The
effect of liquid addition on the gas–solid flow characteristics
in a spouted fluidized bed reactor is investigated from multiple scales
using a coupled computational fluid dynamics-discrete element method.
First, to address the problem that most studies only consider capillary
force, this work proposes a liquid bridge model that includes both
the capillary force and viscous force. Then, the microscopic mechanism
of liquid action is investigated for multiscale analysis. The microscale
study reveals that the increase of liquid content and viscosity will
lead to the increase of the liquid bridge strength between particles,
that is, the increase of liquid content leads to the increase of the
liquid bridge capillary force, while the increase of the liquid viscosity
leads to the increase of the viscous force and a decrease in the capillary
force, which also causes a reversal of the dominant interparticle
forces of the particles. Additionally, the number of liquid bridges
and contact points between particles increases due to the increase
in liquid content, while both decrease when the liquid viscosity increases.
The mesoscopic-scale study finds that more liquid content brings about
more large agglomerates and fewer agglomerates. When μ <
50 mPa·s, higher viscosity increases large agglomerates and decreases
small agglomerates. When μ > 50 mPa·s, the reverse applies.
The macroscale study demonstrates that growing liquid content and
viscosity causes a reduction in the bed expansion ratio and the bubble
phase volume. With a multiscale analysis of liquid action mechanisms
from a microscopic perspective, this work can provide an important
reference for the research on liquid-containing systems.