In
the present study, a double-eccentric design for the
vortex
finder of a cyclone separator was proposed to enhance the cyclone
performance. Using the numerical approaches, the flow field inside
the cyclone was simulated and the cyclone performance was evaluated.
The orthogonal method was adopted to obtain the optimal structure
of the double-eccentric vortex finder. The range analysis of the five
key geometric factors in the double-eccentric design was also conducted.
It was found that cyclone performance is more sensitive to the eccentricity
of the vortex finder than the other factors. The best eccentric angle
of the inlet of the vortex finder is 270°, which markedly improves
the separation efficiency and slightly increases the pressure drop.
The simulated flow field depicted that the double-eccentric vortex
finder results in the strongest swirling flow in the middle and lower
parts of the cyclone compared with the vortex finders of the original,
non-eccentric, and single-eccentric designs. The results also reflected
that off-centering the vortex finder has the most significant impact
on the flow patterns. Moreover, an industrial test was carried out
in a circulating fluidized bed boiler for this novel vortex finder.
The fly ash of the double-eccentric vortex finder becomes finer and
contains less carbon content than that of the original one, which
indicates that the double-eccentric vortex finder successfully enhances
the separation performance.