Abstract (EN):
The effect of intraparticle forced convection on a heterogeneous reaction within a catalyst pellet is studied. The extended dusty gas model is used to describe mass transport for a first-order, irreversible, isothermal reaction with mole changes within a slab-geometry catalyst pellet. Four dimensionless parameters are introduced and studied: the Thiele modulus, phi; the ratio alpha between the Knudsen and effective diffusivities; the ratio beta between the viscous momentum and molecular diffusivity; the normalized external pressure drop Delta f. Results show that pressure gradients can exist within the pellet, as a result of the reaction stoichiometry and the external pressure gradient. The effectiveness factor is not only dependent on the Thiele modulus and on the change in moles, but it is also dependent and enhanced by intraparticle forced convection.
Language:
English
Type (Professor's evaluation):
Scientific
No. of pages:
14