Development of an Experimental Setup and a Validated Model for a Highly Integrated Biocatalytic Process

The development and validation of a mathematical model for a highly integrated biocatalytic process are presented. A multienzymatic cascade comprising three parallel and sequential reaction steps was implemented in a miniplant setup, integrating an enzyme membrane reactor (EMR) and a reactive extraction centrifuge (REC) to enable intensified biotransformations. Laboratory-scale experiments were conducted to obtain the kinetic and thermodynamic data necessary for model development. The resulting process model captures both the enzymatic reaction kinetics and the dynamic behavior of the integrated unit operations. Model validation was performed under representative process conditions in the miniplant system. The results demonstrate good agreement between the model and experimental data, confirming the predictive power of the model and supporting its use in future process design, scale-up, and optimization. This work underscores the importance of model-based development for advancing sustainable and efficient biocatalytic processes.

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Publication Details

Journal
Chem & Bio Engineering
Published
2026-03-26
DOI
https://doi.org/10.1021/cbe.5c00167
Primary Topic
Enzyme Catalysis and Immobilization
Type
article
Field-Weighted Citation Impact
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article

Development of an Experimental Setup and a Validated Model for a Highly Integrated Biocatalytic Process

Thomas Waluga, Paul Bubenheim, Francesca von Ziegner, Grit Brauckmann et al.
Chem & Bio Engineering
Enzyme Catalysis and Immobilization
article

Development of an Experimental Setup and a Validated Model for a Highly Integrated Biocatalytic Process

Thomas Waluga, Paul Bubenheim, Francesca von Ziegner, Grit Brauckmann, Christoph Witthoefft
article en

Abstract

The development and validation of a mathematical model for a highly integrated biocatalytic process are presented. A multienzymatic cascade comprising three parallel and sequential reaction steps was implemented in a miniplant setup, integrating an enzyme membrane reactor (EMR) and a reactive extraction centrifuge (REC) to enable intensified biotransformations. Laboratory-scale experiments were conducted to obtain the kinetic and thermodynamic data necessary for model development. The resulting process model captures both the enzymatic reaction kinetics and the dynamic behavior of the integrated unit operations. Model validation was performed under representative process conditions in the miniplant system. The results demonstrate good agreement between the model and experimental data, confirming the predictive power of the model and supporting its use in future process design, scale-up, and optimization. This work underscores the importance of model-based development for advancing sustainable and efficient biocatalytic processes.

Chem & Bio Engineering
Universität Hamburg (DE), Hamburg University of Technology (DE)
Openalex Percentile: Top 7%
Enzyme Catalysis and Immobilization
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