Experimental data on the attrition of fluidized cracking catalyst (FCC
) powder in the jetting region of a fluidized bed indicate that the at
trition rate is proportional to the orifice velocity raised to the pow
er 3. This dependence is analysed here by coupling the kinetics of att
rition, based on single-particle impact attrition testing, with a hydr
odynamic model of the jetting region, from which the profiles of parti
cle velocity and concentration can be calculated. It is shown that the
approach predicts a power index which is in reasonable agreement with
the experimental data, and it can therefore identify the relative con
tributions to attrition arising from the material response and jet hyd
rodynamics.