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THE UNSTEADY-STATE SOLUTION FOR A FINITE DISPERSION-TYPE CATALYTIC PACKED-BED TUBULAR REACTOR

Korean Journal of Chemical Engineering, September 1985, 2(2),
10.1007/BF02697498
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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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