Use of enzymes in the production of semi-synthetic penicillins and cephalosporins: drawbacks and perspectives

Semi-synthetic β-lactamic antibiotics are the most used anti-bacteria agents, produced in hundreds tons/year scale. It may be assumed that this situation will even increase during the next years, with new β-lactamic antibiotics under development. They are usually produced by the hydrolysis of natural antibiotics (penicillin G or cephalosporin C) and the further amidation of natural or modified antibiotic nuclei with different carboxylic acyl donor chains. Due to the contaminant reagents used in conventional chemical route, as well as the high energetic consumption, biocatalytic approaches have been studied for both steps in the production of these very interesting medicaments during the last decades. Recent successes in some of these methodologies may produce some significant advances in the antibiotics industry. In fact, the hydrolysis of penicillin G to produce 6-APA catalyzed by penicillin G acylase is one of the most successful historical examples of the enzymatic biocatalysis, and much effort has been devoted to find enzymatic routes to hydrolyze cephalosporin C. Initially this could be accomplished in a quite complex system, using a two enzyme system (D-amino acid oxidase plus glutaryl acylase), but very recently an efficient cephalosporin acylase has been designed by genetic tools. Other strategies, including metabolic engineering to produce other antibiotic nuclei, have been also reported. Regarding the amidation step, much effort has been devoted to the improvement of penicillin acylases for these reactions since 1960. New reaction strategies, continuous product extraction or new penicillin acylases with better properties have proven to be the key to have competitive biocatalytic processes. In this review, a critical discussion of these very interesting advances in the application of enzymes for the industrial synthesis of semi-synthetic antibiotics will be presented.

Affinity chromatography of polyhistidine tagged enzymes. New dextran-coated immobilized metal ion affinity chromatography matrices for prevention of undesired multipoint adsorptions

New immobilized metal ion affinity chromatography (IMAC) matrices containing a high concentration of metal-chelate moieties and completely coated with inert flexible and hydrophilic dextrans are here proposed to improve the purification of polyhistidine (poly-His) tagged proteins. The purification of an interesting recombinant multimeric enzyme (a thermoresistant beta-galactosidase from Thermus sp. strain T2) has been used to check the performance of these new chromatographic media. IMAC supports with a high concentration (and surface density) of metal chelate groups promote a rapid adsorption of poly-His tagged proteins during IMAC. However, these supports also favor the promotion of undesirable multi-punctual adsorptions and problems may arise for the simple and effective purification of poly-His tagged proteins: (a) more than 30% of the natural proteins contained in crude extracts from E. coli become adsorbed, in addition to our target recombinant protein, on these IMAC supports via multipoint weak adsorptions; (b) the multimeric poly-His tagged enzyme may become adsorbed via several poly-His tags belonging to different subunits. In this way, desorption of the pure enzyme from the support may become quite difficult (e.g., it is not fully desorbed from the support even using 200 mM of imidazole). The coating of these IMAC supports with dextrans greatly reduces these undesired multi-point adsorptions: (i) less than 2% of natural proteins contained in crude extracts are now adsorbed on these novel supports; and (ii) the target multimeric enzyme may be fully desorbed from the support using 60 mM imidazole. In spite of this dramatic reduction of multi-point interactions, this dextran coating hardly affects the rate of the one-point adsorption of poly-His tagged proteins (80% of the rate of adsorption compared to uncoated supports). Therefore, this dextran coating of chromatographic matrices seems to allow the formation of strong one-point adsorptions that involve small areas of the protein and support surface. However, the dextran coating seems to have dramatic effects for the prevention of weak or strong multipoint interactions that should involve a high geometrical congruence between the enzyme and the support surface.

A kinetic study of synthesis of amoxicillin using penicillin G acylase immobilized on agarose

We present a kinetic model for the synthesis of amoxicillin from p-hydroxyphenylglycine methyl ester and 6-aminopenicillanic acid, catalyzed by penicillin G acylase immobilized on agarose, at 25 degrees C. Michaelis-Menten kinetic parameters (with and without inhibition) were obtained from initial velocity data (pH 7.5 and 6.5). Amoxicillin synthesis reactions were used to validate the kinetic model after checking mass transport effects. A reasonable representation of this system was achieved under some operational conditions, but the model failed under others. Nevertheless, it will be useful whenever a simplified model is required, e.g., in model-based control algorithms for the enzymatic reactor.

Immobilization of functionally unstable catechol-2,3-dioxygenase greatly improves operational stability

Thermophilic catechol 2,3-dioxygenase (EC 1.13.11.2) from Bacillus stearothermophilus has been immobilized on highly activated glyoxyl agarose beads. The enzyme could be fully immobilized at 4 degrees C and pH 10.05 with a high retention of activity (around 80%). Enzyme immobilized under these conditions showed little increase in thermostability compared with the soluble enzyme, but further incubation of immobilized enzyme at 25 degrees C and pH 10.05 for 3 h before borohydride reduction resulted in conjugates exhibiting a 100-fold increase in stability (c.f. the free enzyme). The stability of catechol 2,3-dioxygenase immobilized under these conditions was essentially independent of protein concentration whereas free enzyme was rapidly inactivated at low protein concentrations. An apparent stabilization factor of over 700-fold was recorded in the comparison of free and immobilized catechol 2,3-dioxygenases at protein concentrations of 10 µg/ml. Immobilization increased the 'optimum temperature' for activity by 20 degrees C, retained activity at substrate concentrations where the soluble enzyme was fully inactivated and enhanced the resistance to inactivation during catalysis. These results suggest that the immobilization of the enzyme under controlled conditions with the generation of multiple covalent links between the enzyme and matrix both stabilized the quaternary structure of the protein and increased the rigidity of the subunit structures.

Reversible enzyme immobilization via a very strong and nondistorting ionic adsorption on support-polyethylenimine composites

New tailor-made anionic exchange resins have been prepared, based on films of large polyethylenimine polymers (e.g., MW 25,000) completely coating, via covalent immobilization, the surface of different porous supports (agarose, silica, polymeric resins). Most proteins contained in crude extracts from different sources have been very strongly adsorbed on them. Ionic exchange properties of such composites strongly depend on the size of polyethylenimine polymers as well as on the exact conditions of the covalent coating of the solids with the polymer. On the contrary, similar coating protocols yield similar matrices by using different porous supports as starting material. For example, 77% of all proteins contained in crude extracts from Escherichia coli were adsorbed, at low ionic strength, on the best matrices, and less than 15% of the adsorbed proteins were eluted from the support in the presence of 0.3 M NaCl. Under these conditions, 100% of the adsorbed proteins were eluted from conventional DEAE supports. Such polyethylenimine-support composites were also very suitable to perform very strong and nondistorting reversible immobilization of industrial enzymes. For example, lipase from Candida rugosa (CRL), beta-galactosidase from Aspergillus oryzae and D-amino acid oxidase (DAAO) from Rhodotorula gracilis, were adsorbed on such matrices in a few minutes at pH 7.0 and 4 degrees C. Immobilized enzymes preserved 100% of catalytic activity and remained fully immobilized in 0.2 M NaCl. In addition to that, CRL and DAAO were highly stabilized upon immobilization. Stabilization of DAAO, a dimeric enzyme, seems to be due to the involvement of both enzyme subunits in the ionic adsorption.

Increase in conformational stability of enzymes immobilized on epoxy-activated supports by favoring additional multipoint covalent attachment*

Epoxy supports (Eupergit C) may be very suitable to achieve the multipoint covalent attachment of proteins and enzymes, therefore, to stabilize their three-dimensional structure. To achieve a significant multipoint covalent attachment, the control of the experimental conditions was found to be critical. A three-step immobilization/stabilization procedure is here proposed: 1) the enzyme is firstly covalently immobilized under very mild experimental conditions (e.g. pH 7.0 and 20 degrees C); 2) the already immobilized enzyme is further incubated under more drastic conditions (higher pH values, longer incubation periods, etc.) to "facilitate" the formation of new covalent linkages between the immobilized enzyme molecule and the support; 3) the remaining groups of the support are blocked to stop any additional interaction between the enzyme and the support. Progressive establishment of new enzyme-support attachments was showed by the progressive irreversible covalent immobilization of several subunits of multi-subunits proteins (all non-covalent structures contained in crude extracts of different microorganism, penicillin G acylase and chymotrypsin). This multipoint covalent attachment enabled the significant thermostabilization of two relevant enzymes, (compared with the just immobilized derivatives): chymotrypsin (5-fold factor) and penicillin G acylase (18-fold factor). Bearing in mind that this stabilization was additive to that achieved by conventional immobilization, the final stabilization factor become 100-fold comparing soluble penicillin G acylase and optimal derivative. These stabilizations were observed also when the inactivations were promoted by the enzyme exposure to drastic pH values or the presence of cosolvents.

Affinity chromatography of plasma proteins (guanidinobenzoatase): use of mimetic matrices and mimetic soluble ligands to prevent the binding of albumin on target affinity matrices

Serum albumin is the most abundant protein in plasma and it has a high capacity to bind many small compounds and macromolecules. In this way, albumin may promote important interferences during affinity chromatography of plasma proteins. Guanidinobenzoatase (GB) is a very relevant plasma protease that seems to be related to tumoral processes. This enzyme may be adsorbed on tailor-made agmatine-amide-agarose (CH-A) supports (e.g., the ones having 2 micromol of guanidino groups per ml of agarose attached to the support, through a 6 C aliphatic chain). Such tailor-made supports containing a very low concentration of ionized groups are hardly able to adsorb any protein by anion-exchange. However, they are able to strongly adsorb albumin. In order to solve this problem new mimetic affinity matrices have been designed: (i) by using the same ligand immobilized through a different chemical linkage [guanidino groups attached via secondary amino bonds, (AEA)] or (ii) by using slightly different ligands (e.g., 1,8-octanediamine containing a primary amino group instead of a guanidino one) also attached to the support via amido bonds (CH-DAO). Albumin adsorbs on the target and on the two mimetic matrices while GB is mainly adsorbed on the target one. Moreover, the adsorption of albumin on the affinity matrix (CH-A) is very strongly inhibited by the presence of low concentrations of soluble ligands (e.g., 1,8-octanediamine containing two ionized primary amino groups). On the contrary, the adsorption of GB on CH-A is hardly inhibited by the presence of such mimetic soluble ligand. In this way, the former offering of crude GB samples to AEA plus the use of mimetic inhibitors during adsorption of the extract on CH-A completely prevent the undesirable adsorption of albumin. In a such way, an extremely selective adsorption of GB can be performed. Such an improved chromatography procedure allows a very easy affinity purification and detection of GB.

'Interfacial affinity chromatography' of lipases: separation of different fractions by selective adsorption on supports activated with hydrophobic groups

Lipases contained in commercial samples of lipase extracts from Rhizopus niveus (RNL) and Candida rugosa (CRL) have been selectively adsorbed on hydrophobic supports at very low ionic strength. Under these conditions, adsorption of other proteins (including some esterases) is almost negligible. More interestingly, these lipases could be separated in several active fractions as a function of a different rate or a different intensity of adsorption on supports activated with different hydrophobic groups (butyl-, phenyl- and octyl-agarose). Thus, although RNL seemed to be a homogeneous sample by SDS-PAGE, it could be separated, via sequential adsorption on the different supports, into three different fractions with very different thermal stability and substrate specificity. For example, one fraction hydrolyzed more rapidly ethyl acetate than ethyl butyrate, while another hydrolyzed the acetate ester 7-fold slower than the butyrate. Similar results were obtained with samples of CRL. Again, we could obtain three different fractions showing very different properties. For example, enantioselectivity for the hydrolysis of (R,S) 2-hydroxy-4-phenylbutanoic acid ethyl ester ranged from 1.2 to 12 for different CRL fractions. It seems that very slight structural differences may promote a quite different interfacial adsorption of lipases on hydrophobic supports as well as a quite different catalytic behavior. In this way, this new 'interfacial affinity chromatography' seems to be very suitable for an easy separation of such slightly different lipase forms.

Use of aqueous two-phase systems for in situ extraction of water soluble antibiotics during their synthesis by enzymes immobilized on porous supports

Yields of kinetically controlled synthesis of antibiotics catalyzed by penicillin G acylase from Escherichia coli (PGA) have been greatly increased by continuous extraction of water soluble products (cephalexin) away from the surroundings of the enzyme. In this way its very rapid enzymatic hydrolysis has been avoided. Enzymes covalently immobilized inside porous supports acting in aqueous two-phase systems have been used to achieve such improvements of synthetic yields. Before the reaction is started, the porous structure of the biocatalyst can be washed and filled with one selected phase. In this way, when the pre-equilibrated biocatalyst is mixed with the second phase (where the reaction product will be extracted), the immobilized enzyme remains in the first selected phase in spite of its possibly different natural trend. Partition coefficients (K) of cephalexin in very different aqueous two-phase systems were firstly evaluated. High K values were obtained under drastic conditions. The best K value for cephalexin (23) was found in 100% PEG 600-3 M ammonium sulfate where cephalexin was extracted to the PEG phase. Pre-incubation of immobilized PGA derivatives in ammonium sulfate and further suspension with 100% PEG 600 allowed us to obtain a 90% synthetic yield of cephalexin from 150 mM phenylglycine methyl ester and 100 mM 7-amino desacetoxicephalosporanic acid (7-ADCA). In this reaction system, the immobilized enzyme remains in the ammonium sulfate phase and hydrolysis of the antibiotic becomes suppressed because of its continuous extraction to the PEG phase. On the contrary, synthetic yields of a similar process carried out in monophasic systems were much lower (55%) because of a rapid enzymatic hydrolysis of cephalexin.

A single step purification, immobilization, and hyperactivation of lipases via interfacial adsorption on strongly hydrophobic supports

A number of bacterial lipases can be immobilized in a rapid and strong fashion on octyl-agarose gels (e.g., lipases from Candida antarctica, Pseudomonas fluorescens, Rhizomucor miehei, Humicola lanuginosa, Mucor javanicus, and Rhizopus niveus). Adsorption rates in absence of ammonium sulfate are higher than in its presence, opposite to the observation for typical hydrophobic adsorption of proteins. At 10 mM phosphate, adsorption of lipases is fairly selective allowing enzyme purification associated with their reversible immobilization. Interestingly, these immobilized lipase molecules show a dramatic hyperactivation. For example, lipases from R. niveus, M. miehei, and H. lanuginosa were 6-, 7-, and 20-fold more active than the corresponding soluble enzymes when catalyzing the hydrolysis of a fully soluble substrate (0.4 mM p-nitrophenyl propionate). Even higher hyperactivations and interesting changes in stereospecificity were also observed for the hydrolysis of larger soluble chiral esters (e.g. (R,S)-2-hydroxy-4-phenylbutanoic ethyl ester). These results suggest that lipases recognize these "well-defined" hydrophobic supports as solid interfaces and they become adsorbed through the external areas of the large hydrophobic active centers of their "open and hyperactivated structure". This selective interfacial adsorption of lipases becomes a very promising immobilization method with general application for most lipases. Through this method, we are able to combine, via a single and easily performed adsorption step, the purification, the strong immobilization, and a dramatic hyperactivation of lipases acting in the absence of additional interfaces, (e.g., in aqueous medium with soluble substrate). Copyright 1998 John Wiley & Sons, Inc.

Immobilization of lipases by selective adsorption on hydrophobic supports

The preparation of immobilized derivatives of lipases that may be useful to develop industrial processes of organic synthesis is an exciting field of research in which three main features have to be simultaneously considered: (a) immobilized derivatives have to be compatible with very different reaction requirements (e.g. continuous adjustment of pH with concentrated alkali, use of aqueous media or organic solvents, etc.); (b) Sometimes, some activity/stability properties of lipases should be improved during immobilization; and (c) because of a complex mechanism of action, lipases are poorly active in the absence of hydrophobic interfaces. In this paper, we will review different approaches for lipase immobilization mainly related to the further use of immobilized derivatives to carry out enantio and regioselective hydrolysis in high water-activity systems. Special emphasis is paid to the selective adsorption of lipases on tailor-made strongly hydrophobic support surfaces. This new immobilization procedure is based on the assumption that the large hydrophobic area that surrounds the active site of lipases is the one mainly involved in their adsorption on strongly hydrophobic solid surfaces. Thus, lipases recognize these surfaces similarly to those of their natural substrates and they suffer interfacial activation during immobilization. This immobilization method permits: (a) promote a dramatic hyper-activation of most of lipases after their immobilization. That is, adsorbed lipases show very enhanced esterase activity in the absence of additional hydrophobic interfaces; (b) promote highly selective adsorption of lipases, at very low ionic strength, from impure protein extracts. That is, we can associate immobilization and purification of lipases; (c) promote interesting improvements of enantioselectivity after immobilization; and (d) promote a strong but reversible immobilization that enables us to recover these expensive supports after inactivation of immobilized lipases.

Dynamic reaction design of enzymic biotransformations in organic media: equilibrium-controlled synthesis of antibiotics by penicillin G acylase

Parameters relevant to the thermodynamically controlled synthesis of cephalothin utilizing highly active stabilized penicillin G acylase derivatives were studied. These included solubility/stability of substrates, enzyme derivative activity/stability, reaction course and synthetic yields. These parameters were altered by varying the pH, dimethylformamide concentration and temperature. Simultaneous optimization of the selected parameters could not be achieved with a single set of conditions. However, continuous adjustment of conditions throughout the reaction course allowed each parameter to be optimized (dynamic reaction design). This strategy works by optimizing those parameters that are critical to the overall reaction at a given point, whilst leaving others sub-optimal when their contribution to the total is minimal. This strategy has achieved a 90% transformation of antibiotic nucleus to cephalothin at a final concentration of 20 g/l, high enzyme and reactant stability, with a reaction period of 3 h (using 1 ml of derivative/40 ml of reaction solution).

Purification and partial characterization of a novel thermophilic carboxylesterase with high mesophilic specific activity

An esterase activity obtained from a strain of Bacillus stearothermophilus was purified 5,133-fold to electrophoretic homogeneity with 26% recovery. The purified esterase had a specific activity of 2,032 mumol min-1 mg-1 based on the hydrolysis of p-nitrophenyl caproate at pH 7.0 and 30 degrees C. The apparent molecular mass was 50,000 +/- 2,000 daltons from sodium dodecyl sulfate-polyacrylamide gel electrophoresis and 45,000 +/- 3,000 daltons from gel filtration. Native polyacrylamide gels stained for esterase activity showed three bands. The isoelectric points were estimated to be 5.7, 5.8, and 6.0. Forty amino acid residues were sequenced at the N-terminus. The sequence showed no degeneracy, suggesting that the three esterases are functionally identical carboxylesterases differing by a limited number of amino acids. The enzyme showed maximum activity at pH 7.0 and was very stable at pH 6.0-8.9 with optimum stability at pH 6.0. At this pH and 60 degrees C the half-life was 170 h. Esterase activity was totally inhibited by phenylmethanesulfonyl fluoride, parahydroxymercuribenzoate, eserine, and tosyl-L-phenylalanine, but not by ethylendiaminetetra acetic acid. The esterase obeyed Michaelis-Menten kinetics in the hydrolysis of p-nitrophenyl esters, but both Vmax and KM were protein concentration-dependent. The esterase was able to hydrolyse a number of p-nitrophenyl derivatives (amino acid derivatives and aliphatic acids with different chain lengths).

Industrial design of enzymic processes catalysed by very active immobilized derivatives: utilization of diffusional limitations (gradients of pH) as a profitable tool in enzyme engineering

We have developed integrated studies of enzyme reaction engineering for the hydrolysis of penicillin G catalysed by very active penicillin G acylase (PGA) derivatives. We have studied the distinct effect of a key variable (pH) on different industrial parameters (e.g. activity/stability parameters). In this way we have demonstrated, in contrast with that proposed by other authors, that the generation of gradients of pH inside the porous structure of very active enzyme derivatives may be not a problem but a 'very profitable tool' to improve the whole set of industrial parameters. In this way we can establish two distinct 'optimal pH values': (i) the one inside the particle of the biocatalyst and (ii) the one in the bulk solution. The use of an external pH of 8.0 associated with the promotion of a controlled decrease in internal pH (e.g. around a mean value of 5.5) was very useful to simultaneously obtain interesting values of all industrial parameters: (i) very high hydrolytic yields (higher than 97%); (ii) a very important increase on the stability of PGA derivatives (higher than a 50-fold factor); and (iii) a very small decrease in operational activity (approximately 15%) as compared with the one of soluble enzyme at pH 8.0 with no diffusional hindrances.

Proteolytic degradation of the RGD-binding and non-RGD-binding conformers of human platelet integrin glycoprotein IIb/IIIa: clues for identification of regions involved in the receptor's activation

The human integrin glycoprotein (GP)IIb/IIIa plays a central role in haemostasis as an inducible receptor for fibrinogen and other RGD-containing adhesive proteins at the platelet plasma membrane. Expression of the fibrinogen receptor on platelet activation involves conformational changes in the quaternary structure of GPIIb/IIIa. Little is known, however, about the nature of this conformational transition. Given that isolated GPIIb/IIIa contains a mixture of RGD-binding and non-RGD-binding heterodimers, we used limited proteolysis as a tool for investigating the structural differences between the two conformers. Comparison of their fragmentation patterns shows that, whereas in the non-RGD-binding form of GPIIb/IIIa the N-terminal half of the heavy chain of GPIIb (GPIIbH) and the central region of GPIIIa are cleaved by endoproteinase Arg-C, these domains associate tightly with one another in the RGD-binding GPIIb/IIIa and are thus protected from proteolysis. In addition, the C-terminal half of GPIIb becomes more susceptible to degradation in the non-RGD-binding GPIIb/IIIa conformer. Our interpretation, in the context of available structural and functional data, is that a major relative reorientation of the GPIIbH and GPIIIa extracellular domains takes place along the subunit interface during the conformational transition of the platelet integrin.

Preparation of activated supports containing low pK amino groups. A new tool for protein immobilization via the carboxyl coupling method

A method for the preparation of new aminated agarose gels containing monoaminoethyl-N-aminoethyl structures, MANA-agarose gels, has been developed. These gels contain primary amino groups with a very low pK value (6.8). In addition to that, we have been able to prepare very highly activated gels (e.g., 10% agarose gels containing up to 200 mu Eq of primary amines per milliliter). These two properties make these activated supports suitable for performing novel and interesting methods for protein immobilizations via very mild carbodiimide activation of carboxy groups. For example, very effective coupling reactions can be performed at pH 5.0-6.0 in the presence of low concentrations of activating agent, e.g., 1 mM. By using a model industrial enzyme, beta-galactosidase from Aspergillus oryzae, we have been able to demonstrate the excellent prospects of these novel activated supports.

Enzyme reaction engineering: Synthesis of antibiotics catalysed by stabilized penicillin G acylase in the presence of organic cosolvents

By using very active and very stable penicillin G acylase (PGA)--agarose derivatives we have studied the industrial design of equilibrium-controlled synthesis of lactamic antibiotics. In the presence of high concentrations of organic cosolvents we have carried out the direct enzymatic condensation of phenylacetic acid and 6-aminopenicillanic acid to yield the model antibiotic penicillin G. We have mainly studied the integrated effect of different variables that define the reaction medium on a number of parameters of industrial interest:time course of antibiotic synthesis, highest synthetic yields, stability of the catalyst, and solubility and stability of substrates and products. The main variables tested were the nature and concentration of the organic cosolvent, pH, and temperature. The effects of the variables tested on different parameters were quite different and sometimes opposite. Hence, the optimal experimental conditions for antibiotic synthesis catalysed by PGA were established, as a compromise solution, in order to obtain good values for every parameter of industrial interest. These conditions seem to be important parameters for scale-up (e.g. we have been able to reach more than 95% of synthetic yields with productivities around 0.5 tons of model antibiotic per year per liter of catalyst).

Stabilizing effect of penicillin G sulfoxide, a competitive inhibitor of penicillin G acylase: Its practical applications

We have found that penicillin G sulfoxide (pen G SO) behaves as a general stabilizing agent of two bacterial penicillin G acylases (PGAs) from E. coli and from K. citrophila), and this role is related to a strong inhibitory effect on the enzymes. The stabilizing effect has been observed during two different inactivation processes: (i) thermal inactivation of soluble enzymes at alkaline pH, and (ii) inactivation of immobilized enzymes as a consequence of covalent multiinteraction with highly activated agarose aldehyde gels. At the same time, pen G SO behaves as a strong competitive inhibitor of these two enzymes. The inhibition constant is more than 10-fold lower than the one corresponding to another smaller competitive inhibitor, phenylacetic acid (PAA), the structure of which is exactly the acyl donor moiety corresponding to pen G SO. In turn, PAA hardly exerts any stabilizing effect on PGAs. The stabilizing effect of pen G SO allowed the preparation of derivatives of these PGAs preserving full catalytic activity in spite of being 1,400- and 650-fold more stable than the corresponding soluble or one-point attached immobilized enzymes.

Immobilization-stabilization of penicillin G acylase from Escherichia coli

We have developed a strategy for immobilization-stabilization of penicillin G acylase from E. coli, PGA, by multipoint covalent attachment to agarose (aldehyde) gels. We hve studied the role of three main variables that control the intensity of these enzyme-support multiinteraction processes: 1. surface density of aldehyde groups in the activated support; 2. temperature; and 3. contact-time between the immobilized enzyme and the activated support prior to borohydride reduction of the derivatives. Different combinations of these three variables have been tested to prepare a number of PGA-agarose derivatives. All these derivatives preserve 100% of catalytic activity corresponding to the soluble enzyme that has been immobilized but they show very different stability. The less stable derivative has exactly the same thermal stability of soluble penicillin G acylase and the most stable one is approximately 1,400 fold more stable. A similar increase in the stability of the enzyme against the deleterious effect of organic solvents was also observed. On the other hand, the agarose aldehyde gels present a very great capacity to immobilize enzymes through multipoint covalent attachment. In this way, we have been able to prepare very active and very stable PGA derivatives containing up to 200 International Units of catalytic activity per mL. of derivative with 100% yields in the overall immobilization procedure.