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Optimal temperature profiles in a tubular reactor for a system of consecutive – competing reactions: A + B → RR + B → S

✍ Scribed by A. Burghardt; J. Skrzypek

Book ID
103004689
Publisher
Elsevier Science
Year
1974
Tongue
English
Weight
367 KB
Volume
29
Category
Article
ISSN
0009-2509

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✦ Synopsis

f effectiveness factor for pore diffusion plus reaction G mass velocity h external heat transfer coefficient k first order reaction rate constant k, external mass transfer coefficient K overall coefficient for transfer plus reaction K* overall coefficient based on average value of k, I? overall coefficient corrected for distribution of k, NP.

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Ah&a&-We study the dimensionless heat and mass balance equatibns describing a continuous stirred tank reactor in which there is occurring consecutive first order exothermic reactions. A~~~ ~ymptotic ~c~ations and muner$g calculations are presentqd for both steady states and oscillatory states. A for