Circulating fluidization of slender particles is used widely in industrial production
for example
combustion of biomass stalks and drying or wetting of cuttobaccoThe movement attitude of slender particles is more complicated than that of the spherical particle owing to the slender particles〖DK〗’six degrees of freedom
and thus there are some differences in fluidizing behavior between slender particle and spherical particleNumber concentration is one of the most important features of fluidizing behavior of slender particlesBased on the direct simulation Monte Carlo (DSMC) method
rigid body dynamics and momentum conservation law
a three-dimensional motion model of slender particles
including the inter-particle collision mathematical model
was establishedThe gas-solids flow in an actual circulating fluidized bed was simulated by using the current model
and some number concentration features of slender particles were capturedIn the experimental riser
among all the slender particles
the slender particles with less slenderness firstly arrived at the exit from the near wall regions of the riserThere existed such evident phenomena as floc
migration and so on in the process of fluidizationIn the fluidization state
the number concentration of slender particles did not change evidently with entrance air speed.