Inhibition of chitosan-immobilized urease by slow-binding inhibitors: Ni, F and acetohydroxamic acid

The inhibitions by Ni²⁺ and F⁻ ions and by acetohydroxamic acid of jack bean urease covalently immobilized on chitosan membrane was studied (pH 7.0, 25°C) and compared with those of the native enzyme. The reaction progress curves of the immobilized urease-catalyzed hydrolysis of urea were recorded in the absence and presence of the inhibitors. They revealed that the inhibitions are of the competitive slow-binding type similar to those of native urease. The immobilization weakened the inhibitory effect of the inhibitors on urease as measured by the inhibition constants K_i^*. The increase in their values: 17.9-fold for Ni²⁺, 26.5-fold for F⁻ and 1.7-fold for acetohydroxamic acid, was accounted for by environmental effects generated by heterogeneity of the urease–chitosan system: (1) mass transfer limitations imposed on substrate and reaction product in the external solution, and (2) the increase in local pH on the membrane produced by both the enzymatic reaction and the electric charge of the support. By relating the K_M/K_i^* ratio to the electrostatic potential of chitosan it was found that while the reduced Ni²⁺ inhibition is mainly brought about by the potential, inhibition by acetohydroxamic acid is independent of the potential, and the acid inhibits urease in its non-ionic form. The reduction in F⁻ inhibition was ascribed to the increased pH in the local environment of the immobilized enzyme.     

Immobilization of urease on nanostructured polymer membrane and preparation of urea amperometric biosensor

A new matrix for enzyme immobilization of urease was obtained by incorporating rhodium nanoparticles (5% on activated charcoal) and chemical bonding of chitosan with different concentration (0.15%; 0.3%; 0.5%; 1.0%; 1.5%) in previously chemically modified AN copolymer membrane. The basic characteristics of the chitosan modified membranes were investigated. The SEM analyses were shown essential morphology change in the different modified membranes. Both the amount of bound protein and relative activity of immobilized enzyme were measured. A higher activity (about 77.44%) was measured for urease bound to AN copolymer membrane coated with 1.0% chitosan and containing rhodium nanoparticles. The basic characteristics (pH(opt), T(opt), thermal, storage and operation stability) of immobilized enzyme on this optimized modified membrane were also determined. The prepared enzyme membrane was used for the construction of amperometric biosensor for urea detection. Its basic amperometric characteristics were investigated. A calibration plot was obtained for urea concentration ranging from 1.6 to 23 mM. A linear interval was detected along the calibration curve from 1.6 to 8.2mM. The sensitivity of the constructed biosensor was calculated to be 3.1927 μAmM(-1)cm(-2). The correlation coefficient for this concentration range was 0.998. The detection limit with regard to urea was calculated to be 0.5mM at a signal-to-noise ratio of 3. The biosensor was employed for 10 days while the maximum response to urea retained 86.8%.     

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.     

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%.     

Urease Immobilization on Arylamine Glass Beads and its Characterization

Jack bean urease has been immobilized on arylamine glass beads (200–400 mesh size, 75–100 Å pore size) and its properties compared with soluble enzyme. The binding of urease was 13.71 mg per gram beads. The K_m for soluble and immobilized urease for urea was 4.20 mM and 8.81 mM, respectively. V_max values of urease decreased from 200 to 43.48 μmol of ammonia formed per min per mg protein at 37°C on immobilization. Both pH and buffer ions influenced the activities of soluble as well as immobilized urease. Soluble urease exhibited pH optima at 5.5 and 8.0. However, immobilized urease showed one additional pH optimum at 6.5. In comparison to phosphate buffer, citrate buffer was inhibitory to urease activity. Immobilization of urease on arylamine glass beads resulted in improved thermal, storage and operational stability. Because of inertness of support and stability of immobilized urease, the preparation can find applications in ‘artificial kidney’ and urea estimation in biological fluids viz., blood, milk etc.     

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.     

Amperometric electrode for determination of urea using electrodeposited rhodium and immobilized urease

An amperometric biosensor was developed for determination of urea using electrodeposited rhodium on a polymer membrane and immobilized urease. The urease catalyzes the hydrolysis of urea to NH₄⁺ and HCO₃⁻ ions and the liberated ammonia is catalytically and electrochemically oxidized by rhodium present in the rhodinized membrane on the Pt working electrode. Three types of rhodinized polymer membranes were prepared by varying the number of electrodeposition cycles: membrane 1 with 10 deposition cycles, membrane 2 with 40 cycles and membrane 3 with 60 cycles. The morphologies of the rhodinized membranes were investigated by scanning electron microscopy and the results showed that the deposition of rhodium was like flowers with cornices-like centers. The influence of the amount of electrodeposited rhodium over the electrode sensitivity to different concentrations of ammonia was examined initially based on the cyclic voltammetric curves using the three rhodium modified electrodes. The obtained results convincingly show that electrode with rhodinized membrane 1, which contain the lowest amount of electrodeposited rhodium is the most active and sensitive regarding ammonia. It was found that the anodic oxidation peak of ammonia to nitrogen occurs at 0.60 V. In order to study the performance of urease amperometric sensor for the determination of urea, experiments at constant potential (0.60 V) were performed. The current–time experiments were carried out with urease rhodinized membrane 1 (10 cycles). The amperometric response increased linearly up to 1.75 mM urea. The detection limit was 0.05 mM. The urea biosensor exhibited a high sensitivity of 1.85 μA mM⁻¹ cm⁻² with a response time 15 s. The Michaelis–Menten constant K_m for the urea biosensor was calculated to be 6.5 mM, indicating that the immobilized enzyme featured a high affinity to urea. The urea sensor showed a good reproducibility and stability. Both components rhodium and urease contribute to the decreasing of the production cost of biosensor by avoiding the use of a second enzyme.     

Immobilization of urease on vapour phase stain etched porous silicon

Porous silicon layers fabricated by the reaction-induced vapor phase stain etch method were coated with 5% polyethylenimine. Urease from Canavalia brasiliensis beans was immobilized on this support through covalent linking with 2.5% glutaraldehyde. The pH and temperature profile of the immobilized and free urease exhibited higher activity at pH 6.5 and 37 °C. After being stored for 30 days at 4 °C, the immobilized enzyme had 75% of the initial activity. The maximum apparent Michaelis constant for free urease (K_m) was 94.33 mM whereas for immobilized urease was 53.04 mM. The maximum reaction velocity (V_max) for free urease was 3.51 mmol/min and for immobilized urease was 1.57 mmol/min.     

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 kappa-carrageenan immobilized urease

Urease was encapsulated within kappa-carrageenan beads. Various parameters, such as amount of kappa-carrageenan and enzyme activity, were optimized for the immobilization of urease. Immobilized urease was thoroughly characterized for pH, temperature, and storage stabilities and these properties were compared with the free enzyme. The free urease activity quickly decreased and the half time of the activity decay was about 3 days at 4 degrees C. The immobilized urease remained very active over a long period of time and this enzyme lost about 70.43% of its orginal activity over the period of 26 days for storage at 4 degrees C. The Michaelis constant (Km) and maximum reaction velocity (Vmax) were calculated from Lineweaver-Burk plots for both free and immobilized enzyme systems. Vmax = 227.3 U/mg protein, Km = 65.6 mM for free urease and Vmax = 153.9 U/mg protein, Km = 96.42 mM for immobilized urease showed a moderate decrease of enzyme specific activity and change of substrate affinity.     

Microfluidic conductimetric bioreactor

A microfluidic conductimetric bioreactor has been developed. Enzyme was immobilized in the microfluidic channel on poly-dimethylsiloxane (PDMS) surface via covalent binding method. The detection unit consisted of two gold electrodes and a laboratory-built conductimetric transducer to monitor the increase in the conductivity of the solution due to the change of the charges generated by the enzyme-substrate catalytic reaction. Urea–urease was used as a representative analyte-enzyme system. Under optimum conditions urea could be determined with a detection limit of 0.09 mM and linearity in the range of 0.1–10 mM (r = 0.9944). The immobilized urease on the microchannel chip provided good stability (>30 days of operation time) and good repeatability with an R.S.D. lower than 2.3%. Good agreement was obtained when urea concentrations of human serum samples determined by the microfluidic flow injection conductimetric bioreactor system were compared to those obtained using the Berthelot reaction (P < 0.05). After prolong use the immobilized enzyme could be removed from the PDMS microchannel chip enabling new active enzyme to be immobilized and the chip to be reused.     

Comparative study of controlled pore glass, silica gel and poraver for the immobilization of urease to determine urea in a flow injection conductimetric biosensor system

This study compared the responses of three enzyme reactors containing urease immobilized on three types of solid support, controlled pore glass (CPG), silica gel and Poraver. The evaluation of each enzyme reactor column was done in a flow injection conductimetric system. When urea in the sample solution passed though the enzyme reactor, urease catalysed the hydrolysis of urea into charged products. A lab-built conductivity meter was used to measure the increase in conductivity of the solution. The responses of the enzyme reactor column with urease immobilized on CPG and silica gel were similar and were much higher than that of Poraver. Both CPG and silica gel reactor columns gave the same limit of detection, 0.5 mM, and the response was still linear up to 150mM. The analysis time was 4-5 min per sample. The enzyme reactor column with urease immobilized on CPG gave a slightly better sensitivity, 4% higher than the reactor with silica gel. The life time of the immobilized urease on CPG and silica gel were more than 310h operation time (used intermittently over 7 months). Good agreement was obtained when urea concentrations of human serum samples determined by the flow injection conductimetric biosensor system was compared to the conventional methods (Fearon and Berthelot reactions). These were statistically shown using the regression line and Wilcoxon signed rank tests. The results showed that the reactor with urease immobilized on silica gel had the same efficiency as the reactor with urease immobilized on CPG.     

Preparation and Some Properties of Chitosan Bound Enzymes

An immobilization method using chitosan prepared from chitin as an insoluble carrier was investigated. Glucose isomerase, urease, glucamylase, trypsin and glucose oxidase were attached to chitosan by the aid of water soluble carbodiimide. Their activity yields were as follows; glucose isomerase 32%, urease 44%, glucamylase 8%, trypsin 10%, glucose oxidase 37%.

Immobilized glucose isomerase showed no significant changes in optimal temperature and heat stability. But pH optimum of reaction and pH stability range were somewhat lowered. The inhibitory effects of bivalent metal ions were considerably reduced by immobilization and similar tendency was observed for buffer reagents such as Tris or veronal. Immobilized glucose isomerase was inhibited by 8 m urea or 6 m guanidine hydrochloride in nearly the same way as free enzyme. With SDS, cysteine or mercaptoethanol free glucose isomerase was scarcely affected by these reagents, while immobilized enzyme considerably suffered to a loss of its activity.     

Reversible immobilization of catalase on fibrous polymer grafted and metal chelated chitosan membrane

Poly(itaconic acid) grafted and/or Fe(III) ions incorporated chitosan membranes were used for reversible immobilization of catalase (from bovine liver) via adsorption. The influences of pH and initial catalase concentration on the immobilization capacities of the CH-g-poly(IA) and CH-g-poly(IA)-Fe(III) membranes have been investigated in a batch system. Maximum catalase adsorption onto CH-g-poly(IA) and CH-g-poly(IA)-Fe(III) membrane were found to be 6.3 and 37.8 mg/g polymer at pH 5.0 and 6.5, respectively. The CH-g-poly(IA)-Fe(III) membrane with high catalase adsorption capacity was used in the rest of the study. The K_m value for immobilized catalase on CH-g-poly(IA)-Fe(III) (25.8 mM) was higher about 1.6-fold than that of free enzyme (13.5 mM). Optimum operational temperature was observed at 40 °C, a 5 °C higher than that of the free enzyme and was significantly broader. The optimum operational pH was same for both free and immobilized catalase (pH 7.0). Thermal stability was found to increase with immobilization. Free catalase lost all its activity within 20 days whereas immobilized catalase lost 23% of its activity during the same incubation period. It was observed that the same support enzyme can be repeatedly used for immobilization of catalase after regeneration without significant loss in adsorption capacity or enzyme activity. In addition, the CH-g-poly(IA)-Fe(III) membrane prepared in this work showed promising potential for various biotechnological applications.     

Immobilization of urease by using chitosan–alginate and poly(acrylamide-co-acrylic acid)/κ-carrageenan supports

Jack bean urease (urea aminohydrolase, E.C. 3.5.1.5) was entrapped into chitosan–alginate polyelectrolyte complexes (C-A PEC) and poly(acrylamide-co-acrylic acid)/κ-carrageenan (P(AAm-co-AA)/carrageenan) hydrogels for the potential use in immobilization of urease, not previously reported. The effects of pH, temperature, storage stability, reuse number, and thermal stability on the free and immobilized urease were examined. For the free and immobilized urease into C-A PEC and P(AAm-co-AA)/carrageenan, the optimum pH was found to be 7.5 and 8, respectively. The optimum temperature of the free and immobilized enzymes was also observed to be 55 and 60 °C, respectively. Michaelis–Menten constant (K _m) values for both immobilized urease were also observed smaller than free enzyme. The storage stability values of immobilized enzyme systems were observed as 48 and 70%, respectively, after 70 days. In addition to this, it was observed that, after 20th use in 5 days, the retained activities for immobilized enzyme into C-A PEC and P(AAm-co-AA)/carrageenan matrixes were found as 55 and 89%, respectively. Thermal stability of the free urease was also increased by a result of immobilization.     

Optimization of urease immobilization onto non-porous HEMA incorporated poly(EGDMA) microbeads and estimation of kinetic parameters.

Jack bean urease (urea aminohydrolase, EC 3.5.1.5) was immobilized onto modified non-porous poly(ethylene glycol dimethacrylate/2-hydroxy ethylene methacrylate), (poly(EGDMA/HEMA)), microbeads prepared by suspension copolymerization for the potential use in hemoperfusion columns, not previously reported. The conditions of immobilization; enzyme concentration, medium pH, substrate and ethylene diamine tetra acetic acid (EDTA) presence in the immobilization medium in different concentrations, enzyme loading ratio, processing time and immobilization temperature were investigated for highest apparent activity. Immobilized enzyme retained 73% of its original activity for 75 days of repeated use with a deactivation constant kd = 3.72 x 10(-3) day(-1). A canned non-linear regression program was used to estimate the intrinsic kinetic parameters of immobilized enzyme with a low value of observable Thiele modulus (phi < 0.3) and these parameters were compared with those of free urease. The best-fit kinetic parameters of a Michaelis-Menten model were estimated as Vm = 3.318 x 10(-4) micromol/s mg bound enzyme protein, Km = 15.94 mM for immobilized, and Vm = 1.074 micromol NH3/s mg enzyme protein, Km = 14.49 mM for free urease. The drastic decrease in Vm value was attributed to steric effects, conformational changes in enzyme structure or denaturation of the enzyme during immobilization. Nevertheless, the change in Km value was insignificant for the unchanged affinity of the substrate with immobilization. For higher immobilized urease activity, smaller particle size and concentrated urease with higher specific activity could be used in the immobilization process.     

Urease immobilization on biotinylated polypyrrole coated ChemFEC devices for urea biosensor development

In this report, we describe a novel strategy for the design of a clinical urea biosensor using a process based on assembled multilayer systems. Biotinylated enzyme (urease–subiotin) was immobilized on the biotinylated polypyrrole coated Chemical field effect capacitance (ChemFEC) devices using the high avidin–biotin affinity. The immobilized enzyme activity was checked by its catalytic conversion of urea into carbon dioxide and ammonia. Electrochemical response of the bridge system constructed on Si/SiO₂/Si₃N₄ electrodes to urea addition was evaluated using the capacity–potential measurements. In addition, contact-angle measurements were carried out to control the change of surface energy and their components before and after each layer formation. The developed urea biosensor demonstrates high performances: a good sensitivity of 50 mV/pUrea in the linear urea concentration range from 10⁻⁴ to 10⁻¹ M and an excellent operational stability after three weeks of continuous use. The immobilized urease was characterised through its apparent Michaelis–Menten constant (5 mM) and the activation energy of the enzymatic reaction (20 kJ mol⁻¹). It was also shown that capacitive measurements can be used to quantify the interaction between molecular systems, based on avidin and biotin molecules.     

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.     

Improved octyl glucoside synthesis using immobilized β-glucosidase on PA-M with reduced glucose surplus inhibition

A β-glucosidase extracted from bitter almond (Prunus dulcis var. amara) was immobilized on polyamine microspheres (PA-M) for catalytic octyl glucoside (OG) synthesis from glucose and octanol through reversed hydrolysis. The immobilization increased the activity of enzyme at pH 6.0–7.0, and the optimal reaction temperature for immobilized enzyme was identical to the free enzyme. The thermal stability and solvent tolerance of enzyme were increased by its immobilization. In the co-solvent system using 10% t-butyl alcohol and 10% (v/v) water, the yield of OG was increased by 1.7-fold compared to the yield from the system without co-solvent. Based on dynamic and Dixon plot analyses, the initial reaction velocity (V₀) increased approximately three-fold on immobilization and the OG synthesis was inhibited by surplus glucose. The inhibition dissociation constants for free and immobilized enzyme were 219?mM and 116?mM, respectively. A fed-batch mode was applied in the OG synthesis to minimize substrate inhibition. After 336?h of reaction, the OG yield and the conversion rate of glucose reached 134?mM and 59.6%, respectively. Compared to the batch operation, the fed-bath operation increased the OG yield and the conversion rate of glucose by 340% and 381%, respectively.