
First-order catalytic reaction of A → B with -r'''A = k'''CA in a BFB reactor.
Reactant gas (cA0 = 100 mol m-3) passes upward through a 2 m diameter fluidized bed (εmf = 0.5, alpha = 0.33 and D = 20x10-6 m2 s-1) containing solid catalyst particles (ρs = 2000 kg m-3).
Velocity of bubbles: ubr = m s-1 and ub = m s-1
Model validation: ub/uf =
Height of bed: HBFB = m
Conversion: xA = and cA = mol m-3