Structural differences of commercial and recombinant lipase B from Candida antarctica: An important implication on enzymes thermostability.

Lipase B from Candida antarctica (CalB) is the most widely used lipase, including in many industrial sectors, such as in biodiesel and pharmaceuticals production. CalB has been produced by heterologous expression using Pichia pastoris under PGK constitutive promoter (named LipB). Here, we have studied the structural features of commercial CalB and LipB enzymes using circular dichroism and fluorescence under different conditions. In the presence of denaturing agents CalB was more stable than LipB, in contrast, at increasing temperatures, LipB was more thermostable than CalB. Mass spectrometry data indicates that both enzymes have an insertion of amino acids related to α-factor yeast signal, however LipB enzyme showed the addition of nine residues at the N-terminal while CalB showed only four residues. Molecular modeling of LipB showed the formation of an amphipathic α-helix in N-terminal region that was not observed in CalB. This data suggests that this new α-helix possess could be involved in LipB thermostability. These results associated with new structural studies may provide information to the design of novel biocatalysts.

Immobilization of Lipases on Heterofunctional Octyl-Glyoxyl Agarose Supports: Improved Stability and Prevention of the Enzyme Desorption.

Lipases are among the most widely used enzymes in industry. Here, a novel method is described to rationally design the support matrix to retain the enzyme on the support matrix without leaching and also activate the enzyme for full activity retention. Lipases are interesting biocatalysts because they show the so-called interfacial activation, a mechanism of action that has been used to immobilize lipases on hydrophobic supports such as octyl-agarose. Thus, adsorption of lipases on hydrophobic surfaces is very useful for one step purification, immobilization, hyperactivation, and stabilization of most lipases. However, lipase molecules may be released from the support under certain conditions (high temperature, organic solvents), as there are no covalent links between the enzyme and the support matrix. A heterofunctional support has been proposed in this study to overcome this problem, such as the heterofunctional glyoxyl-octyl agarose beads. It couples the numerous advantages of the octyl-agarose support to covalent immobilization and creates the possibility of using the biocatalyst under any experimental conditions without risk of enzyme desorption and leaching. This modified support may be easily prepared from the commercially available octyl-agarose. Preparation of this useful support and enzyme immobilization on it via covalent linking is described here. The conditions are described to increase the possibility of achieving at least one covalent attachment between each enzyme molecule and the support matrix.

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

Semi-synthetic ß-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 ß-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.

Influence of mass transfer limitations on the enzymatic synthesis of beta-lactam antibiotics catalyzed by penicillin G acylase immobilized on glioxil-agarose.

Mass transfer effects were investigated for the synthesis of ampicillin and amoxicillin, at pH 6.5 and 25 degrees C, catalyzed by penicillin G acylase immobilized on agarose. The influence of external mass transfer was analysed using different stirring rates, ranging form 200 to 800 rpm. Above 400 rpm, the film resistance may be neglected. Intra-particle diffusion limitation was investigated using biocatalysts prepared with different enzyme loads and agarose with different mean pore diameters. When agarose with 6, 8 and 10% of crosslinking were used, for the same enzyme load, substrates and products concentration profiles presented no expressive differences, suggesting pore diameter is not important parameter. An increase on enzyme load showed that when more than 90 IU of enzyme activity were used per mL of support, the system was influenced by intra-particle mass transfer. A reactive-diffusive model was used to estimate effective diffusivities of substrates and products.

Design of new immobilized-stabilized carboxypeptidase a derivative for production of aromatic free hydrolysates of proteins.

This paper presents stable carboxypeptidase A (CPA)-glyoxyl derivatives, to be used in the controlled hydrolysis of proteins. They were produced after immobilizing-stabilizing CPA on cross-linked 6% agarose beads, activated with low and high concentrations of aldehyde groups, and different immobilization times. The CPA-glyoxyl derivatives were compared to other agarose derivatives, prepared using glutaraldehyde as activation reactant. The most stabilized CPA-glyoxyl derivative was produced using 48 h of immobilization time and high activation grade of the support. This derivative was approximately 260-fold more stable than the soluble enzyme and presented approximately 42% of the activity of the soluble enzyme for the hydrolysis of long-chain peptides (e.g., cheese whey proteins previously hydrolyzed with immobilized trypsin and chymotrypsin) and of the small substrate N-benzoylglycyl-l-phenylalanine (hippuryl-l-Phe). These results were much better than those achieved using the conventional support, glutaraldehyde-agarose. Amino acid analysis of the products of the acid hydrolysis of CPA (both soluble and immobilized) showed that approximately four lysine residues were linked on the glyoxyl agarose beads, suggesting the existence of an intense multipoint covalent attachment between the enzyme and the support. The maximum temperature of hydrolysis was increased from 50 degrees C (soluble enzyme) to 70 degrees C (most stable CPA-glyoxyl derivative). The most stable CPA-glyoxyl derivative could be efficiently used in the hydrolysis of long-chain peptides at high temperature (e.g., 60 degrees C), being able to release 2-fold more aromatic amino acids (Tyr, Phe, and Trp) than the soluble enzyme, under the same operational conditions. This new CPA derivative greatly increased the feasibility of using this protease in the production of protein hydrolysates that must be free of aromatic amino acids.

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.