activity. Nevertheless, this immobilized system made it easier to obtain accurately oligomers with different polymerization degrees, notably in modifying the glucuronans residence times in column. Thus oligoglucuronan pools with polymerization degrees between 2 and 25 could be obtained with a productivity ranging from 120 mg h^?1 to 1.2 g h^?1 using 0.9 ml of chromatographic gel with immobilized glucuronan lyase. This methodology opens the way to continuous and large oligoglucuronan productions.     

Immobilization of α-galactosidase on galactose-containing polymeric beads

Industrial application of α-galactosidase requires efficient methods to immobilize the enzyme, yielding a biocatalyst with high activity and stability compared to free enzyme. An α-galactosidase from tomato fruit was immobilized on galactose-containing polymeric beads. The immobilized enzyme exhibited an activity of 0.62 U/g of support and activity yield of 46%. The optimum pH and temperature for the activity of both free and immobilized enzymes were found as pH 4.0 and 37 °C, respectively. Immobilized α-galactosidase was more stable than free enzyme in the range of pH 4.0–6.0 and more than 85% of the initial activity was recovered. The decrease in reaction rate of the immobilized enzyme at temperatures above 37 °C was much slower than that of the free counterpart. The immobilized enzyme shows 53% activity at 60 °C while free enzyme decreases 33% at the same temperature. The immobilized enzyme retained 50% of its initial activity after 17 cycles of reuse at 37 °C. Under same storage conditions, the free enzyme lost about 71% of its initial activity over a period of 7 months, whereas the immobilized enzyme lost about only 47% of its initial activity over the same period. Operational stability of the immobilized enzyme was also studied and the operational half-life (t_1/2 was determined as 6.72 h for p-nitrophenyl α-d-galactopyranoside (PNPG) as substrate. The kinetic parameters were determined by using PNPG as substrate. The K_m and V_max values were measured as 1.07 mM and 0.01 U/mg for free enzyme and 0.89 mM and 0.1 U/mg for immobilized enzyme, respectively. The synthesis of the galactose-containing polymeric beads and the enzyme immobilization procedure are very simple and also easy to carry out.     

Immobilization of catalase onto Eupergit C and its characterization

Bovine liver catalase was covalently immobilized onto Eupergit C. Optimum conditions of immobilization: pH, buffer concentration, temperature, coupling time and initial catalase amount per gram of carrier were determined as 7.5, 1.0 M, 25 °C, 24 h and 4.0 mg/g, respectively. V_max and K_m were determined as 1.4(±0.2) × 10⁵ U/mg protein and 28.6 ± 3.6 mM, respectively, for free catalase, and as 3.7(±0.4) × 10³ U/mg protein and 95.9 ± 0.6 mM, respectively, for immobilized catalase. The thermal stability of the immobilized catalase in terms of half-life time (29.1 h) was comparably higher than that of the free catalase (9.0 h) at 40 °C. Comparison of storage stabilities showed that the free catalase completely lost its activity at the end of 11 days both at room temperature and 5 °C. However, immobilized catalase retained 68% of its initial activity when stored at room temperature and 79% of its initial activity when stored at 5 °C at the end of 28 days. The highest reuse number of immobilized catalase was 22 cycles of batch operation when 40 mg of immobilized catalase loaded into the reactor retaining about 50% of its original activity. In the plug flow type reactor, the longest operation time was found as 82 min at a substrate flow rate of 2.3 mL/min when the remaining activity of 40 mg immobilized catalase was about 50% of its original activity. The resulting immobilized catalase onto Eupergit C has good reusability, thermal stability and long-term storage stability.     

Effect of kinesthetic illusion induced by visual stimulation on muscular output function after short-term immobilization

Kinesthetic illusions by visual stimulation (KiNVIS) enhances corticomotor excitability and activates motor association areas. The purpose of this study was to investigate the effect of KiNVIS induction on muscular output function after short-term immobilization. Thirty subjects were assigned to 3 groups: an immobilization group, with the left hand immobilized for 12 h (immobilization period); an illusion group, with the left hand immobilized and additionally subjected to KiNVIS of the immobilized part during the immobilization period; and a control group with no manipulation. The maximum voluntary contraction (MVC), fluctuation of force (force fluctuation) during a force modulation task, and twitch force were measured both before (pre-test) and after (post-test) the immobilization period. Data were analyzed by performing two-way (TIME × GROUP) repeated measures ANOVA. The MVC decreased in the immobilization group only (pre-test; 37.8 ± 6.1 N, post-test; 32.8 ± 6.9 N, p < 0.0005) after the immobilization period. The force fluctuation increased only in the immobilization group (pre-test; 2.19 ± 0.54%, post-test; 2.78 ± 0.87%, p = 0.007) after the immobilization period. These results demonstrate that induction of KiNVIS prevents negative effect on MVC and force fluctuation after 12 h of immobilization.     

Investigating and optimizing the immobilization of levansucrase for increased transfructosylation activity and thermal stability

Levansucrase (LS) represents a key enzyme in glycoside synthesis of novel prebiotics and β-2,6-levan. The study of the effects of immobilization parameters of LS, produced from Bacillus amyloliquefaciens, onto glyoxyl agarose-iminodiacetic acid/Cu (glyoxyl agarose-IDA/Cu) by response surface methodology revealed the significance of their interactive effects. Retention of activity was altered by interactive effects from buffer molarity/time and buffer pH/buffer molarity. The optimized immobilization conditions were identified to be a protein loading of 9.09 mg protein/g support, a buffer concentration of 608 mM at pH 6.8 and an incubation time of 49 h. Normally a reducing agent is applied to the immobilized enzyme in order to promote the formation of covalent bonds. This step was replaced with the addition of the ionic polymer polyethylenimine (PEI), which provided a better compromise between retained activity and thermal stability of the immobilized LS. Indeed, LS immobilized onto glyoxyl agarose-IDA/Cu/PEI had a retention of activity of 70.91% with a protein yield of 44.73% and an activity yield of 54.69%, while exhibiting a half-life 4.7 times higher than that of the free LS at 50 °C.     

A comparison of the kinetic properties of free and immobilized Aspergillus oryzae β-galactosidase

The objective of this work was to compare the properties of free and immobilized β-galactosidase (Aspergillus oryzae), entrapped in alginate–gelatin beads and cross-linked with glutaraldehyde. The free and immobilized forms of the enzyme showed no decrease in enzyme activity when incubated in buffer solutions in pH ranges of 4.5–7.0. The kinetics of lactose hydrolysis by the free and immobilized enzymes were studied at maximum substrate concentrations of 90 g/L and 140 g/L, respectively, a temperature of 35 °C and a pH of 4.5. The Michaelis–Menten model with competitive inhibition by galactose fit the experimental results for both forms. The K_m and V_m values of the free enzyme were 52.13 ± 2.8 mM and 2.56 ± 0.3 g_glucose/L min mg_enzyme, respectively, and were 60.30 ± 3.3 mM and 1032.07 ± 51.6 g_lactose/min m³_catalyst, respectively, for the immobilized form. The maximum enzymatic activity of the soluble form of β-galactosidase was obtained at pH 4.5 and 55 °C. Alternatively, the immobilized form was most active at pH 5.0 at 60 °C. The free and immobilized enzymes presented activation energies of 6.90 ± 0.5 kcal/mol and 7.7 ± 0.7 kcal/mol, respectively, which suggested that the immobilized enzyme possessed a lower resistance to substrate transfer.     

Effect of changing the nanoscale environment on activity and stability of nitrate reductase

Nitrate reductase (NR) is employed for fabrication of nitrate sensing devices in which the enzyme in immobilized form is used to catalyze the conversion of nitrate to nitrite in the presence of a suitable cofactor. So far, instability of immobilized NR due to the use of inappropriate immobilization matrices has limited the practical applications of these devices. Present study is an attempt to improve the kinetic properties and stability of NR using nanoscale iron oxide (nFe₃O₄) and zinc oxide (nZnO) particles. The desired nanoparticles were synthesized, surface functionalized, characterized and affixed onto the epoxy resin to yield two nanocomposite supports (epoxy/nFe₃O₄ and epoxy/nZnO) for immobilizing NR. Epoxy/nFe₃O₄ and epoxy/nZnO support could load as much as 35.8 ± 0.01 and 33.20 ± 0.01 μg/cm² of NR with retention of about 93.72 ± 0.50 and 84.81 ± 0.80% of its initial activity respectively. Changes in surface morphology and chemical bonding structure of both the nanocomposite supports after addition of NR were confirmed by scanning electron microscopy (SEM) and fourier transform infrared spectroscopy (FTIR). Optimum working conditions of pH, temperature and substrate concentration were ascertained for free as well as immobilized NR preparations. Further, storage stability at 4 °C and thermal stability between 25–50 °C were determined for all the NR preparations. Analytical applications of immobilized NR for determination of soil and water nitrates along with reusability data has been included to make sure the usefulness of the procedure.     

Enhanced d-hydantoinase activity performance via immobilized cobalt ion affinity membrane and its kinetic study

Various immobilized metal ions affinity membranes (IMAMs) were prepared from the regenerated cellulose membrane (RC membrane) and chelated with various metal ions such as Co²⁺, Ni²⁺, Cu²⁺ and Zn²⁺. The D-hydantoin-hydrolyzing enzyme (DHTase) harboring a poly-His tagged residue was used as a model protein to be immobilized on the prepared IMAMs through the direct metal–protein interaction forces. The adsorption isotherm and the kinetic parameters V_max, K_m,app of DHTase on IMAMs were studied. The cobalt ions chelated IMAM (Co-IMAM) was found to yield the highest specific activity of DHTase. Under the immobilization condition, the cobalt ion chelated amount was 161.4 ± 4.7 μmol/disk with a DHTase activity of 4.1 ± 0.1 U/disk. As compared to the free DHTase, the immobilized DHTase membrane could achieve a broader pH tolerance and higher thermal stability. In addition, 98% of the residual activity could be retained for 7-times repeated use. Only little activity loss was observed within 36-day storage at 4 °C. This is the first report concerning about using cobalt ion as the effective chelated metal ion for simultaneous purification and immobilization operation.     

Immobilization of acidic lipase derived from Pseudomonas gessardii onto mesoporous activated carbon for the hydrolysis of olive oil

Mesoporous activated carbon (MAC) derived from rice husk is used for the immobilization of acidic lipase (ALIP) produced from Pseudomonas gessardii. The purified acidic lipase had the specific activity and molecular weight of 1473 U/mg and 94 kDa respectively. To determine the optimum conditions for the immobilization of lipase onto MAC, the experiments were carried out by varying the time (10–180 min), pH (2–8), temperature (10–50 °C) and the initial lipase activity (49 × 10³, 98 × 10³, 147 × 10³ and 196 × 10³ U/l in acetate buffer). The optimum conditions for immobilization of acidic lipase were found to be: time—120 min; pH 3.5; temperature—30 °C, which resulted in achieving a maximum immobilization of 1834 U/g. The thermal stability of the immobilized lipase was comparatively higher than that in its free form. The free and immobilized enzyme kinetic parameters (K_m and V_max) were found using Michaelis–Menten enzyme kinetics. The K_m values for free enzyme and immobilized one were 0.655 and 0.243 mM respectively. The immobilization of acidic lipase onto MAC was confirmed using Fourier Transform-Infrared Spectroscopy, X-ray diffraction analysis and scanning electron microscopy.     

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.     

Immobilized glucose oxidase on different supports for biotransformation removal of glucose from oligosaccharide mixtures

Four immobilized forms of glucose oxidase (GOD) were used for biotransformation removal of glucose from its mixture with dextran oligosaccharides. GOD was biospecifically bound to Concanavalin A-bead cellulose (GOD-ConA-TBC) and covalently to triazine-bead cellulose (GOD-TBC). Eupergit C and Eupergit CM were used for preparation of other two forms of immobilized GOD: GOD-EupC and GOD-EupCM. GOD-ConA-TBC and GOD-EupC exhibited the best operational and storage stabilities. pH and temperature optima of these two immobilized enzyme forms were broadened and shifted to higher values (pH 7 and 35 °C) in comparison with those of free GOD. The decrease of V_max values after immobilization was observed, from 256.8 ± 7.0 μmol min⁻¹ mg_GOD⁻¹ for free enzyme to 63.8 ± 4.2 μmol min⁻¹ mg_GOD⁻¹ for GOD-ConA-TBC and 45 ± 2.7 μmol min⁻¹ mg_GOD⁻¹ for GOD-EupC, respectively. Depending on the immobilization mode, the immobilized GODs were able to decrease the glucose content in solution to 3.8–15.6% of its initial amount The best glucose conversion, was achieved by an action of GOD-EupCM on a mixture of 100 g dextran with 9 g of glucose (i.e. 98.7% removal of glucose).     

Production of xylo-oligosaccharides by immobilized-stabilized derivatives of endo-xylanase from Streptomyces halstedii

An endoxylanase from Streptomyces halstedii was stabilized by multipoint covalent immobilization on glyoxyl-agarose supports. The immobilized enzyme derivatives preserved 65% of the catalytic activity corresponding to the one of soluble enzyme that had been immobilized. These immobilized derivatives were 200 times more stable 200 times more stable than the one-point covalently immobilized derivative in experiments involving thermal inactivation at 60 °C. The activity and stability of the immobilized enzyme was higher at pH 5.0 than at pH 7.0. The optimal temperature for xylan hydrolysis was 10 °C higher for the stabilized derivative than for the non-stabilized derivative. On the other hand, the highest loading capacity of activated 10% agarose gels was 75 mg of enzyme per mL of support. To prevent diffusional limitations, low loaded derivatives (containing 0.2 mg of enzyme per mL of support) were used to study the hydrolysis of xylan at high concentration (close to 1% (w/v)). 80% of the reducing sugars were released after 3 h at 55 °C. After 80% of enzymatic hydrolysis, a mixture of small xylo-oligosaccharides was obtained (from xylobiose to xylohexose) with a high percentage of xylobiose and minimal amounts of xylose. The immobilized-stabilized derivatives were used for 10 reaction cycles with no loss of catalytic activity.     

Improving the activity and stability of Yarrowia lipolytica lipase Lip2 by immobilization on polyethyleneimine-coated polyurethane foam

In this study, polyurethane foam (PUF) was used for immobilization of Yarrowia lipolytica lipase Lip2 via polyethyleneimine (PEI) coating and glutaraldehyde (GA) coupling. The activity of immobilized lipases was found to depend upon the size of the PEI polymers and the way of GA treatment, with best results obtained for covalent-bind enzyme on glutaraldehyde activated PEI-PUF (MW 70,000 Da), which was 1.7 time greater activity compared to the same enzyme immobilized without PEI and GA. Kinetic analysis shows the hydrolytic activity of both free and immobilized lipases on triolein substrate can be described by Michaelis–Menten model. The K_m for the immobilized and free lipases on PEI-coated PUF was 58.9 and 9.73 mM, respectively. The V_max values of free and immobilized enzymes on PEI-coated PUF were calculated as 102 and 48.6 U/mg enzyme, respectively. Thermal stability for the immobilization preparations was enhanced compared with that for free preparations. At 50 °C, the free enzyme lost most of its initial activity after a 30 min of heat treatment, while the immobilized enzymes showed significant resistance to thermal inactivation (retaining about 70% of its initial activity). Finally, the immobilized lipase was used for the production of lauryl laurate in hexane medium. Lipase immobilization on the PEI support exhibited a significantly improved operational stability in esterification system. After re-use in 30 successive batches, a high ester yield (88%) was maintained. These results indicate that PEI, a polymeric bed, could not only bridge support and immobilized enzymes but also create a favorable micro-environment for lipase. This study provides a simple, efficient protocol for the immobilization of Y. lipolytica lipase Lip2 using PUF as a cheap and effective material.     

A comparative performance evaluation of jute and eggshell matrices to immobilize pancreatic lipase

A pancreatic lipase was immobilized on readily available and inexpensive jute and eggshell matrices. The purity of extracted enzyme was confirmed by SDS-PAGE. The maximum protein load for eggshell was 10.23 mg/g, and for jute, it was 5.7 mg/g. The free enzyme activity retention was greater than 80% for eggshell and 43% for jute. The immobilized lipase was stable over a pH range from 7 to 8 for eggshell and 7.5 to 8.5 for jute with over a temperature range from 25 to 45 °C for eggshell and 37 to 40 °C for the jute. FTIR data indicated new bonds on the jute upon immobilization. Although no new bond was observed, immobilization data on eggshell fit well with the Langmuir adsorption isotherm model. The model constants, Γ_max and K_l, were 13.92 mg/g and 0.382 mL/mg, respectively. Mixed adsorption with both ionic and hydrophobic interactions was observed. Lipase adsorption was reduced significantly in presence of Tween 80, whereas the effect was less in case of ionic strength, pH and temperature. For both matrices, scanning electron microscopy (SEM) was used to demonstrate the changes in surface morphology after immobilization. The performance of eggshell was better than that of jute as a matrix for immobilizing pancreatic lipase.     

Polyethylene terephthalate membrane as a support for covalent immobilization of uricase and its application in serum urate determination

A method is described for covalent immobilization of uricase onto polyethylene terephthalate (PET) membrane with a conjugation yield of 4.44 μg/cm² and 66.6% retention of initial activity of free enzyme. The enzyme exhibited an increase in optimum pH from pH 7.0 to 8.5 and K_m for uric acid from 0.075 mM to 0.13 mM but slight decrease in temp. for maximum activity from 37 °C to 35 °C after immobilization. A colorimetric method for determination of serum uric acid was developed using immobilized uricase, which is based on measurement of H₂O₂ by a color reaction consisting of 3,5-dichlorobenzene sulphonic acid (DHBS), 4-aminoantipyrine and peroxidase as chromogenic system. Minimum detection limit of the method was 0.05 mM. Analytical recovery of added uric acid (5 mg/dl and 10 mg/dl) was 94.3% and 89.8%, respectively. Within and between batch coefficient of variation (CV) were <3.2% and <4.3%, respectively. A good correlation (r = 0.98) was found between uric acid values by standard enzymic colorimetric method and the present method. The immobilized uricase was reused 100 times during the span of 60 days without any considerable loss of activity, when stored in reaction buffer at 4 °C. The support chosen for the present study was biocompatible, antimicrobial, inert, impact resistant, light weight and had good shelf life.     

β-Galactosidase of Aspergillus oryzae immobilized in an ion exchange resin combining the ionic-binding and crosslinking methods: Kinetics and stability during the hydrolysis of lactose

In this work, the hydrolysis kinetics of lactose by Aspergillus oryzae β-galactosidase was studied using the ionic exchange resin Duolite A568 as a carrier. The enzyme was immobilized using a β-galactosidase concentration of 16 g/L in pH 4.5 acetate buffer and an immobilization time of 12 h at 25 ± 0.5 °C. Next, the immobilized β-galactosidase was crosslinked using glutaraldehyde concentration of 3.5 g/L for 1.5 h. The influence of lactose concentration was studied for a range of 5–140 g/L, and the Michaelis–Menten model was fitted well to the experimental results with V_m and K_m values of 0.71 U and 35.30 mM, respectively. The influence of the product galactose as an inhibitor on the hydrolysis reaction was studied. The model that was best fitted to the experimental results was the competitive inhibition by galactose with V_m, K_m and K_i values of 0.77 U, 35.30 mM and 27.44 mM, respectively. The influence of temperature on the enzymatic activity of the immobilized enzyme was studied in the range of 10–80 °C, in which the temperature of the maximum activity was 60 °C, with an activation energy of 5.32 kcal/mol of lactose, using an initial concentration of lactose of 50 g/L in a pH 4.5 sodium acetate buffer solution. The thermal stability of the immobilized biocatalyst was determined to be in the range 55–65 °C. The first-order model described well the kinetics of thermal deactivation for all the temperatures studied. The activation energy of thermal deactivation from immobilized biocatalyst was 66.48 kcal/mol with a half-life of 8.9 h at 55 °C.