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Chapter 10: Catalysis and Catalytic Reactors
Additional Homework Problems
CDP10-OB
Benzene and propylene are produced form the cracking of cumene over a silica-alumina catalyst. Unfortunately, a trace amount of cumene hydroperoxide can deactivate the catalyst. The reaction is carried out in a batch reactor at a temperature sufficiently high that the adsorption constants of reactants and products are quite small. The reactor is charged with 0.1% cumene hydroperoxide, 90% N2. and 9.9% cumene at a pressure of 20 atm. The following data were obtained in a well-mixed batch reactor with a catalyst concentration of 1 kg/m3.
t(s) | 0 | 10 | 20 | 30 | 40 | 60 | 80 | 100 | 150 | 200 | 300 | 500 | 750 | 1000 |
% Conversion | 0 | 3.7 | 7.1 | 10.2 | 13.0 | 18.0 | 22.3 | 25.9 | 33.0 | 37.9 | 44.1 | 49.3 | 51.2 | 51.7 |
Determine the reaction order and rate constant with respect to cumene. Determine the order of decay and the decay constant as well (Ans: First-order, k = 6.63 * 10-5 s-1)
[3rd Ed. P10-23]