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Cesar Mateo

Publications and source records attributed to Cesar Mateo.

42 records · Page 3Linked to original sources

A simple strategy for the purification of large thermophilic proteins overexpressed in mesophilic microorganisms: application to multimeric enzymes from Thermus sp. strain T2 expressed in Escherichia coli.

The heating of protein preparations of mesophilic organism (e.g., E. coli) produces the obliteration of all soluble multimeric proteins from this organism. In this way, if a multimeric enzyme from a thermophilic microorganism is expressed in these mesophilic hosts, the only large protein remaining soluble in the preparation after heating is the thermophilic enzyme. These large proteins may be then selectively adsorbed on lowly activated anionic exchangers, enabling their full purification in just these two simple steps. This strategy has been applied to the purification of an alpha-galactosidase and a beta-galactosidase from Thermus sp. strain T2, both expressed in E. coli, achieving the almost full purification of both enzymes in only these two simple steps. This very simple strategy seems to be of general applicability to the purification of any thermophilic multimeric enzyme expressed in a mesophilic host.

Anion Exchange Resins↗

Purification of a catalase from Thermus thermophilus via IMAC chromatography: effect of the support.

A hexameric Mn-catalase was purified from crude extracts of Thermus thermophilus using ammonium sulfate precipitation and ion metal-chelate affinity chromatography (IMAC). Eupergit 250 and Sepabeads FP-EP3 epoxy supports derivatized with iminodiacetic acid (IDA) and copper were used, at similar micromole/packed milliliter of support. Although Eupergit 250-IDA-Cu support adsorbed 80% of the total proteins in the extract, it exhibited a minimum affinity for the catalase. On the other hand, Sepabeads FP-EP3-IDA-Cu allowed the full adsorption of the catalase activity, which could be desorbed in fractions of different purity. This was attributed to a different geometrical congruence of the support surfaces with the enzyme surface, resulting in a different ability to form multipoint interactions with the proteins. Thus, by a cleanup step, followed by a negative chromatographic step using Eupergit 250-IDA-Cu2+ and by the adsorption of the catalase on Sepabeads-IDA-Cu2+ support, a pure enzyme fraction was obtained and its N-terminal end was sequenced.

Adsorption↗

Reversible immobilization of glucoamylase by ionic adsorption on sepabeads coated with polyethyleneimine.

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., 1 M NaCl at pH 5.5). Thermal stability and optimal temperature was marginally improved by this immobilization. Recovered activity depended on the substrate used, maltose or starch, except when very low loading was used. The optimization of the loading allowed the preparation of derivatives with 750 IU/g in the hydrolysis of starch, preserving a high percentage of immobilized activity (around 50%).

Adsorption↗

Reversible and strong immobilization of proteins by ionic exchange on supports coated with sulfate-dextran.

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. This interaction was stronger than that using conventional carboxymethyl cellulose (CMC) and even others such as supports coated with aspartic-dextran polymer. By means of the sequential use of the new supports and supports coated with polyethyleneimine (PEI), all proteins from crude extracts could be immobilized. In fact, a large percentage (over 50%) could be immobilized on both supports. Finally, some industrially relevant enzymes (beta-galactosidases from Aspergillus oryzae, Kluyveromyces lactis, and Thermussp. strain T2, lipases from Candida antarctica A and B, Candida rugosa, Rhizomucor miehei, and Rhyzopus oryzae and bovine pancreas trypsin and chymotrypsin) have been immobilized on these supports with very high activity recoveries and immobilization rates. After enzyme inactivation, the protein could be fully desorbed from the support, and then the support could be reused for several cycles. Moreover, in some instances the enzyme stability was significantly improved, mainly in the presence of organic solvents, perhaps as a consequence of the highly hydrophilic microenvironment of the support.

Adsorption↗

Simple purification of immunoglobulins from whey proteins concentrate.

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. Full desoprtion of the other serum proteins could be achieved without contamination with BSA. Thus, a protein solution containing only Ig and very small proteins (e.g., beta-lactoglobulins and alpha-lactalbumin) was obtained. Offering this protein mixture to a lowly activated aminated support, only Ig adsorbed on the support. It has been shown that BSA is able to interact with other proteins (including Ig and lactalbumins). This ability to form complexes with other proteins prevented the success of the direct adsorption of Ig on this mildly activated support, even although Ig should be the largest protein presented in dairy whey.

Adsorption↗

Immobilization and stabilization of a cyclodextrin glycosyltransferase by covalent attachment on highly activated glyoxyl-agarose supports.

Covalent immobilization of cyclodextrin glycosyltransferase on glyoxyl-agarose beads promotes a very high stabilization of the enzyme against any distorting agent (temperature, pH, organic solvents). For example, the optimized immobilized preparation preserves 90% of initial activity when incubated for 22 h in 30% ethanol at pH 7 and 40 degrees C. Other immobilized preparations (obtained via other immobilization protocols) exhibit less than 10% of activity after incubation under similar conditions. Optimized glyoxyl-agarose immobilized preparation expressed a high percentage of catalytic activity (70%). Immobilization using any technique prevents enzyme inactivation by air bubbles during strong stirring of the enzyme. Stabilization of the enzyme immobilized on glyoxyl-agarose is higher when using the highest activation degree (75 micromol of glyoxyl per milliliter of support) as well as when performing long enzyme-support incubation times (4 h) at room temperature. Multipoint covalent immobilization seems to be responsible for this very high stabilization associated to the immobilization process on highly activated glyoxyl-agarose. The stabilization of the enzyme against the inactivation by ethanol seems to be interesting to improve cyclodextrin production: ethanol strongly inhibits the enzymatic degradation of cyclodextrin while hardly affecting the cyclodextrin production rate of the immobilized-stabilized preparation.

Enzymes, Immobilized↗