Slag tapping cyclone furnace is suitable and promising
for the
utilization of low-ash-melting-point coals without worrying about
the fouling and slagging problems, but its high NO
x
emission has limited its application. In this study, the temperature
profiles, species concentration distributions, and slag tapping behavior
of the cyclone barrel were explored on a self-built 100 kW cyclone
furnace system. A reasonable slag capture ratio of 0.70 can be achieved
for the cyclone barrel even under air-staged conditions. The coincidence
of high temperature and high O
2
concentration in the annular
near-wall area of the cyclone barrel can lead to a large amount of
NO
x
formation, while a NO
x
reduction area with high CO concentration is formed
in the central and lower zones of the cyclone barrel due to strong
swirling effect. The NO
x
emission of cyclone
staged combustion is lower than that of laminar drop-tube staged combustion
in either air-staged or nonstaged cases, which could be attributed
to the swirling effect. The NO
x
reduction
area can be expanded by decreasing the cyclone stoichiometric ratio
(
SR
) or reducing the primary air rate (
PAR
). Compared with the limit effects on the reduction of NO
x
emission by overall-
SR
, NO
x
formation can be greatly dropped by 56%
when the cyclone-
SR
decreases from 1.1 to 0.7. The
swirling intensity in cyclone barrel increases from 1.23 to 12.81
as
PAR
reduces from 0.4 to 0.2, which results in
a reduction of NO
x
formation at the outlet
of the cyclone barrel by half. Besides, the O
2
concentration
in the annular near-wall region can be remarkably reduced by the decentralized
secondary air supply, resulting in a 23% reduction in NO
x
formation in the cyclone barrel.