In this work, the
agglomeration, fragmentation, and separation
process of coarse-grained pulverized coal agglomerates (CGPCA) obtained
from a power plant were achieved using gas–solid fluidized
bed sorting and analyzed through a combination of numerical simulations
and actual experiments with CGPCA. To study the polydispersity and
irregularity of CGPCA, the CGPCA surface fractal dimension was calculated
using fractal dimension combined with scanning electron microscopy.
The two-section fractal dimension of the particle size distribution
was obtained by fitting the logarithmic particle size distribution
of CGPCA. On the basis of the obtained data, the polydisperse particle
drag force model, the agglomeration kernel function, and the breakage
kernel function were modified. Thus, an irregular polydisperse gas–solid
two-phase Eulerian–Eulerian model was constructed to simulate
the sorting process of CGPCA in the fluidized bed. The results of
the numerical simulation investigation were compared with the experimental
results and showed that the simulation data, which considered the
two section fractal dimension, was in better agreement with the experimental
results. The cumulative logarithmic distribution of CGPCA’s
size was segmented and fitted. The values of the two section fractals
of the agglomerates were determined as
D
= 1.014
and
D
= 2.401, respectively. Analysis revealed that
the optimal separation efficiency working condition in the simulation
process, providing the highest separation efficiency of 54.7%, was
generated at air velocity of 1.21 m/s.