## Abstract Previously, using maximum feed concentrations of 500 mg/L, an immobilized cell reactor (ICR) with established biofilm was shown to enhance the biodegradation rate of a candidate naphthenic acid up to two orders of magnitude when compared to a freely suspended cell, well mixed tank react
A model for micro/ultrafiltration cell deactivation in cell-recycle reactors
✍ Scribed by João A P Coutinho; Ana M R B Xavier
- Publisher
- Wiley (John Wiley & Sons)
- Year
- 2000
- Tongue
- English
- Weight
- 110 KB
- Volume
- 75
- Category
- Article
- ISSN
- 0268-2575
No coin nor oath required. For personal study only.
✦ Synopsis
Mechanical stress due to micro/ultra®ltration has been suggested by a number of authors as one of the sources for cell deactivation in continuous cell-recycle reactors. This work introduces cell deactivation in the modelling of cell-recycle fermenters. A two-population based model is used. It is shown that the kinetic parameters obtained from chemostat fermentations describe accurately the experimental results and the apparent deviations to the Luedeking±Piret relationship at low growth rates are explained. The model is applied to the data of two authors with dilution rates (D) ranging 0.2 and 1.05 h À1 and using either Lactobacillus rhamnosus or Lactococcus cremoris cells. Although only data for lactic fermentation were used, the proposed model is of general applicability and not restricted to a type of fermentation, a given apparatus con®guration or Newtonian ¯uids. The development of improved procedures for biological reactor modelling, such as presented in this work, wall allow more adequate and ef®cient design and operation of these reactors.
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