Their performance is tested against experimental data for different operating conditions. The importance of the different assumptions is analyzed and discussed. For the conditions analyzed in the present article the model of Rajah and Wen more closely follows the experimental trends. However, some d
Mathematical modeling of fluidized-bed chlorination of rutile
β Scribed by L. Zhou; H. Y. Sohn
- Publisher
- American Institute of Chemical Engineers
- Year
- 1996
- Tongue
- English
- Weight
- 884 KB
- Volume
- 42
- Category
- Article
- ISSN
- 0001-1541
No coin nor oath required. For personal study only.
β¦ Synopsis
A mathematical model was formulated to describe the reaction rate and the particle size distribution of solids in a Puidized bed for the chlorination of rutile by a CO/CI, mixture. The bubble assemblage model was applied to describe the gas behaLRor in the bed. The particle-size distribution in the bed was determined by a population balance. Predictions of the model gave satisfactoiy agreement with experimental results. The effects of important variables such as superficial gas velocity, exchange rate between the phases, and the reaction-rate constant were evaluated.
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Corrosion of steel bars in concrete may start when the concentration of free chlorine ions in the liquid phase of the pores exceeds a certain threshold level causing depassivation of the bars. The physicochemical processes of diffusion of CI-in the aqueous phase of the pores, their adsorption and bi