Publications by authors named "Benevides C C Pessela"

Subunit dissociation of multimeric proteins is one of the most important causes of inactivation of proteins having quaternary structure, making these proteins very unstable under diluted conditions. A sequential two-step protocol for the stabilization of this protein is proposed. A multisubunit covalent immobilization may be achieved by performing very long immobilization processes between multimeric enzymes and porous supports composed of large internal surfaces and covered by a very dense layer of reactive groups.

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In this chapter, the properties of tailor-made anionic exchanger resins based on films of large polyethylenimine polymers (e.g., molecular weight 25,000) as supports for strong but reversible immobilization of proteins are shown.

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Commercial epoxy supports may be very useful tools to stabilize proteins via multipoint covalent attachment if the immobilization is properly designed. In this chapter, a protocol to take full advantage of the support's possibilities is described. The basics of the protocol are as follows: (1) the enzymes are hydrophobically adsorbed on the supports at high ionic strength.

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A support having similar amounts of carboxymethyl and amino groups has been prepared and evaluated as an ion exchanger. It has been found that this support was able to adsorb a high amount of protein from a crude extract of proteins (approximately 55%) at pH 5. Moreover, it was able to adsorb approximately 60% of the protein that did not become adsorbed on supports bearing just one kind of ionic groups.

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Very weak protein-protein interactions may play a critical role in cell physiology but they are not easily detectable in "in vitro" experiments. To detect these weak interactions, we have developed a strategy that included: (a) design of a rapid and very effective crosslinking of protein-protein complexes with poly-functional reagents; (b) selective adsorption of very large proteins on lowly activated ionic exchangers, based on the need of a multipoint physical adsorption to incorporate the proteins into the matrix; (c) purification by selective adsorption of protein-protein complexes formed by strong protein-protein interactions, via selective adsorption of the complexes on lowly activated ionic exchangers via multi-protein physical adsorption and leaving the non-associated proteins in the solution; (d) reinforcement of very weak protein-protein interactions by selective adsorption of the complex on lowly activated ionic exchange supports via a synergetic cooperation of the weak protein-protein interaction plus the interactions of both proteins with the support enabling the almost full shifting of the equilibrium towards the association position; (e) control of the aggregation state of proteins like BSA, formed by weak protein-protein interactions. In this last case, it seems that the interaction of the protein molecules placed on the borders of the aggregate with the groups on the support partially stabilizes the whole aggregate, although, some molecules of the aggregate cannot interact with the support.

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We have developed a new protocol with only two steps for purification of immunoglobulins (Ig) from a protein concentrate of whey. Following this protocol, we have an 80% recovery of immunoglobulins, fairly pure. The purification was achieved by eliminating the BSA, via a strong adsorption on DEAE-agarose.

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Very weak protein-protein interactions are very difficult to detect because these complexes could be under the detection limit or they tend to dissociate. Here, using as a model the antibody-antigen interaction weaken by the presence of dioxane, we have shown a strategy for the protein complexes purification by selective adsorption of the associated proteins. This strategy is based on the use of poorly activated anionic exchanger supports to selectively adsorb large complexes.

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Taken advantage of the mechanism of adsorption of macro-molecules on ionic exchangers, (a multipoint interaction between the protein and the support), it is possible to selectively adsorb large proteins leaving small ones in the supernatant. Associated proteins should present a significant difference in its size as compared to the non-associated forms. Thus, the protein complexes may have much larger surfaces to interact with the support.

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A strategy to selectively adsorb large proteins on immobilized metal ion affinity chromatography supports is presented. It is based on the fact that large proteins have a large surface that permits the long distance interaction with groups placed quite far apart (very dispersed onto the support surface) in the support, therefore, even using lowly activated supports, these proteins may be able to yield multiple interactions with the support, which is not possible for smaller proteins. This has been shown using a crude extract from Escherichia coli, where only large proteins were adsorbed on supports having 0.

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A successful strategy for the immobilization of rennet from Mucor miehei has been developed. The strategy is based on the immobilization of the enzyme, via their sugar chains at high ionic strength on aminated supports having primary amino groups with a very low pK value. The rennet was covalently immobilized via sugar chains (previously oxidized with periodate), which act as natural spacer arms and allow a very high percentage of rennet activity to be kept against small (H-Leu-Ser-p-nitro-Phe-Nle-Ala-Leu-OMe.

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Glucoamylase (GA) from Aspergillus niger was immobilized via ionic adsorption onto DEAE-agarose, Q1A-Sepabeads, and Sepabeads EC-EP3 supports coated with polyethyleneimine (PEI). After optimization of the immobilization conditions (pH, polymer size), it was observed that the adsorption strength was much higher in PEI-Sepabeads than in Q1A-Sepabeads or DEAE-supports, requiring very high ionic strength to remove glucoamylase from the PEI-supports (e.g.

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Article Synopsis
  • The study measured kinetic constants (Km, Vmax, and inhibition constants) for both soluble and immobilized forms of beta-galactosidase from Kluyveromyces lactis.
  • The soluble enzyme had a Km of 3.6 mM, with competitive inhibition by galactose at 45 mM and noncompetitive inhibition by glucose at 758 mM, while immobilized versions showed similar Km values but significantly reduced noncompetitive inhibition constants when glyoxyl or glutaraldehyde were used.
  • The immobilized enzymes with glyoxyl or glutaraldehyde supports achieved over 99% hydrolysis of lactose in milk, greatly outperforming the soluble enzyme and those immobilized via sugar chains, which only managed
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New and strong ionic exchange resins have been prepared by the simple and rapid ionic adsorption of anionic polymers (sulfate-dextran) on porous supports activated with the opposite ionic group (DEAE/MANAE). Ionic exchange properties of such composites were strongly dependent on the size of the ionic polymers as well as on the conditions of the ionic coating of the solids with the ionic polymers (optimal conditions were 400 mg of sulfate-dextran 5000 kDa per gram of support). Around 80% of the proteins contained in crude extracts from Escherichia coli and Acetobacter turbidans could be adsorbed on these porous composites even at pH 7.

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A novel type of biocatalyst that combines the good properties of cross-linked enzyme aggregates (CLEAs) and hydrophilic microenvironments has been developed. Dextran sulfate- and polyethyleneimine-coated CLEAs of penicillin acylase (CLEA-GDP) were prepared by adding the polymers of different sizes before the precipitation stage of the enzyme. This study presents the development and optimization of a protocol to produce such a biocatalyst using penicillin acylase as a model.

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In this manuscript, we show that the immobilization of proteins following the technique of cross-linked protein aggregates (CLEAS) may permit the stabilization of the most complex multimeric enzymes by preventing their dissociation. To illustrate that, we have first prepared CLEAS with two tetrameric catalases. Activity recovery was over 40%, and no protein subunit could be desorbed from the CLEAS after boiling in SDS.

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The encapsulation of crosslinked enzyme aggregates (CLEA) of penicillin G acylase into a very rigid polymeric matrix based on polyvinyl alcohol (LentiKats) has been used successfully to improve the inadequate mechanical properties of CLEA. This encapsulation decreased CLEA activity by only around 40%. As compensation, a significant improvement in the stability of the CLEA in the presence of organic solvents was detected.

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Ion-exchange chromatography using commercial ionic supports is a commonly used technique for protein purification. However, selective adsorption of a target protein from a given extract onto commercial ion exchangers seems to be quite complex since they are designed to adsorb the maximum percentage of proteins with the opposite charge. In this paper, ion-exchanger supports with different activation degrees (from 1 to 40 micromol of amino groups per g of agarose) have been prepared and used for the purification of large proteins.

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This work exemplifies the advantages of using a battery of new heterofunctional epoxy supports to immobilize enzymes. We have compared the performance of a standard Sepabeads-epoxy support with other Sepabeads-epoxy supports partially modified with boronate, iminodiacetic, metal chelates, and ethylenediamine in the immobilization of the thermostable beta-galactosidase from Thermus sp. strain T2 as a model system.

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New tailor-made cationic exchange resins have been prepared by covalently binding aspartic-dextran polymers (e.g. MW 15 000-20 000) to porous supports (aminated agarose and Sepabeads).

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The properties of a new commercially available amino-epoxy support (amino-epoxy-Sepabeads) for immobilizing enzymes have been compared to those of conventional epoxy supports. The new support has a layer of epoxy groups over a layer of ethylenediamine that is covalently bound to the support. Thus, this support has a great anionic exchanger power and a high number of epoxy groups.

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A novel thermostable chimeric beta-galactosidase was constructed by fusing a poly-His tag to the N-terminal region of the beta-galactosidase from Thermus sp. strain T2 to facilitate its overexpression in Escherichia coli and its purification by immobilized metal-ion affinity chromatography (IMAC). The poly-His tag fusion did not affect the activation, kinetic parameters, and stability of the beta-galactosidase.

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Using the poly-His-tagged-beta-galactosidase from Thermus sp. strain T2 overexpressed in Escherichia coli (MC1116) as a model enzyme, we have developed a strategy to purify and immobilize proteins in a single step, combining the excellent properties of epoxy groups for enzyme immobilization with the good performance of immobilized metal-chelate affinity chromatography for protein purification. The aforementioned enzyme could not be immobilized onto standard epoxy supports with good yields, and after purification and storage, it exhibited a strong trend to yield very large aggregates as shown by ultracentrifugation experiments.

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