Physico-Chemical Characterization of Watermelon Urease upon Immobilization in Alginate Beads

Watermelon (Citrullus vulgaris) urease was immobilized in 3.5% alginate leading to 72% immobilization. There was no leaching of the enzyme over a period of 15 days at 4°C. It continued to hydrolyse urea at a faster rate upto 90 min of incubation. The immobilized urease exhibited a shift of apparent pH optimum by one unit towards acidic side (from pH 8.0 to 7.0). The K_m was found to be 13.3 mM; 1.17 times higher than the soluble enzyme (11.4 mM). The beads were fairly stable upto 50°C and exhibited activity even at ?10°C. The enzyme was significantly activated by ME and it exhibited two peaks of activation; one at lower concentration and another at higher concentration. Time-dependent ureolysis in presence of ME progressed at a much elevated rate. Unlike soluble enzyme, which was inhibited at 200 mM urea, the immobilized enzyme was inhibited at 600 mM of urea and above, and about 47% activity was retained at 2000 mM urea. Moreover, the inhibition caused by high urea concentration was partially abolished by ME. The significance of the observations is discussed.     

Immobilization of watermelon (<Emphasis Type="Italic">Citrullus vulgaris</Emphasis>) urease in agarose gel for urea estimation

Urease from dehusked seeds of watermelon was immobilized in 1.5% agarose gel with 53.9% entrapment. There was negligible leaching (<10% at 4°C) and the same gel membrane could repeatedly be used for seven days. The immobilization exhibited no apparent change in the optimum pH but there was a significant decrease in the optimum temperature (50°C as compared to 65°C for soluble urease). The immobilized urease revealed an apparentK _m of 9.3±0.3 mM; 1.2 times lower than the soluble enzyme (11.4±0.2 mM). Unlike soluble enzyme which was inhibited at 200 mM urea, the immobilized urease was inhibited at 600 mM of urea and above, and about 47% activity was retained at 2 M urea. The time-dependent thermal inactivation kinetics at 48 and 52°C was found to be biphasic, in which half of the initial activity was destroyed more rapidly than the remaining half. These gel membranes were also used for estimating the urea content of the blood samples from the University hospital. The results obtained matched well with those obtained by the usual method employed in the clinical pathology laboratory. The significance of these observations is discussed.     

Properties of urease immobilized on the functional organic silica surface

The paper deals with kinetics of the urea hydrolysis by microbial-origin urease dissolved and immobilized on the organic silica surface. It is shown that hydrolysis kinetics for soluble urease is described by the Michaelis-Menten equation until the concentration of urea reaches 1 M. Two fractions differing in the Michaelis constant are revealed for silochrome immobilized urease. The rate of urea hydrolysis by native and immobilized urease was studied depending on the pH value in presence of the substrate in the 1 M and 5 mM concentration. The hydrolysis rate of 1 M urea in the buffer-free solution by silochrome-immobilized urease is practically independent of pH within 4.5-6.5. Application of a 2.5 mM phosphate-citrate buffer as a solvent causes an increase in the hydrolysis rate within this pH range. For a soluble urease the 1 M urea hydrolysis rate dependence on pH is ordinary at pH 5.8-6.0. If the substrate concentration is 5 mM, the pH-dependences for the rate of the urea hydrolysis by silochrome- and aerosil-immobilized urease are close and at pH above 6.0 coincide with those for a soluble enzyme. The found differences in the properties of soluble and immobilized ureases are explained by the substrate and reaction products diffusion.     

Immobilization of soybean (Glycine max) urease on alginate and chitosan beads showing improved stability: Analytical applications

The soybean (Glycine max) urease was immobilized on alginate and chitosan beads and various parameters were optimized and compared. The best immobilization obtained were 77% and 54% for chitosan and alginate, respectively. A 2% chitosan solution (w/v) was used to form beads in 1N KOH. The beads were activated with 1% glutaraldehyde and 0.5 mg protein was immobilized per ml of chitosan gel for optimum results. The activation and coupling time were 6 h and 12 h, respectively. Further, alginate and soluble urease were mixed to form beads and final concentrations of alginate and protein in beads were 3.5% (w/v) and 0.5 mg/5 ml gel. From steady-state kinetics, the optimum temperature for urease was 65 °C (soluble), 75 °C (chitosan) and 80 °C (alginate). The activation energies were found to be 3.68 kcal mol⁻¹, 5.02 kcal mol⁻¹, 6.45 kcal mol⁻¹ for the soluble, chitosan- and alginate-immobilized ureases, respectively. With time-dependent thermal inactivation studies, the immobilized urease showed improved stability at 75 °C and the t_1/2 of decay in urease activity was 12 min, 43 min and 58 min for soluble, alginate and chitosan, respectively. The optimum pH of urease was 7, 6.2 and 7.9 for soluble, alginate and chitosan, respectively. A significant change in K_m value was noticed for alginate-immobilized urease (5.88 mM), almost twice that of soluble urease (2.70 mM), while chitosan showed little change (3.92 mM). The values of V_max for alginate-, chitosan-immobilized ureases and soluble urease were 2.82 × 10² μmol NH₃ min⁻¹ mg⁻¹ protein, 2.65 × 10² μmol NH₃ min⁻¹ mg⁻¹ protein and 2.85 × 10² μmol NH₃ min⁻¹ mg⁻¹ protein, respectively. By contrast, reusability studies showed that chitosan–urease beads can be used almost 14 times with only 20% loss in original activity while alginate–urease beads lost 45% of activity after same number of uses. Immobilized urease showed improved stability when stored at 4 °C and t_1/2 of urease was found to be 19 days, 80 days and 121 days, respectively for soluble, alginate and chitosan ureases. The immobilized urease was used to estimate the blood urea in clinical samples. The results obtained with the immobilized urease were quite similar to those obtained with the autoanalyzer^®. The immobilization studies have a potential role in haemodialysis machines.     

Urease immobilized on an aminated polysulphone membrane – inhibition by boric acid

An enzymatic membrane for application in the processes of decomposition and removal of urea from aqueous solutions was prepared: jack bean urease was immobilized on an aminated polysulphone membrane by adsorption. The inhibition of the system by boric acid was studied using procedures based on the MICHAELIS-MENTEN integrated equation (non-linear regression, and the linear transformations of WALKER and SCHMIDT, JENNINGS and NIEMANN, and BOOMAN and NIEMANN). The reaction was carried out in a 100 mM phosphate buffer of pH 7.0, containing 2 mM EDTA, obtained by neutralization of orthophosphoric acid with NaOH, at an initial urea concentration of 10 mM, and a temperature of 25 °C. The reaction was initiated by the addition of the enzyme to the urea solution, and was monitored by removing samples of the reaction mixture for NH₃ determinations by the phenol-hypochlorite method until the urea was exhausted. The results were compared with those obtained earlier under the same reaction conditions for free urease and urease covalently immobilized on chitosan. The inhibition was found to be competitive, similar to that of the free enzyme and urease immobilized on chitosan, with inhibition constants K_i equal to 0.36, 0.19 and 0.60 mM. The results show that adsorption of the enzyme on a polysulphone membrane changed the enzyme to a lesser degree than covalent immobilization of the enzyme on a chitosan membrane.     

Immobilization of acetyl-CoA:arylamine N-acetyltransferase and the preparation of an enzyme reactor for the synthesis of N-[11C]acetylserotonin

The enzyme arylamine acetyltransferase (acetyl-CoA:arylamine N-acetyltransferase, EC 2.3.1.5) from pigeon liver is immobilized onto differently derivatized controlled pore glass beads. Different silanes, spacer arms and reactive end-groups were tested, and immobilized enzyme stability tests were performed. From these experiments, the method of choice was selected: immobilization on controlled pore glass beads (24 nm pore size, 75-125 microns particle size) derivatized with gamma-aminopropyl and glutaraldehyde as the reactive end group. The kinetic properties of an enzyme reactor were investigated and optimized. The goal was to obtain a rapid high-yield conversion of 0.5-1 mumol acetyl-CoA to N-acetylserotonin, so that the reactor is useful for the 11C-labelling of N-acetylserotonin. Using an enzyme reactor (9.8 x 0.5 cm i.d.) containing 4.6 U active arylamine acetyltransferase immobilized onto 930 mg carrier, a 70% conversion of acetyl-CoA was obtained within 4 min.     

High throughput covalent immobilization process for improvement of shelf-life,operational cycles,relative activity in organic media and enzymatic kinetics of urease and its application for urea removal from water samples

High throughput covalent urease immobilization was performed through the amide bond formation between the urease and the amino-functional MNPs. The enzyme’s performances, including shelf-life, reusability, enzymatic kinetics, and the enzyme relative activity in organic media was improved. At optimal conditions, the immobilization efficiency was calculated about 95.0% with keeping 94.7% of the urease initial specific activity. The optimal pH for maximum activity of the free and immobilized urease was calculated as 7.0 at 37.0 °C and 8.0 at 60.0 °C, respectively. The kinetics studies showed the K_m of 26.0 mM and 8.0 mM and the V_max of 5.31 μmol mg⁻¹ min⁻¹ and 3.93 μmol mg⁻¹ min⁻¹ for the free and immobilized urease, respectively. The ratio K_cat/K_m as a measure of catalytic efficiency and enzyme specificity was calculated as 0.09 mg mL⁻¹ min⁻¹ and 0.22 mg mL⁻¹ min⁻¹ for the free and immobilized urease, respectively, indicating an improvement in the enzymatic kinetics. The shelf-life and operational studies of immobilized urease indicated that approximately 97.7% and 88.5% of its initial activity was retained after 40 days and 17 operational cycles, respectively. The immobilized urease was utilized to urea removal from water samples with an efficiency between 91.5–95.0%.     

Immobilization/stabilization of acid urease on Eupergit® supports

The adsorption capacity and immobilization rate of two Eupergit® supports for acid urease was studied by varying the ionic strength and enzyme preparation concentration in the immobilizing solution at pH 7. Eupergit® C250 L yielded a series of derivatives with enzyme loadings (Y_P/B) ranging from 48 to 171 mg of bovine serum albumin equivalent (BSAE) per gram of dry support (ds). Use of drastic postimmobilization conditions at pH 9 for 3–9 days yielded a slight decrease (8–14%) in the initial activity of immobilized enzymes and a limited increase in the stabilization factor (1.1–1.5), as assessed by accelerated aging tests at 65°C. Further storage tests at 4°C in the wet state showed that the activity of several derivatives either stabilized or not was practically constant for as long as 547 days. Both free enzyme and immobilized acid urease derivatives exhibited a kinetic pattern of the Michaelis–Menten type. Using the Eadie–Hofstee diagram, the specific ammonia formation rate constant for free (k_cat) or immobilized (k′_cat) enzyme resulted to be little affected by immobilization (k_cat ≈ k′_cat ≈ 18.86 ± 0.34 IU/mg BSAE), whereas the apparent Michaelis constant for immobilized enzymes exhibited a statistically significant increase at P < 0.05 from the intrinsic value (2.55 ± 0.14 mM) for free enzyme to 5.38 ± 0.87 mM as Y_P/B increased to 171 mg BSAE/g ds. By estimating the observable Thiele modulus (?_obs), the activity of the biocatalyst with the greatest enzyme loading at the lowest urea concentrations tested (0.833 mM) was reduced by a factor of about 2 due to internal diffusional limitations. By operating in the pseudofirst‐order regime with immobilized derivatives at Y_P/B about 126 mg BSAE/g ds, their activity after grinding was no more limited by intraparticle diffusion and approached the value for free enzyme. © 2012 American Institute of Chemical Engineers Biotechnol. Prog., 2012     

Preparation and characterization of urease immobilized onto porous chitosan beads for urea hydrolysis

Urease was covalently immobilized onto porous chitosan beads via primary amine groups connected to the backbone via a six-carbon linear alkyl spacer. The optimum conditions for enzyme immobilization are activating the beads with 1%(w/w) glutaraldehyde, reacting the activated beads in pH 7 buffer with the enzyme, using an enzyme to bead weight ratio of 25, and without lyophilization. Chitosan-bound urease was found to fully retain its specific activity. Properties of the immobilized urease were characterized under batch and flow conditions. Increased optimum reaction temperature, enhanced thermal stability and storage stability, and excellent reusability were found after enzyme immobilization. Continuous hydrolysis of urea solution was studied in a column packed with the enzyme-containing beads for its possible application in regenerating dialysate solution during hemodialysis.     

以芳香胺玻璃为载体的固定化的胆固醇脂酶和胆固醇氧化酶

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The effect of phosphate buffer in the range of pH 5.80–8.07 on jack bean urease activity

The effect of phosphate buffer on the activity of jack bean urease was studied in the range of pH 5.80–8.07. The inhibition constants of phosphate buffer were determined by measuring initial reaction rates at each pH for a series of buffer concentrations at a series of urea concentrations. It was shown that: (1) at pH 5.80–7.49 the buffer is a competitive inhibitor of the enzyme with K_i,buffer increasing from 0.54 mM for pH 5.80 to 362 mM for pH 7.49, (2) the values of pK_i,buffer are pH-dependent exhibiting a slope of −1 at pH 5.80–6.5 and a slope of −2 at pH 6.5–7.49, (3) from pH 7.62 as the pH is further raised the competitive inhibition of urease by the buffer was not observed, (4) the true competitive inhibitor of urease is H₂PO₄⁻ ion, and (5) pH 6.5 and 7.6 correspond to the ionization constants of the active site groups of urease responsible for the inhibitory strength of H₂PO₄⁻ ion.     

Enzymatic detection of heavy metal ions in aqueous solution from vegetable wastes by immobilizing pumpkin (<Emphasis Type="Italic">Cucumis melo</Emphasis>) urease in calcium alginate beads

Enzyme urease is extracted from the discarded seeds of pumpkin. Urease was purified to apparent homogeneity (5.2 fold) by heat treatment at 48 ± 1°C and gel filtration through Sephadex G-200. Effect of model metal ions on the activity of the homogeneous enzyme preparation (sp. activity 353 U/mg protein, A₂₈₀/A₂₆₀ = 1.12) of soluble as well as immobilized enzyme was investigated. The soluble and immobilized urease has been used for the quantitative estimation of general water pollution with heavy metal ions like Hg²⁺, Cu²⁺, Cd²⁺, and Co²⁺. The measurements of the urease residual activity have been carried out in tris-acetate buffer after pre-incubation of model metal salt. The inhibition was found to be biphasic with an initial rapid loss of activity and remainder in slow phase of 10∼15 min. The immobilization was done in 3.5% alginate beads leading to 86% of entrapment. There was no leaching of the enzyme over a period of 15 days at 4°C. The beads were fairly stable up to 50°C and exhibited activity even at −10°C. The inhibition by these ions was non-competitive and irreversible, hence could not be restored by dialysis. Based on the values of inhibition constant Ki the heavy-metal ions were found to inhibit urease in the following order Hg²⁺ > Cu²⁺ > Cd²⁺ > Co²⁺.     

Urea hydrolysis by immobilized urease in a fixed-bed reactor: analysis and kinetic parameter estimation

Urea hydrolysis by urease immobilized onto ion exchange resins in a fixed-bed reactor has been studied. A modified Michaelis-Menten rate expression is used to describe the pH-dependent, substrate- and product-inhibited kinetics. Ionic equilibria of product and buffer species are included to account for pH changes generated by reaction. An isothermal, heterogeneous plug-flow reactor model has been developed. An effectiveness factor is used to describe the reaction-diffusion process within the particle phase. The procedure for covalent immobilization of urease onto macroporous cation exchangers is described. Urea conversion data are used to estimate kinetic parameters by a simplex optimization method. The best-fitted parameters are then used to predict the outlet conversions and pH values for systems with various inlet pH values, inlet urea and ammonia concentrations, buffers, particle sizes, and spacetimes. Very good agreement is obtained between experimental data and model predictions. This immobilized urease system exhibits quite different kinetic behavior from soluble urease because the pH near the enzyme active sites is different from that of the pore fluid. This effect results in a shift of the optimal pH value of the V(max) (pH) curve from 6.6 (soluble urease) to ca. 7.6 in dialysate solution, and ca. pH 8.0 in 20mM phosphate buffer. The reactor model is especially useful for estimating intrinsic kinetic parameters of immobilized enzymes and for designing urea removal columns.     

A simple laboratory experiment for teaching enzyme immobilization with urease and its application in blood urea estimation

An experiment is described in which students carry out urease purification, immobilization and its application in blood urea estimation. Urease from pigeonpea is partially purified using acetone fractionation and then immobilized on calcium alginate in the form of beads. The immobilized enzyme has a better shelf-life at 4°C than soluble enzyme. Various aspects of enzyme immobilization are discussed. Blood urea estimation is carried out with immobilized enzyme beads and the beads can be used repeatedly for this purpose making it an economical procedure compared to commercial kits.     

Studies on Horseradish Peroxidase Immobilized onto Arylamine and Alkylamine Glass

Peroxidase from horseradish has been immobilized onto zirconia coated arylamine and alkylamine glass through the process of diazotization and glutaraldehyde coupling, respectively. Arylamine glass bound enzyme retained 77% of the initial activity with a conjugation yield of 18 mg g^-1 support, while alkylamine glass bound enzyme retained 38% of the initial activity with a conjugation yield of 16 mg g^-1 support. The immobilized enzyme showed an increase in optimum pH, temperature for maximum activity, energy of activation (Ea), and thermal stability but decrease in time for linearity and Km for H₂O₂. Vmax value of arylamlne conjugated enzyme decreased but Vmax of alkylamine conjugated enzyme was unaltered compared to free enzyme. Both arylamine and alkylamine bound enzyme showed higher stability in cold compared to that of free enzyme. The application of glass bound peroxidase in discrete analysis of serum urate is demonstrated.     

A poly(N-isopropylacrylamide-co-N-acryloxysuccinimide-co-2-hydroxyethyl methacrylate) composite hydrogel membrane for urease immobilization to enhance urea hydrolysis rate by temperature swing*

A composite membrane made of cross-linked poly(N-isopropylacrylamide-co-N-acryloxysuccinimide-co-2-hydroxyethyl methacrylate) (p(NIPAAm-NAS-HEMA)) hydrogel on polyester nonwoven support has been synthesized. The composite membrane shows temperature-responsive properties similar to conventional PNIPAAm hydrogels beads, which reversibly swells below and de-swells above the lower critical solution temperature of PNIPAAm (around 32 to 33 degrees C). Diffusion of urea through the membrane was temperature-dependent with the effective diffusion coefficient at 20 degrees C being 18 times that at 60 degrees C. Urease was immobilized directly to the membrane by forming covalent bonds between its amino groups and the succinimide ester groups of the membrane. Membrane prepared with NIPAAm to NAS molar ratio of 9, and then reacted in pH 7 buffer with 6 mg of urease gave the best immobilized enzyme, where 0.102 mg protein and 5.71 U activity per cm(2) membrane, and 55% relative specific activity could be obtained. There was negligible internal mass transfer resistance for this preparation judging from the calculated effectiveness factor. Urease shows enhanced thermal stability after immobilization with the first-order inactivation rate constant at 70 degrees C decreased to 1/8 of that of free urease. Membrane-immobilized urease could be utilized in a two-compartment membrane reactor with temperature swing to substantially enhance urea hydrolysis rate. The best operating condition of the membrane reactor was with temperature cycling between 60 to 20 degrees C and with temperature change every 10 min, where concentration of product ammonia after 3 h reaction increased 3.8-folds when compared with isothermal operation at 60 degrees C.     

Preparation,characterization and laboratory-scale application of an immobilized glucoamylase

Glucoamylase (1,4-α-d-glucan glucohydrolase, EC 3.2.1.3) has been covalently immobilized on a polyacrylamide-type support containing carboxylic groups activated by water-soluble carbodiimide. The activity was 5.5– 6.0 units g^?1solid. The optimum pH for catalytic activity was pH 3.8. The apparent optimum temperature was found at 60°C. With soluble starch as substrate the K_m value was 14 mg ml^?1. The pH for maximum stability was pH 4.0–4.5. In the presence of 8 m urea the immobilized glucoamylase retained most of its catalytic activity but it was more susceptible to guanidinium hydrochloride than the soluble enzyme. The practical applicability of immobilized glucoamylase was tested in batch process and continuous operation.     

Improving of Catalase Stability Properties by Encapsulation in Alginate/Fe3O4 Magnetic Composite Beads for Enzymatic Removal of H2O2

The aim of this study was enhancing of stability properties of catalase enzyme by encapsulation in alginate/nanomagnetic beads. Amounts of carrier (10–100 mg) and enzyme concentrations (0.25–1.5 mg/mL) were analyzed to optimize immobilization conditions. Also, the optimum temperature (25–50°C), optimum pH (3.0–8.0), kinetic parameters, thermal stability (20–70°C), pH stability (4.0–9.0) operational stability (0–390 min), and reusability were investigated for characterization of the immobilized catalase system. The optimum pH levels of both free and immobilized catalase were 7.0. At the thermal stability studies, the magnetic catalase beads protected 90% activity, while free catalase maintained only 10% activity at 70°C. The thermal profile of magnetic catalase beads was spread over a large area. Similarly, this system indicated the improving of the pH stability. The reusability, which is especially important for industrial applications, was also determined. Thus, the activity analysis was done 50 times in succession. Catalase encapsulated magnetic alginate beads protected 83% activity after 50 cycles.     

Immobilization imparts stability to watermelon urease to work in water miscible organic media

The behaviour of alginate immobilized and soluble watermelon (Citrullus vulgaris) urease in water miscible organic solvents like, acetonitrile, dimethylformamide (DMF), ethanol, methanol, and propanol is described. The organic solvents exhibited a concentration dependent inhibitory effect on both the immobilized and the soluble urease in the presence of urea. Pretreatment of soluble enzyme preparations with organic solvents in the absence of substrate for 10 min at 30°C led to rapid loss in the activity, while similar pretreatment of immobilized urease with 50% (v/v) of ethanol, propanol, and acetonitrile was ineffective. Time-dependent inactivation of immobilized urease, both in the presence and in the absence of urea, revealed stability for longer duration of time even at very high concentration of organic solvents. The soluble enzyme, on the other hand, was rapidly inactivated even at fairly lower concentrations. The results suggest that the immobilization of watermelon urease in calcium alginate make it suitable for its application in organic media. the observations are discussed.     

Immobilization of urease on vermiculite

Urease (EC 3.5.1.5) of high activity was obtained when the enzyme was immobilized on vermiculite crosslinked with 2.5% glutaraldehyde in chilled EDTA-phosphate buffer (pH 5.5). The highest activity of the immobilized enzyme was at 65°C and pH 6.5 while the optimum temperature for free urease was found to be 25°C. The thermal stability of immobilized urease was observed to be much better than that of the free urease. When stored at 4°C, urease immobilized on vermiculite retained 69 to 81% of its activity after 60 days and 61 to 75% of its original activity was retained after 4 repeated uses.