Aviso: para depositar documentos, por favor, inicia sesión e identifícate con tu cuenta de correo institucional de la UCM con el botón MI CUENTA UCM. No emplees la opción AUTENTICACIÓN CON CONTRASEÑA
 

Let the Substrate Flow, Not the Enzyme: Practical Immobilization of D-Amino Acid Oxidase in a Glass Microreactor for Effective Biocatalytic Conversions

Loading...
Thumbnail Image

Full text at PDC

Publication date

2016

Advisors (or tutors)

Editors

Journal Title

Journal ISSN

Volume Title

Publisher

Wiley
Citations
Google Scholar

Citation

Bolivar, J. M., Tribulato, M. A., Petrasek, Z., & Nidetzky, B. (2016). Let the substrate flow, not the enzyme: Practical immobilization of d-amino acid oxidase in a glass microreactor for effective biocatalytic conversions. Biotechnology and Bioengineering, 113(11), 2342-2349. https://doi.org/10.1002/BIT.26011

Abstract

Exploiting enzymes for chemical synthesis in flow microreactors necessitates their reuse for multiple rounds of conversion. To achieve this goal, immobilizing the enzymes on microchannel walls is a promising approach, but practical methods for it are lacking. Using fusion to a silica-binding module to engineer enzyme adsorption to glass surfaces, we show convenient immobilization of D-amino acid oxidase on borosilicate microchannel plates. In confocal laser scanning microscopy, channel walls appeared uniformly coated with target protein. The immobilized enzyme activity was in the range expected for monolayer coverage of the plain surface with oxidase (2.37 105 nmol/mm2 ). Surface attachment of the enzyme was completely stable under flow. The operational half-life of the immobilized oxidase (25 C, pH 8.0; soluble catalase added) was 40 h. Enzymatic oxidation of D-Met into a-keto-g-(methylthio)butyric acid was characterized in single-pass and recycle reactor configurations, employing in-line measurement of dissolved O2, and off-line determination of the keto-acid product. Reaction-diffusion time-scale analysis for different flow conditions showed that the heterogeneously catalyzed reaction was always slower than diffusion of O2 to the solid surface (DaII 0.3). Potential of the microreactor for intensifying O2-dependent biotransformations restricted by mass transfer in conventional reactors is thus revealed

Research Projects

Organizational Units

Journal Issue

Description

Keywords

Collections