The catalytic cracking of cumene to benzene and propylene is accomplished using a silica-alumina catalyst. The reaction is 1st order in cumene and the rate constant was measured to be 0.80 cm³/(s*g catalyst). Assume that the catalyst is composed of spherical pellets. The radius of the pellet is 0.16 cm, the density is 1.3 g/cm³ and the effective diffusivity is 0.0008 cm² s²¹. Is the observed rate constant the true rate constant or is there an influence of pore diffusion? Justify your answer.

Introduction to Chemical Engineering Thermodynamics
8th Edition
ISBN:9781259696527
Author:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Publisher:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Chapter1: Introduction
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The catalytic cracking of cumene to benzene and propylene is accomplished using a silica-alumina
catalyst. The reaction is 1st order in cumene and the rate constant was measured to be 0.80
cm³/(s*g catalyst). Assume that the catalyst is composed of spherical pellets. The radius of the
pellet is 0.16 cm, the density is 1.3 g/cm³ and the effective diffusivity is 0.0008 cm² s²¹. Is the
observed rate constant the true rate constant or is there an influence of pore diffusion? Justify your
answer.
Transcribed Image Text:The catalytic cracking of cumene to benzene and propylene is accomplished using a silica-alumina catalyst. The reaction is 1st order in cumene and the rate constant was measured to be 0.80 cm³/(s*g catalyst). Assume that the catalyst is composed of spherical pellets. The radius of the pellet is 0.16 cm, the density is 1.3 g/cm³ and the effective diffusivity is 0.0008 cm² s²¹. Is the observed rate constant the true rate constant or is there an influence of pore diffusion? Justify your answer.
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