The decomposition of H2O2 by a novel supported gamma-FeOOH catalyst was per
formed in a continuous fluidized-bed reactor. This catalyst has been succes
sfully used in the treatment of organic contaminants with H2O2 in our previ
ous work. In this study, we attempted to determine the effects of pH, H2O2
concentration, and catalyst concentration on the decomposition of H2O2 An a
pproach, we regarded this reactor as a continuous-flow stirred-tank reactor
, was applied to investigate the kinetic behavior. At low H2O2 concentratio
n, the decomposition rate of H2O2 was found to be proportional to both H2O2
and catalyst concentrations. At high H2O2 concentration, however, the rate
decreased with the increasing H2O2 concentration. This can be explained by
the substrate inhibition model. The large difference in the observed first
-order rate constants under various pH values was also modeled. The model a
greed well with the experimental results. (C) 1999 Elsevier Science B.V. Al
l rights reserved.