Multi-Point Covalent Immobilization of Enzymes on Supports Activated with Epoxy Groups: Stabilization of Industrial Enzymes.

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. (2) There is an "intermolecular" covalent reaction between the adsorbed protein and the supports. (3) The immobilized protein is incubated at alkaline pH to increase the multipoint covalent attachment, thereby stabilizing the enzyme. (4) The hydrophobic surface of the support is hydrophylized by reaction of the remaining groups with amino acids in order to reduce the unfavorable enzyme-support hydrophobic interactions. This strategy has produced a significant increase in the stability of penicillin G acylase compared with the stability achieved using conventional protocols.

Very Strong but Reversible Immobilization of Enzymes on Supports Coated with Ionic Polymers.

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. The polymer is completely coated, via covalent immobilization, the surface of different porous supports. Proteins can interact with this polymeric bed, involving a large percentage of the protein surface in the adsorption. Different enzymes have been very strongly adsorbed on these supports, retaining enzyme activities. On the other hand, adsorption is very strong and the derivatives may be used under a wide range of pH and ionic strengths. These supports may be useful even to stabilize multimeric enzymes, by involving several enzyme subunits in the immobilization.

Stabilization of Multimeric Enzymes via Immobilization and Further Cross-Linking with Aldehyde-Dextran.

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. Additional cross-linking with polyfunctional macromolecules promotes the complete cross-linking of the subunits to fully prevent enzyme dissociation. Full stabilization of multimeric structures has been physically shown because no subunits were desorbed from derivatives after boiling them in SDS. As a functional improvement, these immobilized preparations no longer depend on the enzyme.

Mixed ion exchange supports as useful ion exchangers for protein purification: purification of penicillin G acylase from Escherichia coli.

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. The use of divalent cations reinforced the adsorption of proteins on these supports. These results suggest that the adsorption of proteins on supports bearing almost neutral charge is not driven by the existence of opposite charges between the adsorbent and the biomacromolecule but just by the possibility of forming a high number of enzyme-support ionic bonds. This support has been used to purify the enzyme penicillin G acylase (PGA) from Escherichia coli. PGA was not significantly adsorbed at any pH value on either amino- or carboxyl-activated supports, while it can be fully adsorbed at pH 5 on this new carboxyl-amino matrix. Thus, we have been able to almost fully purify PGA from crude extracts with a very high yield by using these new supports.

Solid phase proteomics: dramatic reinforcement of very weak protein-protein interactions.

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. The size of the aggregates may be defined by controlling the concentration of ionised groups on the support: the less activated the supports are, the bigger the complexes. In this way, solid-phase proteomics could be a very interesting tool to detect weak protein-protein interactions.

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.

Purification, stabilization, and concentration of very weak protein-protein complexes: Shifting the association equilibrium via complex selective adsorption on lowly activated supports.

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. This selective adsorption of the associated proteins shifted the association equilibrium of the soluble proteins toward the associated form. Thus, in the presence of 15% v/v dioxane, a concentration that is able to almost fully break the immunocomplex (less that 3% of the immunocomplex appeared associated when soluble antigen-antibody mixture was cross-linked with aldehyde-dextran), we can obtain more than 90% of the fully pure immunocomplex from the non-associated protein, adsorbed on anionic exchanger supports having a very low activation. This simple strategy may be a very useful tool to solve one of the most relevant challenges in the modern proteomics, the detection of very weak protein-protein interactions.

Selective and mild adsorption of large proteins on lowly activated immobilized metal ion affinity chromatography matrices. Purification of multimeric thermophilic enzymes overexpressed in Escherichia coli.

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 0.25 micromol of metallic groups/g of support. Then, these lowly activated supports have been used for purifying multimeric enzymes from thermophilic organisms (alpha- and beta-galactosidases from Thermus sp. strain T2) cloned and over-expressed in mesophilic ones. A previous heating step of the crude extract destroyed the quaternary structure of all multimeric enzymes from the host (E. coli). Thus, the only large protein remaining in the supernatant of this heated extract are the cloned multimeric thermophilic enzymes, permitting their very simple purification by using only one chromatographic step.

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.

Immobilization of rennet from Mucor miehei via its sugar chain. Its use in milk coagulation.

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.TFA (98%)) and macromolecular substrates (k-casein) (78%). The use of tailor-made aminated support was critical to obtain good stability values, because using fully aminated supports achieved much lower thermostability values than using 50% aminated supports. The optimized derivative was utilized to hydrolyze casein in milk. To prevent the coagulation of the milk in the presence of the derivative, the reaction was performed at 4 degrees C (where hydrolyzed casein did not precipitate). Then the hydrolyzed milk was filtered and latter on heated to 30 degrees C, achieving a similar aggregate to the one achieved with soluble rennet.

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.

Immobilization of lactase from Kluyveromyces lactis greatly reduces the inhibition promoted by glucose. full hydrolysis of lactose in milk.

The kinetic constants (Km, Vmax, and inhibition constants for the different products) of soluble and different immobilized preparations of beta-galactosidase from Kluyveromyces lactis were determined. For the soluble enzyme, the Km was 3.6 mM, while the competitive inhibition constant by galactose was 45 mM and the noncompetitive one by glucose was 758 mM. The immobilized preparations conserved similar values of Km and competitive inhibition, but in some instances much higher values for the noncompetitive inhibition constants were obtained. Thus, when glyoxyl or glutaraldehyde supports were used to immobilize the enzyme, the noncompetitive inhibition was greatly reduced (Ki approximately 15,000 and >40,000 mM, respectively), whereas when using sugar chains to immobilize the enzyme the behavior had an effect very similar to the soluble enzyme. These results presented a great practical relevance. While using the soluble enzyme or the enzyme immobilized via the sugar chain as biocatalysts in the hydrolysis of lactose in milk only around 90% of the substrate was hydrolyzed, by using of these the enzyme immobilized via the glyoxyl or the glutaraldehyde groups, more than 99% of the lactose in milk was hydrolyzed.

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%).

Encapsulation of crosslinked penicillin G acylase aggregates in lentikats: evaluation of a novel biocatalyst in organic media.

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. This could be related to the highly hydrophilic environment inside the LentiKats biocatalysts: Partition experiments showed that the concentration of dioxane inside LentiKats was lower than in the reaction medium. In fact, thermal stability was about the same as in the corresponding CLEA. This permitted great improvement in the reaction rate for thermodynamically controlled synthesis of a model antibiotic (using phenylacetic acid and 7-amino-deacetoxycefalosporanic acid). Even more importantly, yields could be improved by using LentiKats-encapsulated CLEA, very likely by a favorable product/substrate partition. Thus, this very simple technique not only provides an efficient technique for solving the mechanical stability problem associated with CLEA, but also greatly improves the behavior of CLEA in organic media.

Cross-linked aggregates of multimeric enzymes: a simple and efficient methodology to stabilize their quaternary structure.

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. More interestingly, the enzyme stability, which in its soluble form strongly depends on the enzyme concentration, becomes fully independent of this parameter. This permitted the enzyme stability to greatly increase under diluted conditions. In fact, diluted CLEAs presented a higher stability than those of their glyoxyl derivatives counterparts, which were unable to fully stabilize the multimeric structure of these tetrameric enzymes

Co-aggregation of penicillin g acylase and polyionic polymers: an easy methodology to prepare enzyme biocatalysts stable in organic media.

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. Experiments show that CLEA-GDPs have a highly increased stability in organic media. The average half-life of the preparations was much higher than standard CLEA without a microenvironment (CLEA-G), (e.g., more than 25-fold) in the presence of dioxane. However, their thermal stability was not increased, which leads to the conclusion that the stability of CLEA-GDPs in organic media is due to the hydrophilic microenvironment that surrounds the protein enzyme more than to a conformational stiffening effect. This is further supported by solvation experiments that show a preferential hydration of CLEA when polymers are used to coat the enzyme. CLEA-GDPs are clearly better than other biocatalysts in terms of solvent stability.

Ion exchange using poorly activated supports, an easy way for purification of large proteins.

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. These kinds of proteins have large surfaces to interact by many points with the support. Therefore, it was possible to purify large proteins as beta-galactosidase from Thermus sp. strain T2 from a crude extract from Escherichia coli or bovine liver catalase from a commercial preparation, with tailor-made ion-exchanger supports. A simple step of adsorption/desorption on lowly activated supports rendered both enzymes rather pure as confirmed by sodium dodecyl sulphate-polyacrylamide gel electrophoresis. Moreover, this strategy makes also easy the desorption step that requires rather low NaCl concentrations, which may become a serious problem for desorption of large proteins when using conventional supports, due to their ability of generating a very strong adsorption.

New cationic exchanger support for reversible immobilization of proteins.

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). More than 80% of the proteins contained in crude extracts from Escherichia coli and Acetobacter turbidans have been strongly adsorbed on these porous materials at pH 5. This interaction was stronger than in conventional carboxymethyl cellulose (e.g., at pH 7 and 25 degrees C, all proteins previously adsorbed at pH 5 were released from carboxymethyl cellulose, whereas no protein was released from the new supports under similar conditions). Ionic exchange properties of such composites were strongly dependent on the size of the aspartic-dextran polymers as well as on the exact conditions of the covalent coating of the solids with the polymer (optimal conditions: 100 mg aspartic-dextran 20 000/(mL of support); room temperature). Finally, some industrially relevant enzymes (Kluyveromices lactis, Aspergillus oryzae, and Thermus sp. beta-galactosidases, Candida antarctica B lipase, and bovine pancreas trypsin and chymotrypsin) have been immobilized on these supports with very high activity recovery and immobilization rates. After enzyme inactivation, the enzyme can be fully desorbed from the support and the support could be reused for several cycles.

Stabilization of a multimeric beta-galactosidase from Thermus sp. strain T2 by immobilization on novel heterofunctional epoxy supports plus aldehyde-dextran cross-linking.

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. Immobilization yields depended on the support, ranging from 95% using Sepabeads-epoxy-chelate, Sepabeads-epoxy-amino, or Sepabeads-epoxy-boronic to 5% using Sepabeads-epoxy-IDA. Moreover, immobilization rates were also very different when using different supports. Remarkably, the immobilized beta-galactosidase derivatives showed very improved but different stabilities after favoring multipoint covalent attachment by long-term alkaline incubation, the enzyme immobilized on Sepabeads-epoxy-boronic being the most stable. This derivative had some subunits of the enzyme not covalently attached to the support (detected by SDS-PAGE). This is a problem if the biocatalysts were to be used in food technology. The optimization of the cross-linking with aldehyde-dextran permitted the full stabilization of the quaternary structure of the enzyme. The optimal derivative was very active in lactose hydrolysis even at 70 degrees C (over 1000 IU/g), maintaining its activity after long incubation times under these conditions and with no risk of product contamination with enzyme subunits.

Detection and purification of two antibody-antigen complexes via selective adsorption on lowly activated anion exchangers.

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. Here, by selecting the support with the highest activation degree that was unable to adsorb the non-associated proteins, we have shown the simple and selective adsorption of immuno complexes (as a model), while antibodies and antigens remained in the supernatant. Therefore, it was possible to selectively adsorb on lowly activated supports (e.g., agarose 4BCL having only 1 micromol of amino groups per g of support) rabbit IgG/anti-rabbit immunoglobulins (immuno complex), while these supports were unable to adsorb the individual immunoglobulines. Similarly, horseradish peroxidase (HRP)/anti-HRP were selectively adsorbed on lowly activated supports, while the individual proteins were not adsorbed at all. Afterwards, the adsorbed associated proteins (purified at least from the non-associated counterparts and concentrated by the adsorption on the support) may be cross-linked with aldehyde-dextran and be desorbed from the matrix for their analysis. This strategy may permit very simple experiments to detect the presence of protein-protein complexes. Finally, we have shown the advantages of this technique compared to the use of one of the proteins previous immobilized on a support.