alpha-chymotrypsin and 1-4-butanediol

An immobilised enzyme reactor (IMER) in the form of capillary monolith was developed for a micro-liquid chromatography system. The plain monolith was obtained by in situ thermal copolymerisation of glycidyl methacrylate and ethylene dimethacrylate in a fused silica capillary (200 × 0.53 mm ID) by using n-propanol/1,4-butanediol as porogen. The enzyme, α-chymotrypsin (CT), was covalently attached onto the monolith via triazole ring formation by click-chemistry. For this purpose, the monolithic support was treated with sodium azide and reacted with the alkyne carrying enzyme derivative. CT was covalently linked to the monolith by triazole-ring formation. The activity behaviour of monolithic IMER was investigated in a micro-liquid chromatography system by using benzoyl-L-tyrosine ethyl ester (BTEE) as synthetic substrate. The effects of mobile-phase flow rate and substrate feed concentration on the final BTEE conversion were investigated under steady-state conditions. In the case of monolithic IMER, the final substrate conversion increased with increasing feed flow rate and increasing substrate feed concentration. Unusual behaviour was explained by the presence of convective diffusion in the macropores of monolith. The results indicated that the monolithic-capillary IMER proposed for micro-liquid chromatography had significant advantages with respect to particle-based conventional high-performance liquid chromatography-IMERs.

Topics: Butylene Glycols; Chromatography, Liquid; Chymotrypsin; Click Chemistry; Enzymes, Immobilized; Epoxy Compounds; Hydrolysis; Methacrylates; Polymerization; Triazoles; Tyrosine

An enzymic transesterification was carried out in a continuously operated fixed bed reactor. The reaction system consisted of immobilized alpha-chymotrypsin (E.C. 3.4.21.1) catalysing the transfer of the L-phenylalanine radical from the racemic propyl ester to 1,4-butanediol, yielding L-phenylalanine 4-hydroxybutyl ester. The desired reaction was accompanied by alcoholysis due to the presence of 1-propanol liberated during the reaction and by hydrolysis of both the propyl and the hydroxybutyl ester. The problem of shifting pH during the reaction due to ester hydrolysis was overcome by adjusting the initial pH of the substrate feed solution appropriately in order to obtain a sufficiently high buffer capacity provided by the free amino group of the esters. Thus, it was possible to work with shifting pH, an obvious disadvantage for operating reactors of low backmixing for this kind of reaction system. The overall reaction scheme was characterized by the appearance of a maximum ester yield as a function of the operating time in case of batch reactors. Surprisingly, the yield was found to become constant as a function of space-time for continuous operation due to a steeper pH drop. The maximum productivity achieved with respect to the hydroxybutyl ester was about 65 mol d-1 l-1 referred to the catalyst volume.

Topics: Butylene Glycols; Chymotrypsin; Enzymes, Immobilized; Esters; Kinetics; Phenylalanine