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Modeling of chemical reactors—XXIX mixing-cell model for packed bed reactors. Steady state considerations. Problems of multiplicity

✍ Scribed by J. Sinkule; V. Hláv̌acek; J. Votruba; I. Tvrdík

Publisher
Elsevier Science
Year
1974
Tongue
English
Weight
468 KB
Volume
29
Category
Article
ISSN
0009-2509

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✦ Synopsis

The axial heat and mass transfer in tubular catalytic reactors may be described by mixingcell model and diffusion model as well. The diffusion description yields for a strong exothermic reaction and adiabatic conditions three steady state profiles, on the other hand the mixing-cell model gives rise to more than three steady states. A simple numerical and graphical analysis for mixing-cell model is presented.

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