Abstract
Fed-batch and perfusion bioreactors are commonly used in biopharmaceutical production. This study applies mathematical models to investigate the influence of substrate concentration in the media added ((Formula presented.)), operating substrate concentration in the bioreactor ((Formula presented.)), and bioreaction time on the performance of both bioreactors. The performance parameters are titer, productivity, product yield, wasted substrate, and mean product residence time. The difference between the substrate concentration in the media and the operating substrate concentration has a major impact on performance parameters. For a fixed (Formula presented.), operating at higher values of (Formula presented.) is more beneficial to both fed-batch and perfusion performance. Higher productivities are obtained in perfusion, and mean product residence times are shorter. Furthermore, perfusion can obtain titers comparable to fed-batch when operated at similar substrate concentrations. All this suggests that perfusion is more advantageous. It is advantageous to operate the bioreactors over a longer bioreaction time. However, for fed-batch bioreactors, there exists an optimal time after which there is a major progressive reduction in productivity.
| Original language | English |
|---|---|
| Article number | 48 |
| Journal | ChemEngineering |
| Volume | 9 |
| Issue number | 3 |
| DOIs | |
| Publication status | Published - Jun 2025 |
Keywords
- biopharmaceutical
- bioreactor performance
- fed-batch
- perfusion
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