| Autor: |
H. Othman, Sameh, A. Sohsah, Mustfa, M. Ghoneim, Mohammad, E. El-Anadouli, Bahgat |
| Zdroj: |
Industrial & Engineering Chemistry Research; April 2006, Vol. 45 Issue: 8 p2808-2817, 10p |
| Abstrakt: |
Reactor design for fluid−solid, noncatalytic reaction depends on the prediction of the performance of the reactor kinetically. Most mathematical models used to handle a fixed bed reactor in which the solid bed constitutes one of the reactants, while a second reactant is in the fluid phase, are complex and difficult to handle. A new mathematical model which is easier to handle has been developed to describe the system under investigation. The model was examined theoretically and experimentally. A column packed with a chelating cloth filter to separate radionuclides from radioactive waste solution is used as a practical application for the model. A comparison of the model predictions with the experimental results gives a satisfactory agreement at most of the process stages. |
| Databáze: |
Supplemental Index |
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