A comment on “radial mass transfer effects in a porous wall tubular reactor”
✍ Scribed by Mahendra R. Doshi; R. Sankarasubramanian; William N. Gill
- Publisher
- Elsevier Science
- Year
- 1973
- Tongue
- English
- Weight
- 104 KB
- Volume
- 16
- Category
- Article
- ISSN
- 0017-9310
No coin nor oath required. For personal study only.
📜 SIMILAR VOLUMES
An analysis is presented of the concentration protile occurring in a chemical reactor characterized bv radial flow of a fluid between narallel disks. The reaction is the cam&tic oxidation of ethylene on the metal disks and it proceeds at a constant rate because the reactor-is essentially a different
An approximation of the fluid velocity radial profiles within the bed cross-section was taken into account at the numerical solution of the mathematical model of the mass dispersion within the fluid stream, and the effect on the behaviour of the radial Peclet number was analysed numerically and veri
## Ah&act -The mass transfer coel&xent IS predxted for cfiffuslon from a large gas bubble (slug) nsmg m a gas-tidised bed of fine particles cU&uaed m 8 verhcal tube The theory \*) 8 modiiicatma of an ex~stmg result for gas/hqmd systems, to allow for the w&effect tlus IS .s&ca.nt m a gas-fhudwd bed