## INTRODUClTON The advantages of a spouted bed are well known for physical processes with coarse particles. These. processes involve drying, particle coating, granulation and heat transfer operations (Mathur and Epstein, 1974). The fluid from an inlet orifice penetrates through a bed of particle
Gas phase solid-catalysed chemical reaction in spouted beds
β Scribed by G. Rovero; N. Piccinini; J.R. Grace; N. Epstein; C.M.H. Brereton
- Publisher
- Elsevier Science
- Year
- 1983
- Tongue
- English
- Weight
- 753 KB
- Volume
- 38
- Category
- Article
- ISSN
- 0009-2509
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β¦ Synopsis
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 catalyst particle sire, bed depth, spouting velocity. and reaction rate constant (varied by adjusting the hed temperature). The use of a photometric analyser allowed analysis of concentrations at the inlet and exit from the ted, at different radial positions at the bed surface, and at several positions within the bed itself. Very little effect of particle size was found over the range studied (2.58 to 4.38 mm). Contrary to previous expectations, the conversion was found to decrease as the bed diameter wss increased.
The concentration gradients observed in the annulus indicate that the streamtube model is superior to the one-dimensional model, despite the fact that overall conversions predicted by these previously derived models are again simll. The observed gradients were not, however, as pronounced as those predicted by the streamtube model, and this suggests that radial dispersion in the annulus cannot he entirely neglected.
π SIMILAR VOLUMES
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 applicati
## 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
Volumetric thermal capacity of solids is higher than that of gases by three orders of magnitude. We show that this leads to a dynamic response of a fixed bed reactor involving a solid phase reaction which is sluggish compared to that involving a gas pha~ reaction of the same kinetic and thermodynami
## Abstrset -A multitubular catalytic fixed bed reactor for the oxidative coupling of methane is designed. A heterogeneous two-dimensional reactor model taking into account axial dispersion of mass and enthalpy is applied. A reaction network consisting of 36 gas phase radical reactions and 10 cata