Next level of p-phenylene diisothiocyanate-based covalent immobilization of β-D-galactosidase: Technical optimization as an application

In this study, a continuous lactose hydrolysis process in a fixed-bed reactor was developed using β-galactosidase covalently immobilized on resin beads via 1,4-phenylenediisothiocyanate (PDC) as linker. Process conditions, including temperature, enzyme loading, perfusion speed, and repeated perfusion of the same substrate solution were systematically varied. The highest glucose yields were obtained at 55 °C, with increased yields observed at low perfusion speeds, high enzyme loadings, and upon repeated perfusions. Under optimized cycle perfusion over 72 h, final lactose conversion reached approximately 90 % at 37 °C and 80 % at 22 °C. A hydrolysis process in a fixed-bed reactor was successfully established, although further optimization is required.

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Publication Details

Journal
Journal of Biotechnology
Published
2025-12-10
DOI
https://doi.org/10.1016/j.jbiotec.2025.12.004
Primary Topic
Enzyme Catalysis and Immobilization
Type
article
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article

Next level of p-phenylene diisothiocyanate-based covalent immobilization of β-D-galactosidase: Technical optimization as an application

Ursula Eschenhagen, Magnus S. Schmidt, Tabea L. Boehme, Bernadette Straub
Journal of Biotechnology
Enzyme Catalysis and Immobilization
article

Next level of p-phenylene diisothiocyanate-based covalent immobilization of β-D-galactosidase: Technical optimization as an application

Ursula Eschenhagen, Magnus S. Schmidt, Tabea L. Boehme, Bernadette Straub
article en

Abstract

In this study, a continuous lactose hydrolysis process in a fixed-bed reactor was developed using β-galactosidase covalently immobilized on resin beads via 1,4-phenylenediisothiocyanate (PDC) as linker. Process conditions, including temperature, enzyme loading, perfusion speed, and repeated perfusion of the same substrate solution were systematically varied. The highest glucose yields were obtained at 55 °C, with increased yields observed at low perfusion speeds, high enzyme loadings, and upon repeated perfusions. Under optimized cycle perfusion over 72 h, final lactose conversion reached approximately 90 % at 37 °C and 80 % at 22 °C. A hydrolysis process in a fixed-bed reactor was successfully established, although further optimization is required.

Journal of BiotechnologyVol. 410
Nephrologisches Zentrum Villingen-Schwenningen (DE), Furtwangen University (DE)
Openalex Percentile: Top 64%
Enzyme Catalysis and Immobilization
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