In this study, 11
coal mono-combustion tests and four co-combustion
tests of coal and tannery sludge were conducted on a 35 kW fluidized-bed
combustor. The combustion behavior and emission characteristics of
the fuels were investigated on a bubbling fluidized bed (BFB) and
a circulating fluidized bed (CFB). The effects of an excess air ratio,
primary air rate, secondary air ratio, and fuel type on flue gas emissions
were studied. The results showed that the fluidization status and
temperature distribution had direct influences on CO emission. Sufficient
fluidization and high temperature effectively reduced CO emission.
NO
x
emission was relatively sensitive
to the excess air ratio and increased with increasing excess air ratio.
By comparing BFB and CFB, we found that CFBs have an advantage in
optimizing combustion and controlling emissions by enhancing mixing
and increasing freeboard temperatures. The Cr speciation and distribution
among different ash types were extensively investigated in four co-combustion
tests. The results showed that the distribution modes of Cr in BFBs
and CFBs were different and determined by separate fluid dynamics
modes of sludge ash particles in the combustor. The extent of Cr oxidation
in ash in CFB tests was higher than that in BFB tests, particularly
for bottom ash and heat exchanger ash, due to longer residence times
in high-temperature regions.