According to the
design and operational parameters of
the cyclone
liquid slag-discharging boiler, an experimental platform for the cyclone
burner was designed and constructed in a cold state based on the principle
of similarity. The experimental study investigated the effects of
parameters, such as swirl-vane angles, coal concentration, operating
parameters, and particle size, on the flow distribution and vertical
riser resistance characteristics of the vertical cyclone burner. The
results showed that there were differences in flow distribution among
the cyclone burners, and the most uniform flow distribution was achieved
when the swirl-vane angle of the primary air was 30°. The concentration
of pulverized coal significantly influenced the pressure drop in the
vertical ascending section, which increased with higher concentrations
of pulverized coal. When the concentration of pulverized coal remains
constant, the pipeline pressure drop is minimized at a primary air
velocity of 7.5 m/s. As the secondary wind speed increased, the pressure
drop consistently rose; when the secondary wind speed is 22 m/s, the
pressure drop of the pipeline is the maximum; however, excessively
high secondary wind speeds were found to be detrimental to the formation
of an optimal aerodynamic field in the burner. Furthermore, when the
pulverized coal concentration was held constant, materials with larger
particle sizes exhibited the highest pressure drop. When the particle
size increases from 50 to 150 μm, the pressure drop of the vertical
riser segment also increases. Finally, based on the Barth additional
pressure drop theory, the pressure drop formula of the vertical riser
is fitted by a dimensional analysis method, and the correlation formula
of the pressure drop test of gas–solid two-phase flow in the
vertical riser is obtained.