Synthesis of tentacle-type magnetic beads as immobilized metal-chelate affinity support for cytochrome c adsorption

Magnetic poly(2-hydroxyethylmethacrylate) (mPHEMA) beads with an average diameter of 100-140 microm were produced by suspension polymerization in the presence of magnetite particles (i.e. Fe3O4). Specific surface area and average pore size of the magnetic beads was found to be 50 m2/g and 819 nm, respectively. Ester groups in the mPHEMA structure were converted to imine groups by reacting with poly(ethyleneimine) (PEI) in the presence of NaH. Amino (-NH2) content of PEI-attached mPHEMA beads was determined as 102 mg PEI/g. Then, Cu2+ ions were chelated on the magnetic beads in the range of 20-793 micromol Cu2+/g. Cytochrome c (cyt c) adsorption was performed on the metal chelating beads from aqueous solutions containing different amounts of cyt c at different pHs, Cu2+ loadings and temperatures. Cyt c adsorption on the mPHEMA/PEI beads was 4.6 mg/g. Cu2+ chelation increased the cyt c adsorption significantly (40.1 mg/g). Adsorption capacity increased with Cu2+ loading and then reached a saturation value. Cyt c adsorption decreased with increasing temperature. Cyt c molecules could be reversibly adsorbed and eluted ten times with the magnetic adsorbents without noticeable loss in their cyt c adsorption capacity. The applicability of two kinetic models including pseudo-first order and pseudo-second order model was estimated on the basis of comparative analysis of the corresponding rate parameters, equilibrium capacity and correlation coefficients. Results suggest that chemisorption processes could be the rate-limiting step in the adsorption process. In the last part of this article, cyt c adsorption experiments were performed in a magnetically stabilized fluidized bed (MSFB) system at optimum conditions determined from the batch experiments. The adsorption capacity decreased significantly from 46.8 to 15.4 mg/g polymer with the increase of the flow-rate from 0.5 to 4.0 ml/min. The resulting magnetic chelator beads possessed excellent long-term storage stability.     

Protein dye affinity chromatography using immobilized tetraiodofluorescein

The chromatographic behavior of a heterogeneous protein mixture and of a series of homogeneous proteins on the immobilized dye tetraiodofluorescein has been observed and analyzed. Less than 6%, of the millimolar concentration of dye immobilized to a porous agarose matrix is accessible to protein. The affinity of a protein for immobilized dye is dramatically increased by insertion of apolar spacer atoms between the dye and the matrix. Dye columns constructed with a 9-atom spacer can be used to advantage for the retention and competitive elution of proteins not found previously amenable to dye chromatography.     

Agar-based magnetic affinity support for protein adsorption

Magnetic colloidal particles were prepared by a coprecipitation method. The particles were composed of nanometer-sized superparamagnetic Fe(3)O(4) particles stabilized by lauric acid. Then, magnetic agar gel beads were produced by a water-in-oil emulsification method using a mixture of agar solution and the magnetic colloidal particles as the aqueous phase. A reactive triazine dye, Cibacron blue 3GA (CB), was coupled to the gel to prepare an agar-based magnetic affinity support (MAS) for protein adsorption. The support showed good magnetic responsiveness in a magnetic field. Bovine serum albumin (BSA) was used as a model protein to test adsorption equilibrium and kinetic behavior of the MAS. The adsorption equilibrium of BSA to the MAS was described by the Langmuir-type isotherm. Adsorption capacity of the MAS for BSA was up to 25 mg/mL at a CB coupling density of 1.6 micromol/mL. The effect of ionic strength on BSA adsorption was complex, exhibiting a maximum capacity at an ionic strength of 0.06 mol/L. The adsorption of BSA to the MAS was also influenced by pH. Uptake rate of BSA to the MAS was analyzed using a pore diffusion model. The pore diffusion coefficient was estimated to be 1.75 x 10(-11) m(2)/s. Finally, recycled use of the MAS demonstrated the stability of the MAS in protein adsorption and magnetic responsiveness.     

Immobilization of catalase via adsorption onto metal-chelated affinity cryogels

A poly (acrylamide-allylglycidyl ether) [p(AAm-AGE)] cryogel was prepared by radical polymerization of acrylamide (AAm) and allylglycidyl ether (AGE). Cibacron Blue F3GA (CB) was covalently attached to the p(AAm-AGE) cryogel via the reaction between the chloride groups of the reactive dyes and the epoxide groups of the AGE. The CB-attached p(AAm-AGE) cryogel was chelated with Fe³⁺ ions. This immobilized metal ion affinity chromatography (IMAC) cryogel carrying 25.8 ± 2.0 μmol Fe³⁺ ions was used in adsorption studies to interrogate the effects of pH, protein initial concentration, flow rate, temperature and ionic strength on enzyme activity. Maximum adsorption capacities were found to be 75.7 ± 1.2 mg/g for p(AAm-AGE)-CB-Fe³⁺ cryogels and 60.6 ± 1.0 mg/g for p(AAm-AGE)-CB cryogels, respectively. The adsorbed amounts of catalase per unit mass of cryogel reached a plateau value at about 1.5 mg/mL at pH 6.0. The K_m values were found to be 0.73 ± 0.02 g/L for the free catalase and 0.18 ± 0.02 g/L for the immobilized catalase. The V_max value of free catalase (2.0 × 10³ U/mg enzyme) was found to be lower than that of the immobilized catalase (2.5 × 10³ U/mg enzyme). It was also observed that the enzyme could be repeatedly adsorbed and desorbed onto the p(AAm-AGE)-CB-Fe³⁺ cryogel.     

A novel magnetic affinity support for protein adsorption and purification

A novel magnetic support was prepared by an oxidization-precipitation method with poly(vinyl alcohol) (PVA) as the entrapment material. Transmission electron microscopy indicated that the magnetic particles had a core-shell structure, containing many nanometer-sized magnetic cores stabilized by the cross-linked PVA. The particles showed a high magnetic responsiveness in magnetic field, and no aggregation of the particles was observed after the particles had been treated in the magnetic field. These facts indicated that the particles were superparamagnetic. Cibacron blue 3GA (CB) was coupled to the particles to prepare a magnetic affinity support (MAS) for protein adsorption. Lysozyme was used as a model protein to test the adsorption properties of the MAS. The adsorption equilibrium of lysozyme to the MAS was described by the Langmuir-type isotherm. The capacity for lysozyme adsorption was more than 70 mg/g MAS (wet weight) at a relatively low CB coupling density (3-5 micromol/g). In addition, 1.0 M NaCl solution could be used to dissociate the adsorbed lysozyme. Finally, the MAS was recycled for the purification of alcohol dehydrogenase (ADH) from clarified yeast homogenates. Under proper conditions, the magnetic separation yielded over 5-fold purification of the enzyme with 60% recovery of the enzyme activity.     

Chitosan gel beads immobilized Cu (II) for selective adsorption of amino acids

Chitosan (CS) gel beads were prepared by using phase inversion and precipitation technique. The gel beads could bind copper (II), by which Cu (II) ion-immobilized chitosan gel beads (CS-Cu²⁺ gel beads) were prepared, and the amount of the immobilized Cu (II) was about 35 mg/g when the CS gel beads were incubated in 150 ppm cupric sulfate solution. The CS-Cu²⁺ gel beads could selectively adsorb histidine (His) from the mixed solution containing His and tryptophan (Trp); and the selective coefficient which was defined as the adsorbed amount ratio of His to Trp was about 8.0 at the pH value of 7.4. The effect of the pH value on the amino acid adsorption was also studied. In order to investigate the relationship of the amino acid adsorption and protein adsorption, the adsorbed amounts for IgG and albumin were determined; and the results indicated that the CS-Cu²⁺ gel beads could adsorb a larger amount of IgG than albumin due to the larger amount of the exposed residual His. The study provided a sorbent and a method to selectively remove His and IgG.     

An immobilized metal ion affinity adsorption and scintillation proximity assay for receptor-stimulated phosphoinositide hydrolysis

A novel approach to measuring receptor-stimulated phosphoinositide hydrolysis was developed based on the principles of immobilized metal ion affinity chromatography (IMAC) and scintillation proximity assay (SPA). Hard Lewis metal ions, such as Zr(4+), Ga(3+), Al(3+), Fe(3+), Lu(3+), and Sc(3+), were immobilized on SPA beads via metal chelate and utilized as affinity ligands to entrap inositol phosphates. [3H]Inositol phosphates bound to IMAC-SPA beads through the strong interaction of their phosphate group with the immobilized metal ions. The binding brought [3H]inositol phosphates in close proximity to the scintillant embedded in the SPA beads, thereby allowing the radioactivity to be quantified. Quantification of [3H]inositol phosphate production in cells preincubated with [3H]inositol provided a highly sensitive measurement of phosphoinositide hydrolysis. The utility of this approach was demonstrated in measuring the response mediated by the G-protein-coupled neurokinin NK1 receptor and the tyrosine kinase-linked platelet-derived growth factor (PDGF) receptor. Substance P stimulated phosphoinositide hydrolysis concentration-dependently in CHO cells expressing NK1 receptors with a maximal 12-fold increase in inositol phosphate production. Similarly, PDGF-BB stimulated a 5-fold increase in phosphoinositide hydrolysis in quiescent Swiss 3T3 cells. This new approach is highly sensitive, fast, simple, easily performed on 96-well plates, and amenable for high-throughput screening.     

Ironporphyrin immobilized onto montmorillonite as a biomimetical model for azo dye oxidation

In this work, we studied the oxidation of the azo dye Disperse Orange 3 (DO3) by hydrogen peroxide, catalyzed by 5,10,15,20-tetrakis(4-N-methylpyridyl)porphyrin iron(III) chloride immobilized onto montmorillonite K10, FeP-K10. Results showed that the FeP-K10/H₂O₂ system is efficient for discoloration of the DO3 dye, especially at pH 3.0. The catalyst was shown to be relatively stable and could be recycled many times, leading to good yields. DO3 oxidation products were analyzed by gas chromatography and mass spectrometry, being 4-nitroaniline the main product. Tert-butylhydroperoxide and iodosylbenzene were also used as oxidants, giving rise to 4-nitroaniline as product too. The studied system is a good biomimetic model of oxidative enzymes, being a promising discoloring agent for azo dyes.     

Characterization of sand as a support for immobilized enzymes.

The potential of sand as a support for immobilized enzymes was investigated by preparing alkylamine sand and devising methods to measure the total number of amine groups present and the fraction available for immobilization of enzymes. Alcohol dehydrogenase (alcohol: NAD oxidoreductase, EC 1.1.1.1.) and lactate dehydrogenase (L-lactate:NAD oxidoreductase, EC 1.1.1.27) were immobilized on alkylamine sand, and the stability of the immobilized protein and dehydrogenase activity was measured. Urease (urea amidohydrolase, EC 3.5.1.5) was also immobilized on sand to test the applicability of these methods to larger scale immobilizations. Results suggest that sand shows promise as a support for immobilized enzymes.     

LdARL-1 His-tagged recombinant protein: purification by immobilized metal affinity expanded bed adsorption

Previously we have cloned three ADP-ribosylation factor-like (ARL) genes from the parasitic protozoan Leishmania donovani: LdARL-3A and 3B, LdARL-1. LdARL-3A was previously purified as an active native form, which was able to bind GTP in vitro. In this paper, we have performed the production and the purification of Histidine-tagged (His-tagged) LdARL-1 recombinant protein by immobilized metal affinity chromatography (IMAC) using expanded bed adsorption (EBA) technology. This protein was purified with more than 95% purity and could be successfully used for GTP-binding assay.     

Optimization of adsorption conditions of papain on dye affinity membrane using response surface methodology

The adsorption of papain on Reactive Blue 4 dye–ligand affinity membrane was investigated in a batch system. The combined effects of operating parameters such as initial pH, temperature, and initial papain concentration on the adsorption were analyzed using response surface methodology. The optimum adsorption conditions were determined as initial pH 7.05, temperature 39 °C, and initial papain concentration 11.0 mg/ml. At optimum conditions, the adsorption capacity of dye–ligand affinity membrane for papain was found to be 27.85 mg/g after 120 min adsorption. The papain was purified 34.6-fold in a single step determined by fast protein liquid chromatography. More than 85% of the adsorbed papain was desorbed using 1.0 M NaCl at pH 9.0 as the elution agent. The purification process showed that the dye–ligand immobilized composite membrane gave good separation of papain from aqueous solution.     

An oriented adsorption strategy for efficient solid phase PEGylation of recombinant staphylokinase by immobilized metal-ion affinity chromatography

Conjugation of truncated recombinant staphylokinase (trSak) with polyethylene glycol (PEG) is an effective way to overcome its short plasma half-life and enhance its therapeutic potential. However, conventional amine directed PEGylation chemistry inevitably led to modification at its functionally important N terminus, which resulted in a significantly reduced bioactivity of trSak. In this study, a novel solid phase PEGylation process was developed to shield the N-terminal region of the protein from PEGylation. The process was achieved by oriented adsorption of an N-terminally His-tagged trSak (His-trSak) onto an immobilized metal-ion affinity chromatography (IMAC). His-trSak was efficiently separated and retained on IMAC media before reaction with succinimidyl carbonate mPEG (SC-mPEG, 5, 10 or 20 kDa). The IMAC derived mono-PEGylated His-trSak showed structural and stability properties similar to the liquid phase derived conjugate. However, isoelectric focusing electrophoresis analysis revealed that mono-PEGylated His-trSaks via solid phase PEGylation were more homogeneous than those from liquid phase PEGylation. Moreover, tryptic peptide mapping analysis suggested that a complete N-terminal blockage of IMAC bound His-trSak from PEGylation with 10 kDa- and 20 kDa-SC-mPEG. In contrast, only partial protection of the N-terminal region was obtained for 5 kDa-SC-mPEG. Bioactivities of 10 kDa- and 20 kDa-PEG-His-trSak conjugates without N-terminal PEGylation were significantly higher than those of randomly PEGylated products. This further demonstrated the advantage of our new on-column PEGylation strategy.     

Polymer versus monomer as displacer in immobilized metal affinity chromatography

Successful immobilized metal affinity chromatography (IMAC) of proteins on Cu²⁺-iminodiacetic acid Sepharose has been carried out in a displacement mode using a synthetic copolymer of vinyl imidazole and vinyl caprolactam [poly(VI-VCL)] as a displacer. Vinyl caprolactam renders the co-polymer with the thermosensitivity, e.g., property of the co-polymer to precipitate nearly quantitatively from aqueous solution on increase of the temperature to 48°C. A thermostable lactate dehydrogenase from the thermophilic bacterium Bacillus stearothermophilus modified with a (His)₆-tag [(His)₆-LDH] has been purified using an IMAC column. For the first time it was clearly demonstrated that a polymeric displacer [poly(VI-VCL)] was more efficient compared to a monomeric displacer (imidazole) of the same chemical nature, probably due to the multipoint interaction of imidazole groups within the same macromolecule with one Cu²⁺ ion. Complete elution of bound (His)₆-LDH has been achieved at 3.7 mM concentration of imidazole units of the co-polymer (5 mg/ml), while this concentration of free imidazole was sufficient to elute only weakly bound proteins. Complete elution of (His)₆-LDH by the free imidazole was achieved only at concentrations as high as 160 mM. Thus, it was clearly demonstrated, that the efficiency of low-molecular-mass displacer could be improved significantly by converting it into a polymeric displacer having interacting groups of the same chemical nature.     

Chitosan from Syncephalastrum racemosum used as a film support for lipase immobilization

Chitosan from a native Mucoralean strain, Syncephalastrum racemosum, isolated from herbivorous dung (Northeast-Brazil), was used as a film support for lipase immobilization. S. racemosum showed highest chitosan yield (152 mg g dry mycelia weight(-1); 15.2% of dry mycelia weight) among the nine strains screened, which presented 89% D-glucosamine. A chitosan film was used for lipase (EC 3.1.1.3) immobilization using glutaraldehyde as a bifunctional agent. The immobilized lipase retained 47% (12.6 micromol s(-1) m(-2)) of its initial catalytic activity after four cycles of reaction. This result is comparable (same order of magnitude) to that of the enzyme immobilized on film made from commercially available crustacean chitosan.     

Sodium alginate/Na(+)-rectorite composite microspheres: Preparation, characterization, and dye adsorption

Sodium alginate/Na(+)-rectorite (SA/Na(+)REC) intercalated nano-composite microspheres were prepared in an inverse suspension system. The effect of the preparation conditions of SA/Na(+)REC composite microspheres on adsorption capacity for Basic Blue 9 was investigated. The structure and morphology were analyzed by Fourier transform infrared spectroscopy (FTIR), X-ray diffraction (XRD) and scanning electron microscope (SEM). The results showed that the optimal condition was that the amount of Na(+)-rectorite was 2wt%, the amount of cross-linker was 0.384% and the amount of the initiator was 8%. SEM showed that it is porous products with spherical particulate surface. XRD showed that intercalation is formed between Na(+)-rectorite and sodium alginate. The adsorption capacity of SA/Na(+)REC was investigated in comparison with Na(+)-rectorite and sodium alginate using different cationic dyes. The SA/Na(+)REC composite microspheres showed the highest adsorption capacity. The reason lies in the existence of intercalated sodium alginate. It could enlarge the pore structure of microspheres, facilitating the penetration of macromolecular dyes.     

The preparation and properties of hornblende as a support for immobilized invertase

The suitability of hornblende as a support for immobilized β-fructofuranosidase (invertase) was studied, with regard to the physical stability of the support and the thermal and operational stability of the immobilized enzyme. Hornblende was more stable than Enzacryl-Alo or Enzacryl-TIO, and marginally more stable than porous glass. Invertase immobilized on hornblende was more stable during long-term operation than invertase immobilized on porous glass. An active preparation of immobilized invertase was obtained also on pyroxene particles.     

Use of chemically modified activated carbon as a support for immobilized enzymes

Loading and activity assays of the enzymes alpha-chymotrypsin, alpha-chymotrypsinogen, and glucose oxidase covalently bound to an activated carbon support are presented. The activated carbon support material was pretreated using either a radio-frequency oxygen plasma or an electrochemical oxidation to maximize the enzyme attachment. Cyanuric chloride or water-soluble carbodiimide linking reactions were used to covalently attach the enzymes to the carbon support. Discussion of the relative merits of each reaction scheme is presented.     

Recycling of textile bleaching effluents for dyeing using immobilized catalase

Catalase was immobilized on alumina carrier and crosslinked with glutaraldehyde. Storing stability, temperature and pH profiles of enzyme activity were studied in a column reactor with recirculation and in a batch stirred-tank reactor. The immobilized enzyme retained 44% of its activity at pH 11, 30 °C and 90% at 80 °C, pH 7. The half-life time of the immobilized catalase was increased to 2 h at pH 12, and 60 °C. Acceptable results were achieved when the residual water from the washing process of H₂O₂-bleached fabrics was treated with the immobilized enzyme and then reused for dyeing.     

Protein A immobilized affinity cartridge for immunoglobulin purification

Recombinant Protein A was immobilized on a cellulose and acrylic composite matrix through Schiff base formation. Various factors that could affect the binding of immunoglobulin by the Protein A molecules immobilized on the solid matrix were studied to achieve optimum affinity purification. The spacer arm length and ligand concentration of Protein A were verified as factors crucial to optimized IgG purification. Liquid-phase environmental conditions such as pH and salt concentration also play important roles in adsorption capacity by affecting the molecular interaction between IgG and the immobilized Protein A. The rate of interaction between Protein A and IgG is rather fast, with minimal differences observed at 10-fold increases in the cartridge loading rate. This paper describes a cellulose/acrylic composite matrix for immobilizing Protein A, at an optimized ligand concentration, installed on a spacer arm of adequate length, to purify immunoglobulins from animal plasma. The fast-flow property of the cartridge made from such a matrix and its simplicity in operation provide effective means for purifying immunoglobulins on a relatively large scale.