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Simulation of the Industrial Packed Bed Catalytic Reactor for the Partial Oxidation of Methanol to Formaldehyde:

✍ Scribed by Moustafa, T. M.


Publisher
Curtin University of Technology
Year
2008
Tongue
English
Weight
486 KB
Volume
11
Category
Article
ISSN
0969-1855

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A reactor model for a downer-regenerator circulating fluidized-bed (CFB) during the partial oxidation of n-butane to maleic anhydride is presented. Upflow reactors (risers) suffer from severe solids back mixing and gas-solids-separation, in comparison down flow reactors exhibit a more uniform gas-so