Abstract
The unsteady-state solution is obtained by an operator theory in functional analysis setting for a general finite catalytic packed-bed tubular reactor model with axial dispersion in the bed, mass transfer between the catalyst particles and the flowing phase, and intraparticle diffusion and surface reaction in the catalyst particles.
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Kim, D.H., Ma, G.Y. & Chang, K.S. The unsteady-state solution for a finite dispersion-type catalytic packed-bed tubular reactor. Korean J. Chem. Eng. 2, 125–132 (1985). https://doi.org/10.1007/BF02697498
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DOI: https://doi.org/10.1007/BF02697498