New Scale-Up Technologies for Hydrogenation Reactions in Multipurpose Pharmaceutical Production Plants

Authors

  • Thierry Furrer Institute for Chemistry and Bioanalytics, University of Applied Sciences and Arts Northwestern Switzerland, School of Life Sciences (FHNW HLS), Hofackerstrasse 30, CH-4132 Muttenz https://orcid.org/0000-0002-1096-209X
  • Benedikt Müller Institute for Chemistry and Bioanalytics, University of Applied Sciences and Arts Northwestern Switzerland, School of Life Sciences (FHNW HLS), Hofackerstrasse 30, CH-4132 Muttenz
  • Christoph Hasler Institute for Chemistry and Bioanalytics, University of Applied Sciences and Arts Northwestern Switzerland, School of Life Sciences (FHNW HLS), Hofackerstrasse 30, CH-4132 Muttenz
  • Bernhard Berger Siegfried AG, Untere Brühlstrasse 4, CH-4800
  • Michael Karl Levis Siegfried AG, Untere Brühlstrasse 4, CH-4800 Zofingen
  • Andreas Zogg Institute for Chemistry and Bioanalytics, University of Applied Sciences and Arts Northwestern Switzerland, School of Life Sciences (FHNW HLS), Hofackerstrasse 30, CH-4132 Muttenz

DOI:

https://doi.org/10.2533/chimia.2021.948

PMID:

34798917

Keywords:

Agitated vessel, Hydrogenation, Process modelling, Quality by Design (QbD), Scale-up / Scale-down

Abstract

The classical scale-up approach for hydrogenation reaction processes usually includes numerous laboratory and pilot scale experiments. With a novel scale-up strategy a significant number of these experiments may be replaced by modern computational simulations in combination with scale-down experiments. With only a few laboratory scale experiments and information about the production scale reactor, a chemical process model is developed. This computational model can be used to simulate the production scale process with a range of different process parameters. Those simulations are then validated by only a few experiments in an advanced scale-down reactor. The scale-down reactor has to be geometrically identical to the corresponding production scale reactor and should show a similar mass transfer behaviour. Closest similarity in terms of heat transfer behaviour is ensured by a sophisticated 3D-printed heating / cooling finger, offering the same heat exchange area per volume as in production scale. The proposed scale-up strategy and the custom-designed scale-down reactor will be tested by proof of concept with model reactions and those results will be described in a future publication. This project is an excellent example of a collaboration between academia and industry, which was funded by the Aargau Research Fund. The interest of academia is to study and understand all physical and chemical processes involved, whereas industry is interested in generating a robust and simple to use tool to improve scale-up and make reliable predictions.

Downloads

Published

2021-11-11

How to Cite

[1]
T. Furrer, B. Müller, C. Hasler, B. Berger, M. K. Levis, A. Zogg, Chimia 2021, 75, 948, DOI: 10.2533/chimia.2021.948.