A two-dimensional heat transfer model was validated against two experimental studies from the literature which describe the growth of Aspergillus niger during solid-state fermentation in packed bed bioreactors. With the same set of model parameters, the twodimensional model was able to describe both
โฆ LIBER โฆ
Oxygen transfer characteristics of a centrifugal, packed-bed reactor during viscous xanthan fermentation
โ Scribed by Y. Lo; C. Hsu; S. Yang; D. Min
- Publisher
- Springer
- Year
- 2001
- Tongue
- English
- Weight
- 144 KB
- Volume
- 24
- Category
- Article
- ISSN
- 1615-7605
No coin nor oath required. For personal study only.
๐ SIMILAR VOLUMES
Validation of a model describing two-dim
โ
Penjit Sangsurasak; David A. Mitchell
๐
Article
๐
1998
๐
John Wiley and Sons
๐
English
โ 225 KB
๐ 3 views
Dispersion and Mass Transfer Effects on
โ
V. Ramachandra Murty; Jayadev Bhat; P. K. A. Muniswaran; S. Sivasankaran
๐
Article
๐
2008
๐
John Wiley and Sons
๐
English
โ 407 KB
๐ 2 views
## Abstract The performance of an immobilized packed bed reactor for the hydrolysis of rice bran oil has been investigated and can be well described by a dispersion model with an average standard deviation of 0.0388. Global mass transfer coefficients estimated using the model and experimental data