The decomposition of cyclohexane to benzene and hydrogen is mass transfer limite
ID: 789321 • Letter: T
Question
The decomposition of cyclohexane to benzene and hydrogen is mass transfer limited at high temperatures. The reaction is carried out at 2 atm and 500oC in a plug-flow packed-bed catalytic reactor, 50 cm in internal diameter. The reactor is packed with spherical catalyst pellets that are 1 cm in diameter. The bed porosity is 40%. The feed entering the reactor is 20% cyclohexane and 80% hydrogen at a volumetric flow rate of 60 liters per minute. You may assume that the value of the mass transfer coefficient, kG, is 0.40 cm/min. Calculate the length of reactor necessary to achieve 90% conversion of cyclohexane ?
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