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.