Dry
coal beneficiation has played a vital role during the initial
stage of coal cleaning in recent years. Successful utilization of
a gas–solid fluidized bed for >6 mm coal cleaning motivates
scholars to explore the possibility of fine coal cleaning using dry
beneficiation methods. In this study, pulsed flow was introduced into
a fluidized bed to optimize bubble behavior, thus improving the density
stability. The equation of minimum fluidization velocity (
U
mfp
) in a gas-vibro fluidized bed for coal preparation
was investigated theoretically. An equation has been proposed for
predicting
U
mfp
while considering changes
in the friction coefficient (
C
f
) in the
gas-vibro fluidized bed. Based on two-phase theory, the correlation
of bed density was determined by analyzing the bubble behavior in
the gas-vibro fluidized bed. The theoretical bed density was then
compared with experimental data of the bed density and separation
density. The predicted bed density in monodisperse and binary dense
medium systems was found to be consistent with the experimental results.
Overall, the equation of bed density is suitable for estimating the
separation density in the gas-vibro fluidized bed.