Chemically modified porous silica gel as a bioadsorbent and a biocatalyst.

Aminopropyl silica gel was prepared from porous silica gel by reaction with γ-aminopropyltrimethoxysilane in toluene and was used for immobilizing chymotrypsin (EC 3.4.4.5) and human serum albumin. Immobilized chymotrypsin was used for the resolution of N-acetyl-dl-phenylalanine and immobilized human serum albumin was used for the purification of goat anti-human serum albumin. Epoxy silica gel, prepared by reaction of porous silica gel with γ-glycidoxypropyltriethoxysilane, was coupled with m-aminobenzamidine and the resulting matrix was used for trypsin purification.     

Production of L-lysine by immobilized trypsin. Study of DL-lysine methyl ester resolution

The possibility of producing L-lysine from chemically synthesized DL-lysine has been investigated. Optical resolution of racemic DK-lysine may be achieved by using the stereospecific esterasic activity of trypsin on DL-lysine methyl ester, which gives L-lysine and unchanged D-lysine methyl ester. SL-lysine methyl ester spontaneous hydrolysis may be neglected when operating at pH 5.5 and 30 degrees C. Effect of pH and substrate concentration on hydrolysis rate has been investigated when using as a catalyst either soluble or immobilized trypsin. For this purpose, trypsin was coupled onto an amine porous silica, Spherosil, activated with glutaraldehyde. The optimal pH is 5.8 for soluble trypsin and 6.0 for immobilized trypsin. It was yet possible to lower the parent optimal pH of immobilized trypsin, and thus increase its activity at 5.5, by co-grafting onto Spherosil an aminosilane, for enzyme coupling via glutaraldehyde activation and a positively charged diethyl amino ethyl (DEAE) silane, for decreasing the pH of trypsin microenvironment.     

Characterization of efficient proteolysis by trypsin loaded macroporous silica

Tryptic digestion of proteins in trypsin loaded porous silica has been shown to be highly efficient. Enzymatic silica-reactors were prepared by immobilizing trypsin into macroporous ordered siliceous foam (MOSF) and into mesoporous SBA-15 silica which has a smaller pore size. The tryptic products from the silica reactors were analyzed by matrix-assisted laser desorption ionization time-of-flight mass spectrometry (MALDI-TOF MS), and a higher proteolysis efficiency was obtained with MOSF. These results can be well interpreted by a sequential digestion model taking into account the confinement and concentration enrichment of both the substrates and enzymes within the silica pores. Proteins at low concentrations and proteins in urea and surfactant solutions were also successfully digested with the MOSF-based reactor and identified by MS. Considering that the immobilized trypsin could retain its enzymatic activity for weeks, this MOSF reactor provides many advantages compared to free enzyme proteolysis. As a proof-of-concept, the digest of a real complex sample extracted from the cytoplasm of mouse liver tissue using trypsin loaded MOSF yielded better results than the typical in-solution protocol.     

Use of hexadecyl Fractosil as a hydrophobic carrier for adsorptive immobilization of proteins

Fractosil, a porous form of silica, has been used for the preparation of a hydrophobically derivatized carrier for protein immobilization. Interaction of a number of arbitrarily chosen proteins with hexadecyl-substituted Fractosil has been investigated. Binding of proteins was found to take place with retention of their native properties. Glutamate dehydrogenase, used as a model allosteric protein, was found to retain its catalytic and allosteric properties upon binding to the adsorbent in the form of suspension or column. Positive cooperative interactions for binding of bovine serum albumin and glutamate dehydrogenase to the matrix were observed. These findings are discussed in terms of hydrophobic interactions occurring between various residues of the protein molecules and the hydrophobic ligands in addition to those interactions which may occur with the unsubstituted gel. Results presented on immobilized glutamate dehydrogenase, trypsin, alpha-chymotrypsin, alpha-amylase, and amyloglucosidase clearly indicate possible potential of the support for continuous catalytic transformations.     

Chemically surface modified gel (CSMG): an excellent enzyme-immobilization matrix for industrial processes

Invertase from S. cerevisiae has been immobilized on porous silica matrix, formed using sol-gel chemistry, with surface area of approximately 650 m(2)/g. The co-condensation of silica sol with 3-aminopropyl(triethoxy)silane produced an amino-chemically surface modified silica gel (N-CSMG) with a very high ligand loading of 3.6 mmol/g SiO(2); significantly higher than commercially available matrices. Surface amine groups were activated with glutaraldehyde to produce GA-N-CSMG, and invertase covalently attached by the aldehyde. Invertase was used as a model enzyme to measure the immobilizing character of the GA-N-CSMG material. Using an optimized immobilization protocol, a very high loading of 723 mg invertase per gram GA-N-CSMG is obtained; 3-200-fold higher than values published in literature. The reproducible, immobilized activity of 246,000 U/g GA-N-CSMG is also greater than any other in literature. Immobilized invertase showed almost 99% retention of free enzyme activity and no loss in catalytic efficiency. The apparent kinetic parameters K(M) and V(M) were determined using the Michealis-Menten kinetic model. K(M) of the free invertase was 1.5 times greater than that of the immobilized invertase--indicating a higher substrate affinity of the immobilized invertase. These findings show considerable promise for this material as an immobilization matrix in industrial processes.     

Porous zirconia: a new support material for enzyme immobilization

Four different proteases (trypsin, chymotrypsin, papain and pepsin) were covalently attached to the surface of a new type of porous zirconia, as well as a conventional porous silica, activated with 3-isothiocyanatopropyltriethoxy silane (NCS-silane). The immobilization efficiency onto the porous zirconia material was evaluated in terms of the amount of enzyme attached to the particles and from the biological activity remaining after the immobilization step. The results were compared with the corresponding experiments with a porous silica of similar surface area/g support material. In addition, the storage stability of the modified zirconia and silica biocatalysts were evaluated. These results indicated that specific immobilized enzyme biocatalysts can be achieved with this new zirconia support material which exhibits different properties to those observed with the more conventional silica-based materials. Moreover, the results with the enzyme-zirconia biocatalysts also indicate different characteristics when compared with data for the same enzymes immobilized under similar buffer conditions to organic support materials as previously described by various other investigators. The advantages of zirconia-based immobilized enzyme biocatalysts in terms of their density and chemical robustness are also described relative to other alternative support materials currently in use.     

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.     

Use of porous pyrolytic carbon for analytical and microscale high-performance liquid chromatographic bioseparations

Porous carbonaceous adsorbent was prepared by carbonization of saccharose in silica gel pores followed by leeching out of the silica matrix. The product of pyrolysis was then deactivated by hydrogenation. The resulting adsorbent shows intermediate sorption properties between those of the highly polar pyrolytic glassy carbon and the hydrophobic graphitized carbon. The microparticulate mesoporous carbon was examined for its use in capillary HPLC separations. The separation of selected stereoisomers in a 320 μm I.D. capillary column packed with the porous carbon particles is described and discussed. Additionaly, the porous carbon filled with dextran gel was tested as a material for direct HPLC analysis of drugs in human serum.     

Development of sensors for direct detection of organophosphates. Part I: Immobilization, characterization and stabilization of acetylcholinesterase and organophosphate hydrolase on silica supports

Biosensors for organophosphates in solution may be constructed by monitoring the activity of acetylcholinesterase (AChE) or organophosphate hydrolase (OPH) immobilized to a variety of microsensor platforms. The area available for enzyme immobilization is small (< 1 mm2) for microsensors. In order to construct microsensors with increased surface area for enzyme immobilization, we used a sol-gel process to create highly porous and stable silica matrices. Surface porosity of sol-gel coated surfaces was characterized using scanning electron microscopy; pore structure was found to be very similar to that of commercially available porous silica supports. Based upon this analysis, porous and non-porous silica beads were used as model substrates of sol-gel coated and uncoated sensor surfaces. Two different covalent chemistries were used to immobilize AChE and OPH to these porous and non-porous silica beads. The first chemistry used amine-silanization of silica followed by enzyme attachment using the homobifunctional linker glutaraldehyde. The second chemistry used sulfhydryl-silanization followed by enzyme attachment using the heterobifunctional linker N-gamma-maleimidobutyryloxy succinimide ester (GMBS). Surfaces were characterized in terms of total enzyme immobilized, total and specific enzyme activity, and long term stability of enzyme activity. Amine derivitization followed by glutaraldehyde linking yielded supports with greater amounts of immobilized enzyme and activity. Use of porous supports not only yielded greater amounts of immobilized enzyme and activity, but also significantly improved long term stability of enzyme activity. Enzyme was also immobilized to sol-gel coated glass slides. The mass of immobilized enzyme increased linearly with thickness of coating. However, immobilized enzyme activity saturated at a porous silica thickness of approximately 800 nm.     

Immobilization of glucoamylase on porous silicas

The influence of the pore structure of silica carriers (macroporous silica gels, silochromes and porous glasses) on the catalytic activity of immobilized glucoamylase (exo 1,4-α-d-glucosidase, 1,4-α-d-glucan glucohydrolase EC 3.2.1.3) has been studied. The dependence of the immobilized glucoamylase activity, in units g^?1, on the carrier pore diameter was found to pass through a maximum within a range 70–100 nm. Macroporous silica gels can be used with success as carriers for glucoamylase immobilization instead of porous glasses and silochromes.     

Preparation and characterization of silica gel/chitosan composite for the removal of Cu(II) and Pb(II)

Silica gel/chitosan composite (SiCS) was prepared via., sol-gel method by mixing silica gel and chitosan and cross-linked with bifunctional cross-linker glutaraldhyde. The SiCS composite was characterized using FT-IR, SEM-EDAX, XRD and BET methods. The sorption of copper and lead ions onto SiCS has been investigated. The SiCS composite was found to have excellent metal sorption capacity than the silica gel (Si) and chitosan (CS). The sorption experiments were carried out in batch mode to optimize various parameters viz., contact time, pH, initial metal ion concentration, co-ions and temperature that influence the sorption. Langmuir, Freundlich and Dubinin-Radushkevich adsorption isotherm models were applied to describe isotherm constants. Equilibrium data agreed well with the Freundlich isotherm model. Thermodynamic studies revealed that the nature of sorption is spontaneous and endothermic. The SiCS removes metals by means of adsorption and complexation. Sorption capacity of SiCS is compared with other sorbents which suggest that this composite was useful for removing copper and lead from aqueous solution.     

Digital microfluidic hydrogel microreactors for proteomics

Proteolytic digestion is an essential step in proteomic sample processing. While this step has traditionally been implemented in homogeneous (solution) format, there is a growing trend to use heterogeneous systems in which the enzyme is immobilized on hydrogels or other solid supports. Here, we introduce the use of immobilized enzymes in hydrogels for proteomic sample processing in digital microfluidic (DMF) systems. In this technique, preformed cylindrical agarose discs bearing immobilized trypsin or pepsin were integrated into DMF devices. A fluorogenic assay was used to optimize the covalent modification procedure for enzymatic digestion efficiency, with maximum efficiency observed at 31 μg trypsin in 2-mm diameter agarose gel discs. Gel discs prepared in this manner were used in an integrated method in which proteomic samples were sequentially reduced, alkylated, and digested, with all sample and reagent handling controlled by DMF droplet operation. Mass spectrometry analysis of the products revealed that digestion using the trypsin gel discs resulted in higher sequence coverage in model analytes relative to conventional homogenous processing. Proof-of-principle was demonstrated for a parallel digestion system in which a single sample was simultaneously digested on multiple gel discs bearing different enzymes. We propose that these methods represent a useful new tool for the growing trend toward miniaturization and automation in proteomic sample processing.     

High-throughput protein digestion by trypsin-immobilized monolithic silica with pipette-tip formula

Based on the monolithic silica gel materials with hierarchical pore structure and on the SPE devices (MonoTip) developed thereof, a trypsin-immobilized monolithic silica in a pipette tip (MonoTip Trypsin) suitable for digesting proteins has been newly developed. The surface of monolithic silica fixed into the tip was chemically modified with trypsin via an aminopropyl group. Trypsin-immobilized monolith successfully performed a rapid digestion of reduced and alkylated proteins with only a few times pipetting operation for the pre-treatment procedure of chromatographic analysis. The novel solid-phase digestion tool using monolithic silica allows a high-throughput trypsin proteolysis of bio-substances in proteomics.     

Dextran synthesis by immobilized dextran sucrase

Dextran sucrase has been produced by fermentation of Leuconostoc mesenteroides NRRL B-512, with and without continuous sucrose addition to improve enzyme production. The enzyme preparation has been concentrated from the fermentation broth by ultrafiltration and purified by gel permeation chromatography on Ultrogel. The specific activity of the dextran sucrase was greatly enhanced by calcium chloride addition to the purified enzyme. This enzyme preparation has been immobilized by covalent coupling onto an amino porous silica support (Spherosil) activated with glutaraldehyde. Immobilized dextran sucrase derivatives with an activity up to 830 dextran sucrase units per g. support could thus be obtained. The effect of the support specific area on coupling efficiency and reaction kinetics has been investigated, and the effect of intraparticular diffusion underlined. The molecular weight distribution of the dextran has been determined when varying several parameters.     

High-throughput protein digestion by trypsin-immobilized monolithic silica with pipette-tip formula

Based on the monolithic silica gel materials with hierarchical pore structure and on the SPE devices (MonoTip®) developed thereof, a trypsin-immobilized monolithic silica in a pipette tip (MonoTip® Trypsin) suitable for digesting proteins has been newly developed. The surface of monolithic silica fixed into the tip was chemically modified with trypsin via an aminopropyl group. Trypsin-immobilized monolith successfully performed a rapid digestion of reduced and alkylated proteins with only a few times pipetting operation for the pre-treatment procedure of chromatographic analysis. The novel solid-phase digestion tool using monolithic silica allows a high-throughput trypsin proteolysis of bio-substances in proteomics.     

Evaluation of a silica-coated magnetic nanoparticle for the immobilization of a His-tagged lipase

Magnetic particles of size 10 nm have been coated with silica to a mean diameter of 40 nm and charged with Cu²⁺ ions via a multidentate ligand, iminodiacetic acid (IDA), for the immobilization of His-tagged Bacillus stearothermopilus L1 lipase. Microporous (average pore diameter of 60 Å) silica gel with a mean particle diameter of 115 µm has been used as a comparative support material. The molar ratio of Cu²⁺ to IDA was found to be 1:1.14 and 1:1.99 in the silica gel and the silica-coated magnetic nanoparticles (SiMNs), respectively. The specific activity of the immobilized enzyme was found to conform to the following order: Cu²⁺-charged SiMN>SiMN>Cu²⁺-charged silica gel>silica gel. When it was immobilized on the Cu²⁺-charged SiMNs, over 70% of the initial activity of the lipase remained after it had been reused five times. However, only 20% of the initial activity remained after the enzyme immobilized on the Cu²⁺-charged silica gel had been reused five times. For the enzyme immobilized on supports without Cu²⁺ cations, all activity was lost after threefold reuse. The differences in the specific activities and the efficiencies of reuse of the enzymes immobilized on the various support materials are discussed in terms of immobilization mechanisms (physical adsorption vs. coordination bonding), mass transfer of a substrate and a product of the enzyme reaction, and the status of the Cu (Cu bound to the IDA on the silica layer vs. Cu directly adsorbed on the silica layer).     

Immobilized trypsin on hydrophobic cellulose decorated nanoparticles shows good stability and reusability for protein digestion

The preparation of biocatalysts based on immobilized trypsin is of great importance for both proteomic research and industrial applications. Here, we have developed a facile method to immobilize trypsin on hydrophobic cellulose-coated silica nanoparticles by surface adsorption. The immobilization conditions for the trypsin enzyme were optimized. The as-prepared biocatalyst was characterized by Fourier transform infrared spectroscopy, transmission electron microscopy, and elemental analysis. In comparison with free enzyme, the immobilized trypsin exhibited greater resistances against thermal inactivation and denaturants. In addition, the immobilized trypsin showed good durability for multiple recycling. The general applicability of the immobilized trypsin for proteomic studies was confirmed by enzymatic digestion of two widely used protein substrates: bovine serum albumin (BSA) and cytochrome c. The surface adsorption protocols for trypsin immobilization may provide a promising strategy for enzyme immobilization in general, with great potential for a range of applications in proteomic studies.     

Stabilization of prostaglandin synthetase by immobilization of goat seminal microsomes on silica gel-G

Prostaglandin synthetase was immobilized by adsorption of goat vesicular microsomes on silica gel containing CaSO4 (silica gel G). Repeated cycles of enzymatic conversion of arachidonic acid to prostaglandin by the immobilized microsomes increased the product yield by 1.5 fold, in comparison to the same by free microsomal particles. The presence of Ca2+ in silica gel is responsible for this improved yield of prostaglandin as the divalent metal ion stabilized prostaglandin synthetase activity in a remarkable way. Microsomal particles immobilized on solid supports like alumina G and controlled pore glass were not very effective.     

A simple kinetic model for the hydrolysis of α-d-glucans using glucoamylase immobilized on titanium (IV) activated porous silica

A simple kinetic model which describes the hydrolysis of α-d-glucans by immobilized glucoamylase (exo-1,4-d-glucosidase, EC 3.2.1.3) is reported. The hydrolysis of starch, amylose, amylopectin, maltose and 40DE starch hydrolysates using glucoamylase immobilized on alkylamine derivatives of titanium(IV) activated porous silica are described by a kinetic model based on Langmuir-Hinshelwood kinetics. This model involves enzyme kinetics with or without product inhibition and reverse reactions as well as mass transfer and diffusion effects in immobilized enzyme reactors. The results of other authors are also interpreted by the model developed in this article.     

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.