We have investigated the self-diffusion in a stable gas-fluidized bed of fi
ne powder. Two regimes have been observed: for gas velocities v(g) above th
e minimum fluidization velocity v(m) and below a critical gas velocity v(c)
smaller than the minimum bubbling velocity v(b) the powder does not mix. E
xperimental measurements show the existence of yield stresses in this regim
e which are responsible for the static behavior of the bed. For v(g) > v(c)
the yield stress vanishes: the bed behaves like a fluid and displays a dif
fusive dynamics. In this region we have found that the diffusion coefficien
t D increases with gas velocity until the bed expansion approaches its maxi
mum value.