## Abstrati -The performance of a 0 15 m diameter spouted bed reactor has been studled for decomposltlon of ozone on Iron oxide catalyst The vmables Include bed depth. catalyst parWe sue and spoutmg gas velocity The spouted bed conversion data are compared agamst predIctIons from theoretical model
Vapour phase chemical reaction in spouted beds: A theoretical model
โ Scribed by Kishan B. Mathur; C.J. Lim
- Publisher
- Elsevier Science
- Year
- 1974
- Tongue
- English
- Weight
- 714 KB
- Volume
- 29
- Category
- Article
- ISSN
- 0009-2509
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โฆ Synopsis
A theoretical model of a spouted bed chemical reactor, involving vapour phase reaction in the presence of catalyst or heat carrier particles, is proposed. The hydrodynamic features relevant to the model are described in as generalized a manner as permitted by the available information. The application of the model is then demonstrated by making certain predictions concerning the effect of the major variables on gas conversion for a first order reaction, as well as on the relative performance of spoited, fixed, and fliidized bed systems.
๐ SIMILAR VOLUMES
## Abets&-Previously reported experimental work on the decomposition of ozone in a 0.15 m diameter spouted bed of angular ion oxide catalyst particles has been extended to spherical catalyst particles in both 0.15 rn and 0.22 m dia. columns. Other variables, aside from cohunn diameter, included ca
Relationships giving spout diameter as a function of height are developed for both twodimensional and cylindrical spouted beds, and tested against experimental data selected from the literature. The required input information includes the average spout diameter and the spout expansion angle. The for
P, in Fig. 1 (p. 1618) should be p,,g, and the isolated g should be deleted. (1 + r:)"" in eq. ( 25) (p. 1621) should be (1 + r:\*)"\*. C, in eq. ( 31) (p. 1621) should be C,H, and +C,(l -C:)"\* should be -C,(l -C:)"'. The last exponent, l/2, in both eq. ( 34) and eq. ( 36) (p. 1621) should be -l/2