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Optimization and scale-up of oligonucleotide synthesis in packed bed reactors using computational fluid dynamics
Christian Wolfrum1, Andre Josten, Peter Götz
1Eckart GmbH Werk Wackersdorf, Boschstraße 1, 92442, Wackersdorf, Germany.
Biotechnology Progress
|August 9, 2014
Summary
A computational fluid dynamics model optimizes oligonucleotide synthesis scale-up in packed bed reactors. This validated model successfully predicted process performance at a larger scale, improving manufacturing efficiency.
Area of Science:
- Chemical Engineering
- Biotechnology
- Computational Science
Background:
- Oligonucleotide synthesis is crucial for various biotechnological applications.
- Scaling up oligonucleotide synthesis in packed bed reactors presents significant challenges.
- Accurate modeling is needed to optimize process parameters and ensure efficient scale-up.
Purpose of the Study:
- To develop and validate a computational fluid dynamics (CFD) model for oligonucleotide synthesis in packed bed reactors.
- To utilize the CFD model for optimizing the scale-up of the oligonucleotide synthesis process.
- To assess the feasibility of large-scale production based on simulation.
Main Methods:
- Developed a CFD model incorporating reaction kinetics data under defined conditions.
- Validated the model against experimental data for flow conditions and reaction kinetics.
- Performed scale-up simulations from a 0.3 g capacity column to a 440 g capacity scale.
Main Results:
- The CFD model accurately predicted flow conditions and reaction kinetics.
- Model validation confirmed its reliability for process analysis.
- Scale-up simulations demonstrated the model's effectiveness in predicting performance at a larger scale.
Conclusions:
- The developed CFD model is a valuable tool for analyzing and optimizing oligonucleotide synthesis in packed bed reactors.
- The model facilitates efficient and reliable scale-up of the synthesis process.
- CFD modeling enables successful prediction of large-scale production performance.
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