Abstract
In this research we analyze the steady-state operation of a continuous flow bioreactor, with or without recycle, and an idealized or nonidealized continuous flow membrane reactor. The model extends to include a fixed bed reactor where a fraction of the biomass is detached by the flow. The reaction is assumed to be governed by Tessier growth kinetics. We show that a flow reactor with idealized recycle has the same performance as an idealized membrane reactor and that the performance of a nonidealized membrane reactor is identical to that of an appropriately defined continuous flow bioreactor with nonidealized recycle. The performance of all three reactor types can therefore be obtained by analyzing a flow reactor with recycle. The steady states of the recycle model are found and their stability determined as a function of the residence time. The performance of the reactor at large residence times is obtained.
Original language | English |
---|---|
Pages (from-to) | 417-433 |
Number of pages | 17 |
Journal | Chemical Engineering Communications |
Volume | 199 |
Issue number | 3 |
DOIs | |
Publication status | Published - Mar 2012 |
Keywords
- Bioreactor
- Kinetics
- Membrane reactor
- Modeling
- Stirred tank
ASJC Scopus subject areas
- Chemistry(all)
- Chemical Engineering(all)