In this study, the
combustion and emission characteristics of slurry
from an Indonesian lignite washery tailing (LWT) and a bituminous
coal were studied and compared in both a bubbling fluidized bed (BFB)
and a circulating fluidized bed (CFB). The effects of excess air ratio,
feeding rate, secondary air ratio, and secondary air location on the
flue gas emissions were analyzed to investigate the optimal operating
conditions. The results show that it is feasible to directly fire
LWT slurry in a CFB. The temperature of the dense-phase bed firing
the LWT slurry can reach 800 °C but is lower than that of a normal
BFB/CFB firing coal. Both SO2 and NO emissions of bituminous
coal are higher than those of LWT slurry, but their emission characteristics
are still below the limits for both EU and Chinese regulations. Improved
emission characteristics are observed when firing LWT slurry and coal
in CFB compared to BFB. Two main differences were found between LWT
slurry and coal: (1) Low primary air (PA) flow rates facilitate the
defluidization of the FB combustor when firing LWT slurry. (2) High
feeding rates of LWT slurry may reduce the temperature along FB instead.
These factors should be paid special attention when designing and
operating an FB system. Optimal secondary air (SA) ratios were determined
for both LWT slurry and coal. The SA should not be located near the
distributor. All of the analyses in this study provide useful information
for the design and operation of a commercial FB system.
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