Mathematical description of heat and mass transfer during deep bed drying: Effect of product shrinkage on bed porosity
โ Scribed by Lyes Bennamoun; Azeddine Belhamri
- Publisher
- Elsevier Science
- Year
- 2008
- Tongue
- English
- Weight
- 269 KB
- Volume
- 28
- Category
- Article
- ISSN
- 1359-4311
No coin nor oath required. For personal study only.
๐ SIMILAR VOLUMES
The pressure drop per umt length m flow through packed beds or past turbulence promoters IS the sum of viscous and kmetlc losses 5 = a@+ bpV2 The transfer rates m such systems (dependent only on the VISCOUS forces at the transfer surfaces) are correlated by -112 = K [Re\*]-"e and may therefore be p
## 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