Pilot plant production of glucose with glucoamylase immobilized to porous silica.

Glucoamylase was immobilized to porous silica and its kinetics and stability were observed with acid- and alpha-amylase-hydrolyzed dextrin as feed. The enzyme was found to be extremely stable in both laboratory and pilot plant operations. When the feed had been previously only lightly hydrolyzed, pore diffusion limitation caused appreciable decreases in glucose production rate. The severity of starch hydrolysis to dextrin markedly affected ultimate glucose yields. The diffusional gradients present in the carrier pores caused the immobilized enzyme to yield lower glucose concentrations than the free enzyme at similar feed conditions.     

Preparation of high-capacity supports containing protein G immobilized to porous silica

This study examined the preparation of high-capacity silica supports containing immobilized protein G. A maximum content of 39 mg protein G/g silica was obtained when using 100 Å pore size silica, followed by 33 mg/g for 50 Å silica and 9.3-24 mg/g for 300-4000 Å silica. The surface coverage of protein G increased with pore size, with a maximum level of 0.037 μmol/m² being obtained for 4000 Å silica. These supports gave comparable apparent activities (i.e., 30-47% binding to rabbit immunoglobulin G [IgG]), with the highest binding capacities (71-77 mg IgG/g silica) being obtained for 50-100 Å silica.     

Properties of ribulose diphosphate carboxylase immobilized on porous glass

Ribulose-1,5-diphosphate carboxylase from spinach has been bound to arylamine porous glass with a diazo linkage and to alklamine porous glass with glutaraldehyde. Stability at elevated temperatures and responses to changes of pH and ribulose-1,5-diphosphate, Mg²⁺, and dithiothreitol concentrations were not significantly different from the soluble enzyme, though stability at 4°C was somewhat improved.     

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.     

Glucose oxidase enzyme immobilized porous silica for improved performance of a glucose biosensor

High activity of glucose oxidase (GOD) enzyme (immobilized in porous silica particles) is desirable for a better glucose biosensor. In this work, effect of pore diameter of two porous hosts on enzyme immobilization, activity and glucose sensing was compared. The hosts were amine functionalized: (i) microporous silica (NH₂-MS) and (ii) mesoporous silica (NH₂-SBA-15). Based on whether the dimension of GOD is either larger or smaller than the pore diameter, GOD was immobilized on either external or internal surface of NH₂-MS and NH₂-SBA-15, with loadings of 512.5 and 634 mg/g, respectively. However, GOD in NH₂-SBA-15 gave a higher normalized absolute activity (NAA), which led to an amperometric sensor with a larger linear range of 0.4–13.0 mM glucose. In comparison, GOD in NH₂-MS had a lower NAA and a smaller linear range of 0.4–3.1 mM. In fact, the present GOD-NH₂-SBA-15 electrode based sensor was better than other MS and SBA-15 based electrodes reported in literature. Thus, achieving only a high GOD loading (as in NH₂-MS) does not necessarily give a good sensor performance. Instead, a host with a relatively larger pore than enzyme, together with optimized electrode composition ensures the sensor to be functional in both hyper- and hypoglycemic range.     

Preparation and activity of carbonic anhydrase immobilized on porous silica beads and graphite rods

Techniques for the immobilization of bovine carbonic anhydrase (BCA) on porous silica beads and graphite are presented. Surface coverage on porous silica beads was found to be 1.5 x 10(-5) mmol BCA/m(2), and on graphite it was 1.7 x 10(-3) mmol BCA/m(2) nominal surface area. Greater than 97% (silica support) and 85% (graphite support) enzyme activity was maintained upon storage of the immobilized enzyme for 50 days in pH 8 buffer at 4 degrees C. After 500 days storage, the porous silica bead immobilized enzyme exhibited over 70% activity. Operational stability of the enzyme on silica at 23 degrees C and pH 8 was found to be 50% after 30 days. Catalytic activity expressed as an apparent second-order rate constant K'(Enz) for the hydrolysis of p-nitrophenyl acetate (p-NPA) catalyzed by BCA immobilized on silica beads and graphite at pH 8 and 25 degrees C is 2.6 x 10(2) and 5.6 x 10(2) M(-1)s(-1) respectively. The corresponding K(ENZ) value for the free enzyme is 9.1 x 10(2) M(-1)s(-1). Activity of the immobilized enzyme was found to vary with pH in such a manner that the active site pK, on the porous silica bead support is 6.75, and on graphite it is 7.41. Possible reasons for a microenvironmental influence on carbonic anhydrase pK(a), are discussed. Comparison with literature data shows that the enzyme surface coverage on silica beads reported here is superior to previously reported data on silica beads and polyacrylamide gels and is comparable to an organic matrix support. Shifts in BCA-active site pK(a) values with support material, a lack of pH dependent activity studies in the literature, and differing criteria for reporting enzyme activity complicate literature comparisons of activity; however, immobilized BCA reported here generally exhibits comparable or greater activity than previous reports for immobilized BCA.     

Investigation of the operational stabilities and kinetics of glucoamylase immobilized on alkylamine derivatives of titanium(IV)-activated porous inorganic supports

Glucoamylase (exo-1,4-α-d-glucosidase, EC 3.2.3.1) was coupled to several porous silica matrices by an improved metal-link/chelation process using alkylamine derivatives of titanium(IV)-activated supports. In order to select the titanium activation procedure which gave stable enzyme preparations, long-term stability tests were performed. The immobilized glucoamylase preparations, in which the carrier was activated to dryness with a 15% w/v TiCl₄ solution, displayed very stable behaviour, with half-lives of ～60 days. The optimum operating conditions were determined for these preparations. There are significant differences between the behaviour of the immobilized enzyme and the free enzyme. The apparent K_m increased on immobilization due to diffusional resistances. The pH optimum for the immobilized preparation showed a slight shift to acid pH relative to that of the soluble enzyme. Also, the optimum temperature descreased to 60°C after immobilization. In order to test Michaelis-Menten kinetics at high degrees of conversion, time-course analysis of soluble starch hydrolysis was performed. It was observed that simple Michaelis-Menten kinetics are not applicable to the free/immobilized glucoamylase-starch system at high degrees of conversion.     

Lipoamide dehyrogenase immobilized on porous glass.

Lipoamide dehydrogenase (NADH:lipoamide oxidoreductase, EC 1.6.4.3) isolate from pig heart and Escherichia coli was covalently coupled by both diazonium and amide bonds to controlled pore glass beads (96% silica). When the enzyme was immobilized in the presence of NAD+, the enzyme no longer exhibited its normal requirement for NAD+ for full activity. If the immobilized enzyme was then treated with NADase, the requirement for NAD+ was restored. Enzyme immobilized in the absence of NAD+ exhibited normal NAD+ dependence both prior to an after NADase treatment. These results are discussed in terms of co-immobilization of NAD+ at or near the allosteric site of the enzyme.     

Hydrolysis of aryl beta-maltotriosides by sweet potato beta-amylase and soybean beta-amylase.

Sweet potato beta-amylase [EC 3.2.1.2, alpha 1,4-D-glucan maltohydrolase]-catalyzed hydrolyses of aryl beta-maltotriosides with substituents, NO2-, Cl-, and Br- at the o-, m-, and p-positions in the phenyl ring were studied at pH 4.8 and 25 degrees C. The hydrolyses of a few of the maltotriosides by soybean beta-amylase [EC 3.2.1.2, alpha-1,4-D-glucan maltohydrolase] were also studied at pH 5.4 and 25 degrees C. It was found that the aryl beta-maltotriosides were preferentially hydrolyzed into maltose and aryl beta-D-glucosides by both beta-amylases. The Michaelis constant Km and the molecular activity ko were determined for the hydrolyses of these maltotriosides and compared with those of maltotriose and maltotetraose. Aryl beta-maltotriosides were more rapidly hydrolyzed than maltotriose by a factor of 30--80, and more slowly hydrolyzed than maltotetraose by a factor of 10--30, depending on the kinds of substituents. The rapid hydrolysis of aryl beta-maltotrioside as compared with maltotriose may be due to the interaction of an aryl group with the subsite of beta-amylase. This is in contrast with glucoamylase [EC 3.2.1.3, alpha-1,4-D-glucan glucohydrolase] of Rhizopus niveus-catalyzed hydrolysis of phenyl beta-maltoside, whose phenyl group does not interact so much with the subsite of the enzyme.     

Preparation of an immobilized two-enzyme system, beta-amylase-pullulanase, to an acrylic copolymer for the conversion of starch to copolymer for the conversion of starch to maltose. I. Preparation and stability of immobilized beta-amylase

β-Amylase (EC 3.2.1.2), obtained from barley, was chemically attached to a crosslinked copolymer of acrylamide-acrylic acid using a water-soluble carbodiimide. The derivative showed 23% β-amylase activity in relation to that of free enzyme with a coupling yield of 40% based on the amount of added β-amylase. In order to find optimal coupling conditions, the effect of pH and different carbodiimide concentrations was investigated. The enzymic activity associated with different β-amylase concentrations was further outlined. A slightly increased operational stability for the enzyme upon immobilization was observed. Markedly improved operational stability has been obtained by coupling in the presence of reduced glutathione of bovine serum albumin.     

Characteristics of yeast invertase immobilized on porous cellulose beads.

Invertase from Candida utilis was immobilized on porous cellulose beads by an ionic-quanidino bond. The immobilized invertase showed optimum activity between pH 4.0 and 5.4, while the free enzyme had a sharp optimum at pH 4.1. Both temperature profiles were fairly similar up to 55 degrees C. However, above this temperature the immobilized enzyme was more stable than the free enzyme. From the temperature data, the activation energies were found to be 7,322 and 4,052 cal/g mol for the free and the immobilized enzyme, respectively. Candida invertase shows characteristics of substrate inhibition. Both the Km and Ki for the free and the immobilized enzymes were determined. The apparent Ki for the immobilized invertase was much higher than the Ki of the free enzyme, suggesting a diffusion effect. Immobilized invertase molecules deep in the pores only see sucrose concentrations much less than the bulk concentrations. Immobilization, thus, offers certain processing advantages in this regard.     

Adsorption of charged substrates and products on an enzyme reactor prepared by glutaraldehyde coupling on alkylamine derivatives of Ti(IV)-coated porous silica beads

Ti(IV) coating of porous silica beads, followed by derivatization with 1,6-diaminohexane and activation with glutaraldehyde was tested for the immobilization of glutamate decarboxylase (l-glutamate 1-carboxylyase, EC 4.1.1.15). The enzyme column prepared with the immobilized glutamate decarboxylase was designed for the preparation of 1 μmol γ-[¹³N]aminobutyric acid, a new tracer for positron emission tomography. Preliminary results, indicating high immobilization yields of active enzyme with good long term stabilities, led to a more detailed investigation of the Ti(IV) coating. When a column, containing about 1 g of enzyme-loaded beads was used for the synthesis of γ-[¹³N]aminobutyric acid (GABA) from l-[¹³N]glutamate, most of the¹³N activity remained adsorbed onto the column. The elution patterns of l-glutamate and GABA from columns of glutamate decarboxylase, immobilized on Ti(IV) coated silica beads, were investigated by using an h.p.l.c. u.v. detector. Different treatments of the Ti(IV) coated supports were tested to improve the desorption kinetics of GABA and l-glutamate. None of these methods gave a satisfactory improvement of the elution patterns of GABA and l-glutamate. The results indicate that the Ti(IV) coated silica beads have a large adsorption capacity, even though the enzyme is covalently linked. The described immobilization method is not recommended for enzymes having charged substrates or products and in which a small amount of substrate has to be applied onto a reactor containing a large amount of Ti(IV) coated support. The method can be applied when the enzyme reactor is operated in steady state conditions with continuous supply of substrate.     

Investigation of the binding mechanism of glucoamylase to alkylamine derivatives of titanium(IV)-activated porous inorganic supports

Glucoamylase (exo-1,4-α-d-glucosidase, EC 3.2.1.3) has been coupled to several porous silica matrices by a new covalent process using alkylamine derivatives of titanium(IV)-activated supports. In order to investigate the interaction of the titanium element with the silanol groups of the inorganic matrices, activation was performed at different times, using titanium(IV) chloride, either pure or as a 15% w/v solution, in 15% w/v hydrochloric acid at 25, 45 and 80°C, followed by washing with sodium acetate buffer (0.02m, pH 4.5) or chloroform. Using pure TiCl₄, the highest activities of all preparations were obtained at 80°C and with acetate buffer washing, resulting from a higher content of titanium coating of the carrier. When activation was performed in aqueous TiCl₄ solution, followed by a drying step, the highest activity was obtained with preparations washed with chloroform, with or without amination. When reacting pure TiCl₄ with controlled pore glass (CPG) and with porous silica (Spherosil), colour formation was observed after reaction of glutaraldehyde with the aminated support. This did not happen when Celite was used as the support. As a criterion for comparison of the different immobilized enzyme preparations, the concept of an ‘instability factor’, which measures the percentage of immobilized enzyme activity due to release of enzyme into solution, is introduced. Instability factors of immobilized enzyme preparations on Celite were always higher than those obtained with the other matrices, confirming that there was no covalent coupling of the enzyme to Celite. However, when the activation was performed with aqueous TiCl₄ solution with drying, Schiff's base formation was observed in all preparations and very stable immobilized enzyme preparations were obtained. The results of the activation of controlled pore glass and porous silica with pure titanium(IV) chloride suggest the existence of a true reaction between the titanium element and the silanol groups of these carriers by formation of a bridge, Si-O-Ti, while with the titanium(IV) chloride solution in hydrochloric acid, a coating of hydrous titanium(IV) oxide is obtained.     

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.     

Affinity chromatography of proteinases using bacitracin immobilized to porous glass beads

J. FONTECHA, T. REQUENA AND H.E. SWAISGOOD. 1996. This study describes an affinity chromatography procedure for proteinase purification using bioselective binding to immobilized bacitracin. By coupling bacitracin to controlled-pore glass (CPG) beads, an affinity matrix was obtained that permitted rapid purification of proteinases under conditions that minimize autolysis. Bacitracin-CPG was used to bioselectively adsorb the extracellular proteinase secreted by Enterococcus faecalis var. liquefaciens IFPL 383. The overall purification obtained with this procedure was 5149-fold. The ability of bacitracin-CPG to bind other proteinases was examined using various commercial proteinases. The specific activities of subtilin BPN' and proteinase K were increased by bioselective adsorption and excellent recoveries of all proteinases applied were obtained.     

Fourier transform infrared assay of membrane lipids immobilized to silica: leaching and stability of immobilized artificial membrane-bonded phases

A nondestructive, sensitive assay to monitor the hydrocarbon content of silica-based chromatography particles has been developed. The assay requires a microscope accessory interfaced with a Fourier transform infrared (FTIR) spectrometer. For determining hydrocarbon content, undiluted alkyl-silica-bonded phases were pressed into a thin wafer. Hydrocarbon content was quantitated using the integrated hydrocarbon band intensity between 2995 and 2825 cm-1 [i.e., band area C-H] and the integrated silica oxide band intensity between 1945 and 1780 cm-1 [i.e., band area Si-O]. Plotting the [band area C-H]/[band area Si-O] ratio vs the carbon content determined by elemental analysis gave a correlation coefficient of r = 0.997. The FTIR assay was validated on 5-, 7-, and 12-microns silica particles using three different immobilized artificial membrane (IAM) silica-bonded phases. The utility of the FTIR assay in determining hydrocarbon content was demonstrated by evaluating hydrocarbon leaching from IAM phases exposed to mobile-phase solvents. The ability of organic solvents to leach hydrocarbon from IAM phases containing phosphatidylcholine (PC) as the immobilized ligand was chloroform greater than ethanol approximately methanol greater than ethyl acetate greater than methylene chloride greater than acetonitrile greater than acetone. Acetone and acetonitrile cause very little hydrocarbon leaching from HPLC-IAM.PC columns. When challenged with different mobile phases, IAM.PC columns perfused with mobile phase are more stable than IAM.PC-bonded phases stirred in mobile phases. IAM.PC contains lecithin linked to silica by amide bonds.(ABSTRACT TRUNCATED AT 250 WORDS)     

Immobilization of enzymes on porous silica supports

Four silica supports differing in pore dimensions were activated by treatment with SiCl₄ and then with ethylenediamine to obtain alkylamine groups on the silica surface. Three enzymes, peroxidase from cabbage, glucoamylase from Aspergillus niger C and urease from soybean were immobilized on these supports using glutaraldehyde as coupling agent. It was found that the protein content, the retained enzymatic activity and the storage stability of the silica supported enzymes were considerably affected by support pore size and enzyme molecular weight, the factors which are supposed to alter protein distribution inside the support pores. The highest activity was found for peroxidase and glucoamylase attached to the silica with the widest pores, but their loss in activity during storage was considerable. The urease retained less activity after immobilization, but its storage stability was excellent.