Determination of total and active immobilized enzyme distribution in porous solid supports

The total and active immobilized enzyme (IME) distributions in porous supports are studied both theoretically and experimentally. In order to determine experimentally the enzyme distribution profiles within a single particle, we construct a diffusion cell containing controlled-pore glass particles such that the cell would mimic a large pellet support. Our purpose is to study the interplay between the diffusion process within the interparticle void space and immobilization process in the controlled-pore glass particles onto the evolution of the (total and active) enzyme distributions. A mathematical model is developed to describe the interaction of various processes within the diffusion cell. The immobilized enzymes are determined for a system of trypsin and controlled-pore glass particles. The total amount of enzymes are determined by the amino acid analysis, and the active fraction is obtained by an active-site titration. The experimentally measured total IME profiles compare very well with that predicted by the model. The determined active enzyme profile is found to be nonuniform one, and it represents about 40% of the total enzyme immobilized in the support particles.     

Tyrosine hydroxylase activity of immobilized tyrosinase on enzacryl-AA and CPG-AA supports: Stabilization and properties

Frog epidermis tyrosinase has been immobilized on Enzacryl-AA (a polyacrylamide-based support) and CPG(zirclad)-Arylamine (a controlled pore glass support) in order to stabilize the tyrosine hydroxylase activity of the enzyme; in this way, the immobilized enzyme could be used to synthesize L-dopa from L-tyrosine. The activity immobilization yield Y(IME) (act) (higher than 86%), coupling efficiency (up to 90%), storage stability (no loss in 120 days), and reaction stability (t(1/2) was higher than 20 h in column reactors) were measured for tyrosinase after its immobilization. The results showed a noticeable improvement (in immobilization yield, coupling efficiency, and storage and operational stabilities) over previous reports in which tyrosinase was immobilized for L-dopa production. The activity and stability of immobilized enzyme preparations working in three different reactor types have been compared when used in equivalent conditions with respect to a new proposed parameter of the reactor (R(p)), which allows different reactor configurations to be related to the productivity of the reactor during its useful life time. The characteristic reaction inactivation which soluble tyrosinase shows after a short reaction time has been avoided by immobilization, and the stabilization was enhanced by the presence of ascorbate. However, another inactivation process appeared after a prolonged use of the immobilized enzyme. The effects of reactor type and operating conditions on immobilized enzyme activity and stability are discussed.     

Fundamental studies of glucose oxidase immobilization on controlled pore glass

Immobilization experiments have been performed with glucose oxidase as enzyme and controlled-pore glass of different pore sizes as support for chemical coupling. The experimental results have been analyzed for comparison with the theoretical model predictions. Analysis of the initial stage of the process gives the fundamental characteristic of the immobilization reaction. These investigations allow us to study the influence of the degree of diffusional restriction on the evolution of the immobilization process and spatial distribution of immobilized enzyme. Nonuniformly distributed concentrations have been achieved within the porous matrix, and suggestions have been made in designing such profiles by choosing appropriate experimental parameters.     

Decoupling of melting domains in immobilized ribonuclease A

Ribonuclease A has been immobilized on silica beads through glutaraldeyde-mediated chemical coupling in order to improve the stability of the protein against thermal denaturation. The thermodynamic and binding properties of the immobilized enzyme have been studied and compared with those of the free enzyme. The parameters describing the binding of the inhibitor 3′ -CMP (K_a and ΔH) as monitored by spectrophotometry and calorimetry were not significantly affected after immobilization. Conversely both the stability and unfolding mechanism drastically changed. Thermodynamic analysis of the DSC data suggests that uncoupling of protein domains has occurred as a consequence of the immobilization. The two state approximation of the protein unfolding process is not longer valid for the immobilized RNase. Protein stability strongly depends on the hydrophobicity properties of the support surface as well as on the presence of the inhibitor and pH. For example, after immobilization on a highly hydrophobic surface, the enzyme is partially in the unfolded state. The binding of a ligand is able to reorganize the protein structure into a native-like conformation. The refolding rates are different for the two protein domains and vary as a function of pH and presence of the inhibitor 3′-CMP. © 1994 Wiley-Liss, Inc.     

Enhancing the functional properties of thermophilic enzymes by chemical modification and immobilization

The immobilization of proteins (mostly typically enzymes) onto solid supports is mature technology and has been used successfully to enhance biocatalytic processes in a wide range of industrial applications. However, continued developments in immobilization technology have led to more sophisticated and specialized applications of the process. A combination of targeted chemistries, for both the support and the protein, sometimes in combination with additional chemical and/or genetic engineering, has led to the development of methods for the modification of protein functional properties, for enhancing protein stability and for the recovery of specific proteins from complex mixtures. In particular, the development of effective methods for immobilizing large multi-subunit proteins with multiple covalent linkages (multi-point immobilization) has been effective in stabilizing proteins where subunit dissociation is the initial step in enzyme inactivation. In some instances, multiple benefits are achievable in a single process.Here we comprehensively review the literature pertaining to immobilization and chemical modification of different enzyme classes from thermophiles, with emphasis on the chemistries involved and their implications for modification of the enzyme functional properties. We also highlight the potential for synergies in the combined use of immobilization and other chemical modifications.     

Distribution of immobilized enzymes on porous membranes

In this article, the results from a theoretical and experimental investigation of enzyme immobilization in porous membranes are reported. A theoretical model of the immobilization process, which accounts for restricted diffusion of enzyme in the pores of the membrane, has been developed. The model predicts the effect of immobilization kinetics and time of immobilization on the enzyme distribution in the pores of the membrane. The immobilization of glucose oxidase and glucose oxidase-biotin conjugate on porous alumina membranes was experimentally investigated. Enzyme uptake data was correlated to the theory to determine the rate constant of imobilization and the distribution of the enzyme in the pore. Immobilization studies were carried out for enzyme adsorption and for enzyme attachment by covalent coupling. The distribution of enzyme was experimentally studied by assembling five membranes in the diffusion cell. Following immobilization, the membranes were separated and each was assayed for activity. The amount of active enzyme present in each membrane yielded a discrete distribution that compared well with that predicted by theory. (c) 1992 John Wiley & Sons, Inc.     

Effects of mass-transfer resistance on apparent stability and performance of fixed-bed immobilized enzyme reactors: theory and experiments with immobilized invertase

Taking the hydrolysis of sucrose by invertase immobilized on anion-exchange resin as an example, the effects of mass-transfer resistance on the apparent stability of immobilized enzyme (IME) and the optimal policy for an IME reaction in a fixed-bed reactor have been studied theoretically and experimentally. The following results were obtained: (1) The effect of mass-transfer resistance on the effective deactivation rate of IME is summarized in two parameters concerning the intraparticle diffusion alpha(p) and the interparticle alpha(f). (2) At a constant processed amount of raw materials, there exists an optimal flow rate of reaction fluid to enhance the reactor performance while the mass-transfer resistance shifts the optimal point. (3) The intrinsic deactivation rate of IME has been estimated from the relationship between the fractional conversion at the reactor outlet and the operation time.     

Laccase immobilization on enzymatically functionalized polyamide 6,6 fibres

Polyamide matrices, such as membranes, gels and non-wovens, have been applied as supports for enzyme immobilization, although in literature the enzyme immobilization on woven nylon matrices is rarely reported. In this work, a protocol for a Trametes hirsuta laccase immobilization using woven polyamide 6,6 (nylon) was developed. A 2⁴ full factorial design was used to study the influence of pH, spacer (1,6-hexanediamine), enzyme and crosslinker concentration on the efficiency of immobilization. The factors enzyme dosage and spacer seem to have played a critical role in the immobilization of laccase onto nylon support. Under optimized working conditions (29 U mL⁻¹ of laccase, 10% of glutaraldehyde, pH = 5.5, with the presence of the spacer), the half-life time attained was about 78 h (18% higher than that of free enzyme), the protein retention was 30% and the immobilization yield was 2%. The immobilized laccase has potential for application in the continuous decolourization of textile effluents, where it can be applied into a membrane reactor.     

Immobilization–stabilization of the lipase from Thermomyces lanuginosus: Critical role of chemical amination

This paper describes the immobilization and stabilization of the lipase from Thermomyces lanuginosus (TLL) on glyoxyl agarose. Enzymes attach to this support only by the reaction between several aldehyde groups of the support and several Lys residues on the external surface of the enzyme molecules at pH 10. However, this standard immobilization procedure is unsuitable for TLL lipase due to the low stability of TLL at pH 10 and its low content on Lys groups that makes that the immobilization process was quite slow. The chemical amination of TLL, after reversible immobilization on hydrophobic supports, has been shown to be a simple and efficient way to improve the multipoint covalent attachment of this enzyme. The modification enriches the enzyme surface in primary amino groups with low pKb, thus allowing the immobilization of the enzyme at lower pH values. The aminated enzyme was rapidly immobilized at pH 9 and 10, with activities recovery of approximately 70%. The immobilization of the chemically modified enzyme improved its stability by 5-fold when compared to the non-modified enzyme during thermal inactivation and by hundreds of times when the enzyme was inactivated in the presence of organic solvents, being both glyoxyl preparations more stable than the enzyme immobilized on bromocyanogen.     

Theoretical and experimental analysis of a soluble enzyme membrane reactor.

Recently enzyme immobilization techniques have been proposed that are mainly founded on the formation of an enzyme-gel layer onto the active surface of an ultrafiltration membrane within an unstirred ultrafiltration cell. If the membrane molecular-weight cutoff is less than the enzyme molecular weight and hence such as to completely prevent enzyme permeation (once the enzyme solution has been charged into the test cell and pressure applied to the system), a time progressive increase in enzyme concentration takes place at the upstream membrane surface that can eventually lead to gelation and hence to enzyme immobilization. However, depending on the total enzyme amount fed, the maximum enzyme concentration achieved in the unsteady state could be less than the gelation level. In this situation, no immobilization occurs and the enzyme still remains in the soluble form although it is practically confined within a limited region immediately upstream the membrane and at fairly high concentrations. In this paper, the experimental conditions that allow gelling to occur are discussed together with a theoretical analysis of the soluble enzyme membrane reactor which is obtained when no gelling takes place. Such a system could be usefully employed in performing kinetic analyses at high enzyme concentration levels that are still in the soluble form.     

Enzyme loading in a solid support with nonuniform pore size distribution

The concept of pore size distribution is incorporated into the Clark model of enzyme immobilization in the present study. This refined model predicted that in the case of small harmonic pore radius with the same surface area and porosity of the support, more enzyme could be loaded in a support with nonuniform pores than that with uniform pores. In comparing the enzyme loading efficiency of the support with two different pore size distributions, the one with Gaussian distribution had the greater amount of enzyme immobilized than the other one with Rajagopalan's distribution. Furthermore, more enzyme could be loaded in a support with wider Gaussian pore size distribution than that with narrower distribution. The immobilized enzyme profile in the solid support with pore size distribution displayed a stepwise pattern which differed appreciably from the sigmoidal profile predicted for the support with uniform pore size. This stepwise enzyme distribution profile became sigmoidal with decreasing h(T) or increasing k. The new model could be used for designing protocols for an enzyme immobilization process.     

A novel heterofunctional epoxy-amino sepabeads for a new enzyme immobilization protocol: immobilization-stabilization of beta-galactosidase from Aspergillus oryzae

The properties of a new and commercially available amino-epoxy support (amino-epoxy-Sepabeads) have been compared to conventional epoxy supports to immobilize enzymes, using the beta-galactosidase from Aspergillus oryzae as a model enzyme. The new support has a layer of epoxy groups over a layer of ethylenediamine that is covalently bound to the support. This support has both a great anionic exchanger strength and a high density of epoxy groups. Epoxy supports require the physical adsorption of the proteins onto the support before the covalent binding of the enzyme to the epoxy groups. Using conventional supports the immobilization rate is slow, because the adsorption is of hydrophobic nature, and immobilization must be performed using high ionic strength (over 0.5 M sodium phosphate) and a support with a fairly hydrophobic nature. Using the new support, immobilization may be performed at moderately low ionic strength, it occurs very rapidly, and it is not necessary to use a hydrophobic support. Therefore, this support should be specially recommended for immobilization of enzymes that cannot be submitted to high ionic strength. Also, both supports may be expected to yield different orientations of the proteins on the support, and that may result in some advantages in specific cases. For example, the model enzyme became almost fully inactivated when using the conventional support, while it exhibited an almost intact activity after immobilization on the new support. Furthermore, enzyme stability was significantly improved by the immobilization on this support (by more than a 12-fold factor), suggesting the promotion of some multipoint covalent attachment between the enzyme and the support (in fact the enzyme adsorbed on an equivalent cationic support without epoxy groups was even slightly less stable than the soluble enzyme).     

Mechanistic investigation of ultrasonic enhancement of glycerol bioconversion by immobilized Clostridium pasteurianum on silica support

Glycerol, the principal byproduct of biodiesel production, can be a valuable carbon source for bioconversion into diverse class of compounds. This article attempts to investigate the mechanistic aspects of ultrasound mediated bioconversion of glycerol to ethanol and 1,3‐propanediol (1,3‐PDO) by immobilized Clostridium pasteurianum cells on silica support. Our approach is of coupling experimental results with simulations of cavitation bubble dynamics and enzyme kinetics. In addition, the statistical analysis (ANOVA) of experimental results was also done. The glycerol uptake by cells was not affected by either immobilization or with ultrasonication. Nonetheless, both immobilization and ultrasonication were found to enhance glycerol consumption. The enhancement effect of ultrasound on glycerol consumption was most marked (175%) at the highest glycerol concentration of 25 g/L (271.7 mM). The highest glycerol consumption (32.4 mM) was seen for 10 g/L (108.7 mM) initial glycerol concentration. The immobilization of cells shifted the metabolic pathway almost completely towards 1,3‐PDO. No formation of ethanol was seen with mechanical shaking, while traces of ethanol were detected with ultrasonication. On the basis of analysis of enzyme kinetics parameters, we attribute these results to increased substrate‐enzyme affinity and decreased substrate inhibition for 1,3‐PDO dehydrogenase in presence of ultrasound that resulted in preferential conversion of glycerol into 1,3‐PDO. Biotechnol. Bioeng. 2013; 110: 1637–1645. © 2013 Wiley Periodicals, Inc.     

Reversible denaturation of carbonic anhydrase provides a method for its adsorptive immobilization

Palmityl-substituted sepharose 4B has been used for adsorptive immobilization of heat-denatured carbonic anhydrase. The native form of this enzyme does not show any affinity for binding to this hydrophobic support. However, through the process of denaturation-renaturation performed by heating and subsequent cooling of an enzyme solution in the presence of the matrix, it was possible to obtain a catalytically active immobilized preparation, which was used successfully in continuous catalytic transformations. It is suggested that this simple procedure may provide a convenient method of immobilization for proteins, which are not normally adsorbed on hydrophobic supports.     

碳纳米管固定化纤维素酶的最佳工艺研究

纤维素酶在环保、医药、食品等领域都具有广泛的应用前景,但由于纤维素酶的生产成本较高,生物活性较低,使得纤维素酶的应用受到了限制。为了寻找一种固定化纤维素酶的方法,使酶可以重复多次使用,首次以多壁碳纳米管为载体固定化纤维素酶,研究功能化的多壁碳纳米管固定化纤维素酶的固定化条件,采用正交试验对酶固定化中的主要条件进行优化,并通过傅里叶变换红外光谱仪对多壁碳纳米管（multiwalled carbon nanotube,MWCNTs）、纤维素酶及固定化纤维素酶的结构进行表征。结果表明,固定化纤维素酶的最佳工艺条件为：酶浓度5 mg·mL-1,温度40 ℃,pH 5.0,固定化时间3 h;通过傅里叶变换红外光谱证实纤维素酶成功固定到多壁碳纳米管上。     

Use of chemically modified PMMA microspheres for enzyme immobilization

Modified poly(methyl methacrylate) (PMMA) microspheres, about 7microm in diameter, carrying aldehyde groups on their surfaces were synthesized and used as the support for enzyme immobilization. The immobilizing behavior as well as the properties of immobilized enzyme was studied. The amount of bound enzyme can be extended to 76.8mg g(-1) support, which is relatively much higher than other supports. The kinetic investigation derived from three typical models shows that the practical process is more complicated than the ideal condition, with one or more interactions being involved in the immobilization process. The K(m) value is actually larger and V(max) is smaller in the immobilized form than those in the free form. The increased resistance of the immobilized enzyme against the changes of temperature indicates that immobilizing enzyme onto the modified microspheres is useful for enzyme immobilization.     

Polymer materials for enzyme immobilization and their application in bioreactors

Enzymatic catalysis has been pursued extensively in a wide range of important chemical processes for their unparalleled selectivity and mild reaction conditions. However, enzymes are usually costly and easy to inactivate in their free forms. Immobilization is the key to optimizing the in-service performance of an enzyme in industrial processes, particularly in the field of non-aqueous phase catalysis. Since the immobilization process for enzymes will inevitably result in some loss of activity, improving the activity retention of the immobilized enzyme is critical. To some extent, the performance of an immobilized enzyme is mainly governed by the supports used for immobilization, thus it is important to fully understand the properties of supporting materials and immobilization processes. In recent years, there has been growing concern in using polymeric materials as supports for their good mechanical and easily adjustable properties. Furthermore, a great many work has been done in order to improve the activity retention and stabilities of immobilized enzymes. Some introduce a spacer arm onto the support surface to improve the enzyme mobility. The support surface is also modified towards biocompatibility to reduce non-biospecific interactions between the enzyme and support. Besides, natural materials can be used directly as supporting materials owning to their inert and biocompatible properties. This review is focused on recent advances in using polymeric materials as hosts for lipase immobilization by two different methods, surface attachment and encapsulation. Polymeric materials of different forms, such as particles, membranes and nanofibers, are discussed in detail. The prospective applications of immobilized enzymes, especially the enzyme-immobilized membrane bioreactors (EMBR) are also discussed.     

Enzyme immobilization in a biomimetic silica support

Robust immobilization techniques that preserve the activity of biomolecules have many potential applications. Silicates, primarily in the form of sol-gel composites or functionalized mesoporous silica, have been used to encapsulate a wide variety of biomolecules but the harsh conditions required for chemical synthesis limit their applicability. Silaffin polypeptides from diatoms catalyze the formation of silica in vitro at neutral pH and ambient temperature and pressure. Here we show that butyrylcholinesterase entrapped during the precipitation of silica nanospheres retained all of its activity. Ninety percent of the soluble enzyme was immobilized, and the immobilized enzyme was substantially more stable than the free enzyme. The mechanical properties of silica nanospheres facilitated application in a flow-through reactor. The use of biosilica for enzyme immobilization combines the excellent support properties of a silica matrix with a benign immobilization method that retains enzyme activity.     

Laccase immobilization on enzymatically functionalized polyamide 6,6 fibres

Polyamide matrices, such as membranes, gels and non-wovens, have been applied as supports for enzyme immobilization, although in literature the enzyme immobilization on woven nylon matrices is rarely reported. In this work, a protocol for a Trametes hirsuta laccase immobilization using woven polyamide 6,6 (nylon) was developed. A 2⁴ full factorial design was used to study the influence of pH, spacer (1,6-hexanediamine), enzyme and crosslinker concentration on the efficiency of immobilization. The factors enzyme dosage and spacer seem to have played a critical role in the immobilization of laccase onto nylon support. Under optimized working conditions (29 U mL⁻¹ of laccase, 10% of glutaraldehyde, pH = 5.5, with the presence of the spacer), the half-life time attained was about 78 h (18% higher than that of free enzyme), the protein retention was 30% and the immobilization yield was 2%. The immobilized laccase has potential for application in the continuous decolourization of textile effluents, where it can be applied into a membrane reactor.     

Preparation and properties of immobilized amyloglucosidase on nonporous PS/PNaSS microspheres

Nonporous polystyrene/poly(sodium styrene sulfonate) (PS/PNaSS) microspheres were used for immobilization of amyloglucosidase and the properties of immobilized enzyme was studied and compared with those of free enzyme. Sulfonated groups on the PS/PNaSS microspheres present a very simple, mild, and time-saving process for enzyme immobilization. Nonporous microspheres provide their surface for immobilization of enzyme and prevent the diffusion limitation problem in the pore. Despite the high concentration of bound enzyme the influence of immobilization on kinematic parameters, K(m) and V(max), is relatively low compare to other porous supports. Simple and time-saving immobilization procedure as well as the effects of pH and temperature on immobilized enzyme also showed that the PS/PNaSS microspheres could be good support.