Immobilization of firefly luciferase on glass rods: Properties of the immobilized enzyme

Firefly luciferase has been covalently linked with glutaraldehyde to alkylamine glass beads which had been cemented to glass rods. The immobilized enzyme has a lower pH optima than the soluble enzyme and emits light with a major peak at 615 nm, while the soluble enzyme emits light with a peak at 562 nm. The immobilized enzyme is stable and can be used for multiple assays. The peak light intensity is linear with respect to ATP concentration in the range of 1 × 10⁻⁵ to 1 × 10⁻⁸ . The luciferase rods have been used in a coupled assay to measure the rate of ATP production catalyzed by creatine phosphokinase. This immobilized luciferase should be very useful for assaying low levels of ATP in any type of sample.     

Parameter evaluation and performance studies in a fluidized-bed immobilized enzyme reactor

Dispersion and mass-transfer characteristics and fluidization parameters influencing the performance of a small pilot-plant immobilized enzyme reactor are evaluated. The suitability of a dispersed plug-flow model to predict the conversions obtained in the enzymatic reaction (starch → glucose) catalyzed by amyloglucosidase immobilized to solid and porous carriers is assessed. The performance of a fluidized-bed reactor is compared on the basis of a normalized residence time with that of a fixed bed and found to be superior.     

Stability of immobilized alcohol dehydrogenase prepared using the thermostable enzyme from yeast mitochondria

Alcohol dehydrogenase from yeast was partially purified by heat treatment (70°C, 30 min) and immobilized on porous glass, Enzacryl-TI0 and hornblende. The stabilities of these preparations were studied at 30°C and in the case of Enzacryl-TI0 and hornblende at 50°C also. These stabilities were compared with those of immobilized alcohol dehydrogenase from yeast cytosol. In all cases the mitochondrial enzyme provided the more stable bound enzyme conjugates. However, at 50°C the soluble mitochondrial enzyme was more stable than any of the immobilized derivatives: half-life values were 40, 14 and 8 h for the soluble, Enzacryl-TI0 and hornblende samples, respectively.     

Nonporous magnetic materials as enzyme supports: studies with immobilized chymotrypsin.

Chymotrypsin has been immobilized to several nonporous magnetic materials. Nickel particles were considered to be most suitable as immobilized enzyme supports. Chymotrypsin immobilized to nonporous magnetic supports was not fouled significantly by either whole milk or clarified yeast homogenate. AE-cellulose-chymotrypsin was rapidly fouled by both these materials and chymotrypsin immobilized to acrylic-based ion exchangers was slowly fouled. Immobilized enzyme activity was found to be inversely proportional to particle diameter for nonporous rock magnetic particles. Immobilization by adsorption and then glutaraldehyde crosslinking was used to produce controlled amounts of chymotrypsin on the particles. Esterolytic activity increased with enzyme loading but caseinolytic activity did not increase. Chymotrypsin is inhibited by metal ions from the magnetic supports. It is partially protected by use of a preliminary protein coating and may be reactivated by incubation with EDTA or BSA.     

Enhancement of enzyme reaction of magnetically anisotropic polyacrylamide gel rods immobilized with ferromagnetic powder and beta-D-galactosidase in an alternating magnetic field

An immobilized polyacrylamide gel containing beta-D-galactosidase and Sr-Ba-ferrite was magnetized in a static magnetic field. The gel rods (10 mm long, O 2 mm) exhibiting magnetic anisotropy could move at lower than 100 Hz but not at higher than 250 Hz in an alternating magnetic field of 200 Oe. In case of immovability of gel rods, the apparent enzymic activity increased 3 times higher under exposure of an alternating magnetic field of 500 Oe (570 Hz). It could be explained that the ferromagnetic powder inside the gel might vibrate under the influence of elasticity of gel in the alternating magnetic field of 100 or 500 Oe and 0.2-12 kHz. This might facilitate faster diffusion of the substance inside the gel and transportation of the substrate and the product through the surface of gel. Consequently, the enzyme reaction was apparently activated.     

Flow dynamics of immobilized enzyme reactors

Summary Enzymic conversion of glucose to fructose was carried out in a packed bed and in a fluidized bed reactor. The flow dynamics of these two flow systems, loaded with two different types of immobilized loaded with two different types of immobilized glucose isomerase particles, were studied. The theoretical RTD curve calculated from the axial dispersed plug flow model equation was matched to the experimental RTD curve by an optimization technique. The effect of fluid velocity on the extent of liquid dispersion was established. Theoretical predictions on the conversion of glucose to fructose were calculated using three mathematical models, namely, a plug flow model, a continuous stirred tank reactor (CSTR) model and an axial dispersed plug flow model. The experimental results showed that the axial dispersed plug flow model was superior in predicting the performance of both the packed bed and fluidized bed reactor.Abbreviations C Dimensionless concentration - D Dispersion coefficient [cm²/sec] - d _p Mean particle diameter [cm] - E Enzyme concentration [mol/gm] - F Fructose concentration [mol/cm³] - F _e Equilibrium fructose concentration [mol/cm³] - G Glucose concentration [mol/cm³] - G _e Equílibrium glucose concentration [mol/cm³] - G _o Initial glucose concentration [mol/cm³] - Reduced glucose concentration [mol/cm³] - K Equilibrium constant - K _mf Forward reaction rate constant [mol/cm³] - K _mr Reserve reaction rate constant [mol/cm³] - K _m Rate constant [mol/cm³] - L Total length of the reactor bed [cm] - l Length [cm] - Q Flow rate [cm³/s] - r Rate of reaction based on volume of substrate - u Superficial liquid velocity [cm/s] - v Interstitial liquid velocity [cm/s] - V Reactor bed volume [cm³] - V _mf Forward reaction rate constant [mol/s·g enzyme] - V _mr Reserve reaction rate constant [mol/s·g enzyme] - z Dimensionless distance along the reactor - Density [g/cm²]     

Stability of immobilized yeast alcohol dehydrogenase

The effects of substrate on stabilities of native (NA) and three kinds of immobilized yeast alcohol dehydrogenase (IMA), namely PGA (the carrier; porous glass), SEA (agarose gel) prepared covalently, and AMA (anion-exchange resin) prepared ionically, were studied. The following results were obtained. (1) The deactivations of NA and IMA free from the substrate or in the presence of ethanol obey the first-order kinetics, whereas, in the presence of butyraldehyde, their deactivation behaviors are explained on the basis of coexistence of two components of YADHs, namely the liable E₁, and the comparatively stable E₂, with different first-order deactivation constants. (2) A few attempts for stabilization of IMA were carried out from the viewpoint of the effects of crosslinkages among the subunits of YADH for PGA and the multibonding between the carrier and enzyme for SEA. The former is effective for the stabilization, whereas the later is not.     

An enzyme immobilized microassay in capillary electrophoresis for characterization and inhibition studies of alkaline phosphatases

A simple and fast dynamically coated capillary electrophoretic method was developed for the characterization and inhibition studies of alkaline phosphatases (EC 3.1.3.1). An inside capillary enzymatic reaction was performed, and hydrolysis of the substrate 4-nitrophenylphosphate to 4-nitrophenol was measured. Fused-silica capillary surface was dynamically modified with polycationic polybrene coating. By reversal of the electroosmotic flow (EOF), analysis time was reduced up to 3 min as the anionic analytes were migrated in the same direction as the EOF. Furthermore, the sensitivity of the method was increased using electroinjection through high-field amplified injection. The baseline separation of 4-nitrophenylphosphate and 4-nitrophenol was achieved by employing 50 mM sodium phosphate as the running buffer (pH 8.5), 0.0025% polybrene, and a constant voltage of −15 kV, and the products were detected at 322 nm. Under the optimized conditions, a good separation with high efficiency was achieved. The new method was applied to study enzyme kinetics and inhibitor screening. K_m and K_i values obtained with the new CE method were compared well with the standard spectrophotometric method. Dynamic coating of fused-silica capillary gave fast and reproducible separation of substrate and product. The method can be easily optimized for inhibition studies of other isozymes.     

Biosensors and enzyme immobilized electrodes.

A biosensor is a device which consists of a biological sensing element connected to a transducer. The transducer can be electronic, optical, electrical, etc. This emerging technology offers us a powerful tool which is radically altering our approach to analytical methods. It was realised that enzymes are natural sensors on account of their highly selective nature. Much of the impetus to the work has come from medical requirements. Instant analysis of clinical samples has an obvious appeal to physicians and patients alike. Of particular interest is the possibility of continuous 'in-vivo' monitoring of metabolites, drugs and proteins using miniature, portable systems. In recent years, there has been a growing demand for biosensors in the fields of veterinary science, animal husbandry, the food industry and environmental monitoring. However, the possibility of successful application rests upon future developments. Increasing attention will have to be paid to the engineering of both the basic components and the device on the whole. New biochemical reactions will either have to be discovered or engineered through genetic manipulation or chemical techniques. Optimization of response time, selectivity, stability and low costs should receive priority considerations.     

Spatiotemporal behaviors in immobilized enzyme systems

The immobilization of enzymes within an artificial membrane, with a homogeneous distribution of the active sites, allows a simple modelling in a well defined context. The systems are described by non-linear PDE'S, taking into account enzyme reaction and metabolite diffusion. These equations can exhibit several types of behaviors, qualitatively different from those observed in solution, such as hysteresis, oscillations and pattern formations. Preliminary experimental results have shown the existence of sustained oscillations and instabilities with immobilized acetylcholinesterase and phosphofructokinase.     

纳米材料固定化酶的研究进展

近年来,纳米技术为酶固定化提供了多种纳米级材料,纳米材料固定化酶不仅具有高的酶负载量,而且具有良好的酶稳定性。本文基于纳米材料固定化酶,对纳米材料的种类进行了总结,分析了纳米材料对固定化酶性能的影响,并介绍了纳米级固定化方法及纳米材料固定化酶在生物转化、生物传感器、生物燃料电池等领域的应用。     

Stabilization of enzyme immobilized in temperature-sensitive hydrogels

-Galactosidase was immobilized in a crosslinked poly(N-isopropylacrylamide-co-acrylamide) hydrogel which exhibits an LCST(lower critical solution temperature) behavior. The hydrogel collapses above the LCST, and expands below the LCST. The temperature-dependent phase transition was around 37 °C. The stability of immobilized enzyme was investigated at different temperatures which allow different degrees of collapse in the hydrogel matrix. It was hypothesized that the immobilzed enzyme is more stable in the collapsed matrix due to the physical restraint imposed on the enzyme entrapped.     

On-line synthesis utilizing immobilized enzyme reactors based upon immobilized dopamine beta-hydroxylase

Immobilized enzyme reactors (IMERs) based upon dopamine beta-hydroxylase (DBH) have been developed. Immobilized artificial membrane (IAM) and glutaraldehyde-P (Glut-P) stationary phases have been used to immobilize DBH. When DBH is immobilized on the Glut-P interphase the enzyme is outside the stationary phase whereas with the IAM interphase the enzyme is embedded within the interphase surroundings. The activity of each IMER and their ability for on-line hydroxylation has been investigated. The resulting IMERs are enzymatically active and reproducible. The IMERs can be utilized through the use of coupled chromatography to characterize the cytosolic (DBH-Glut-P-IMER) and membrane-bound (DBH-IAM-IMER) forms of the enzyme. The substrate is injected onto the individual IMERs and the reactants and products are eluted onto a phenylboronic acid column for on-line extraction. The substrates and products are then transported via a switching valve to coupled analytical columns. The results demonstrate that enzyme-substrate and enzyme-inhibitor interactions can be investigated with the on-line system. These IMERs can be utilized for the discovery and characterization of new drug candidates specific for the soluble form and membrane-bound form of DBH. The effects of flow-rate, contact time, pH and temperature have also been investigated.     

Operational effectiveness factors of immobilized enzyme systems

The steady-state and operational effectiveness factors for hydrolytic enzymes immobilized in spherical gel particles have been calculated by the collocation method for a wide range of microenvironmental conditions (given by the Thiele modulus) and macroenvironmental conditions (given by the Sherwood number and the relative substrate content). The operational effectiveness factor is a measure of the ratio of the times required to convert a defined amount of substrate with the same amount of free and immobilized enzyme, respectively. Calculations were made for reactors where the diffusion layers of the different enzyme-containing gel particles do not overlap. The theoretical values were compared with experimental values for stirred reactors with chymotrypsin and trypsin immobilized in spherical particles (Sepharose and Sephadex). Low molecular weight substrates were used. The theoretical and experimental values were found to agree within the experimental error. This demonstrates the predictive capacity of the collocation method in estimating steady-state and operational effectiveness factors for enzyme reactors. The microenvironment and macroenvironment were both found to influence the effectiveness over a wide range of substrate concentrations. However, the macroenvironmental influence is negligible when the Sherwood number of the reactor is larger than ～50. Then, the diffusion layer thickness is small compared with the dimensions of the enzyme-containing particles. The effectiveness factors calculated here can also be used to predict the performance of continuous stirred tank and plug-flow reactors.     

Plasmodium falciparum hypoxanthine guanine phosphoribosyltransferase. Stability studies on the product-activated enzyme

Hypoxanthine guanine phosphoribosyltransferases (HGPRTs) catalyze the conversion of 6-oxopurine bases to their respective nucleotides, the phosphoribosyl group being derived from phosphoribosyl pyrophosphate. Recombinant Plasmodium falciparum HGPRT, on purification, has negligible activity, and previous reports have shown that high activities can be achieved upon incubation of recombinant enzyme with the substrates hypoxanthine and phosphoribosyl pyrophosphate [Keough DT, Ng AL, Winzor DJ, Emmerson BT & de Jersey J (1999) Mol Biochem Parasitol98, 29-41; Sujay Subbayya IN & Balaram H (2000) Biochem Biophys Res Commun279, 433-437]. In this report, we show that activation is effected by the product, Inosine monophosphate (IMP), and not by the substrates. Studies carried out on Plasmodium falciparum HGPRT and on a temperature-sensitive mutant, L44F, show that the enzymes are destabilized in the presence of the substrates and the product, IMP. These stability studies suggest that the active, product-bound form of the enzyme is less stable than the ligand-free, unactivated enzyme. Equilibrium isothermal-unfolding studies indicate that the active form is destabilized by 2-3 kcal x mol(-1) compared with the unactivated state. This presents a unique example of an enzyme that attains its active conformation of lower stability by product binding. This property of ligand-mediated activation is not seen with recombinant human HGPRT, which is highly active in the unliganded state. The reversibility between highly active and weakly active states suggests a novel mechanism for the regulation of enzyme activity in P. falciparum.     

Effectiveness factor calculations for immobilized enzyme catalysts

The steady state, nonlinear diffusion equations which describe reactions in constrained enzyme solutions are of great interest in many biological and engineering applications. As in other types of nonlinear differential equations, exact analytical solutions do not exist except in some simplified cases. In this paper, a general procedure is presented for solving numerically for the substrate concentration profile and effectiveness factor utilizing the transformation method suggested by Na and Na. Design correlations for enzyme solutions constrained within spherical membranes are included. The use of a unique definition of the Thiele Modulus in these charts permits the clear illustration of the effects of substrate concentration and external mass transfer resistances on the overall effectiveness factor for the catalyst particle.     

Packed-bed immobilized enzyme reactors for complex processes

Utilization of enzymic reactors for biotechnological-biomedical applications is currently developing at a sustained pace.Our present study concentrates on development of procedures for describing the performance of devices where enzyme-catalyzed reactions between two substrates take place, and for the rational design and optimization of the reactors considered. Within this context, an analytical model was developed for immobilized enzyme packed-bed reactors; it takes into account internal diffusion limitations for the cosubstrates, and hydrodynamic backmixing effects. In order to overcome the complex mathematical problems involved, the compartmental analysis approach was employed.Using this model, performance was simulated for various configurations of the enzymic unit, i.e. from a continuously operated stirred tank reactor (CSTR) to an essentially plug flow type. In addition, an experimental method is described for quantitatively assessing the backmixing effects prevailing in the reactor.The procedures established also provide the ground for further developments, particularly for systems where, in parallel to the enzymic reaction, additional processes (e. g. complexation) take place.List of Symbols C _j,i mM Concentration of substrate j in the pores of stage - iD _j cm²/s Internal (pore) diffusion coefficient of substrate j; defined in Eq. (7) - D _e cm²/s Axial dispersion diffusion coefficient - D _j, cm²/s cm²/s Bulk diffusion coefficient for substrate j - E mM Enzyme concentration inside the catalytic pores - J _j,immol/s/cm² Net flux of substrate j taking place from the bulk of stage i into the corresponding pores; defined in Eq. (6) - K _m,1, K _m,2 mM Michaelis-Menten constants for cosubstrates 1 and 2, respectively - k s ^–1 Catalytic constant - k _s cm/s Catalytic constant - n Total number of elementary stages in the reactor - Q cm³/s Volumetric flow rate throught the reactor - r cm Radius of the pore - R _j,i mM/s Reaction rate of substrate j in stage i, in terms of volumetric units - S cm² Internal surface of a pore - S _j,0 mM Concentration of substrate j in the reactor feed - S _j,i–1, S _j,i mM Concentration of substrate j in the bulk phase leaving stages i — 1 and i, respectivley - V _i cm³ Total volume of stage i (bulk phase + pore phase + inert solid carrier) - V cm³ Total volume of the reactor - V _m ^* mmol/s/cm² Maximal reaction rate in terms of surface units; defined in Eq. (8) - V _m mM/s Maximal reaction rate in terms of volumetric units; defined in Eq. (8) - V _p cm³ Volume of one pore - y cm Axial coordinate of the pores - y ₀ cm Depth of the pores - Z cm Axial coordinate of the reactor - Z ₀ cm Length of the reactor - ₁ Dimensionless parameter; defined in Eq. (27) - ₂ Dimensionless parameter; defined in Eq. (27) - ₁ Dimensionless parameter; defined in Eq. (27) - ₂ Dimensionless parameter; defined in Eq. (27) - Ratio between the radius of the enzyme molecule and the radius of the pore (dimensionless) - V₁ Dimensionless parameter; defined in Eq. (21) - v₂ Dimensionless parameter; defined in Eq. (21) - Q Volumetric packing density of catalytic particles (dimensionless) - Ø Porosity of the catalytic particles (dimensionless) - Ø Dimensionless concentration of substrate j in pores of stage i; defined in Eq. (16) - _j,i-1,_j,i Dimensionless concentration of substrate j in the bulk phase of stage i; defined in Eq. (18) - Dimensionless position; defined in Eq. (16) - ² s² Variance; defined in Eq. (33) - Mean residence time in the reactor; defined in Eq. (33)     

Polyvinylferrocenium immobilized enzyme electrode for choline analysis

The response characteristics of a new enzyme electrode for determining choline are reported. The enzyme electrode consists of a polyvinylferrocenium perchlorate coated Pt surface onto which the enzyme, choline oxidase, is attached. Choline oxidase catalyzes the oxidation of choline to betaine, producing H₂O₂. Current due to H₂O₂ oxidation catalyzed by polyvinylferrocenium centers was measured. The effects of choline concentration, the amount of enzyme immobilized and the operating pH and temperature on the response of the enzyme electrode were studied. The effects of interferents were also investigated. The response time was found to be 60–70 s and the upper limit of the linear working portion was found to be 1.2 mM choline concentration. The minimum substrate concentration that produced detectable current was 4.0×10⁻⁶ M choline concentration. The steady-state current of this enzyme electrode was reproducible within ±4.6% of relative error. The apparent Michaelis–Menten constant (K_Mapp) and the activation energy, E_a, of this immobilized enzyme system were found to be 2.32 mM and 38.91 kJ/mol, respectively.     

Improved immobilized enzyme systems using spherical micro silica sol-gel enzyme beads

Spherical micro silica sol-gel immobilized enzyme beads were prepared in an emulsion system using cyclohexanone and Triton-X 114. The beads were used for thein situ immobilization of transaminase, trypsin, and lipase. Immobilization during the sol to gel phase transition was investigated to determine the effect of the emulsifying solvents, surfactants, and mixing process on the formation of spherical micro sol-gel enzyme beads and their catalytic activity. The different combinations of sol-gel precursors affected both activity and the stability of the enzymes, which suggests that each enzyme has a unique preference for the silica gel matrix dependent upon the characteristics of the precursors. The resulting enzyme-entrapped micronsized beads were characterized and utilized for several enzyme reaction cycles. These results indicated improved stability compared to the conventional crushed form silica sol-gel immobilized enzyme systems.