The cumene c9h12 a cracking reaction to form benzene c6h6


Intra-particle diffusion in catalyst particles

1. The cumene (C9H12) (A) cracking reaction to form benzene C6H6 (B)is often used as a model reaction for determining the relative activities of cracking catalysts:

C9H12 → C6H6 + C3H6

A → B + C

The reaction takes place on silica-alumina catalyst in the temperature range of 300°C to 600°C. Calculate the combined diffusivity DA’ and effective diffusivity DeA of cumene in a mixture of benzene and cumene at 1 atm total pressure and 510°C within the pores of a TCC (thermal cracking catalyst) bed assuming equimolar counter diffusion applies. Report you answers in units of cm2 /s

TCC catalyst data:

SG = 342 m2 /g

eS = 0.51

eq. catalyst dia. Dp = 0.43 cm

ρp = 1.14 g/cm3

R = 8.314 J/mol·K

A narrow pore size distribution and tortuosity factor of 3 may be assumed. Use of methods by Poling et al. suggest ordinary (molecular) diffusion DAB = 0.150 cm2 /s. Confirm the assumption of narrow pores such that the Knudsen diffusion term is dominant.

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