Unsteady‐state operation of continuous fermentor for enhancement of cell mass production
- 4 August 1987
- journal article
- research article
- Published by Wiley in Biotechnology & Bioengineering
- Vol. 30 (2) , 187-195
- https://doi.org/10.1002/bit.260300208
Abstract
The transient behavior of continuous fermentation is studied concentrating on the time scale intrinsic to the system. The time scale is the time required for the fermentorto reach a stable steady state after the disturbance of cell mass is introduced. When the cell concentration is disturbed from the steady‐state value, in particular, at the dilution rate near washout, the transient period becomes extended significantly, and the steady state is resumed sluggishly. This sluggish transient behavior could be turned to an advantage for enhancing the cell mass output rate. The proposed transient operation is a continuous fermentation whereby a positive disturbance in the cell mass is introduced, so that the cell concentration is higher than the steady‐state value for an extended transient period. It is shown that a significantly higher cell mass production than that from the steady‐state continuous fermentation can be achieved. Simple experiments were performed to demonstrate the improvement of cell (Candida utilis) productivity.Keywords
This publication has 4 references indexed in Scilit:
- An experimental investigation of stability and multiplicity of steady states in a biological reactorAIChE Journal, 1981
- Optimal control of bacterial growthAutomatica, 1972
- A nonlinear regulator problem for a model of biological waste treatmentIEEE Transactions on Automatic Control, 1971
- Fermentation Process Control, Population Dynamics of a Continuous Propagator for MicroorganismsJournal of Agricultural and Food Chemistry, 1954