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Approximation of the dynamical model of fixed bed reactors via a singular perturbation approach

✍ Scribed by D. Dochain; B. Bouaziz


Publisher
Elsevier Science
Year
1994
Tongue
English
Weight
458 KB
Volume
37
Category
Article
ISSN
0378-4754

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✦ Synopsis


In this paper, we propose to study the dynamics of fixed bed reactors with axial dispersion in the general case of a non-isothermal process involving N components and M reactions. It will be shown by using singular perturbation that for large dispersion coefficient values, the fixed bed reactor tends to a stirred tank reactor. Singular perturbation results in a series expansion of the state variables (component concentrations and temperature). The computation will be carried out up to the first order. The dynamical equations of the zero order approximation are the those of the corresponding stirred tank reactor.


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Abstraet--A mathematical model for the startup period of a fixed-bed reactor with first-order reaction kinetics, axial dispersion and film mass transfer resistance was formulated and solved analytically using Laplace transform. The solution can be used to correlate or predict the reactant concentrat