The application of the dispersion model of flow reactors for reactions of any order with two reactants and different initial concentrations yields a system of differential equations which can by considering the stoichiometry of the reaction be reduced to one differential equation. The numerical sol
The role of axial dispersion in trickle-flow laboratory reactors
β Scribed by David E. Mears
- Publisher
- Elsevier Science
- Year
- 1971
- Tongue
- English
- Weight
- 342 KB
- Volume
- 26
- Category
- Article
- ISSN
- 0009-2509
No coin nor oath required. For personal study only.
β¦ Synopsis
Axial dispersion or backmixing appears to be responsible for adverse mass velocity effects observed in trickle-flow laboratory reactors. At low Reynolds numbers typical of bench-scale units, the dispersion problem can be at least an order-of-magnitude more severe in trickle-flow than vaporphase operation.
A simple perturbation criterion is derived for the minimum reactor length required for freedom from significant axial dispersion effects. It shows that the minimum length increases with both conversion and reaction order, and is inversely proportional to the Bodenstein number.
π SIMILAR VOLUMES
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Two hydrodynamic models of the hquld m a trtckle-bed reactor PE and PDE model, have been consldered, and the Influence of the ldentlficatlon method on the parameter values was exammed The employed ldentlticatlon methods were the moments method, supplemented by graphlcal determmatlons on the response