The hydrodynamic
behavior of particles
in a 3D integral multi-jet spout-fluidized bed has been studied experimentally
by particle image velocimetry method. In the cross section of the
spouted bed, especially in the annulus, it was found that particle
movement can be effectively promoted by adding the integral multi-jet,
thus enhancing the radial movement of particles in the annulus and
effectively eliminating the dead zone of particle flow in the annulus
region. With the decrease of particle handling capacity, the fluidization
effect of multi-jets was improved. When the static bed depth was 0.165
m, the enhancement effect of multi-jets on the movement of particles
in the spouted bed would be optimal. When the particle diameter was
overly small, the fluidization effect of the side jet would be relatively
low, while excessive particle diameter would weaken the fluidization
effect of the side jet due to the rise in the inertia force of particles.
The analysis of the average turbulent kinetic energy and radial velocity
of the particles revealed that when the particle diameter is equal
to 0.72 mm, the strengthening factor of movement of particles (η)
reaches the peak, the turbulence fluctuation of particles in the annulus
region reaches the highest, and the fluidization effect of side jets
on the particles is the best.