The main purpose of this study was to examine the effect
of particle
size on blending methods for pulverized coals, using a thermo-gravimetric
analyzer (TGA) and an entrained drop tube reactor (EDTR). The experiment
was performed with three particle sizes (small: 45–75 μm,
medium: 75–90 μm, large: 150–180 μm) and
two blending methods (bunker-blend and furnace-blend). The TGA results
show that high rank coal (Trafigura), containing lower volatile matter,
was more difficult to ignite than low rank coal (Berau). Also, faster
ignition and higher reactivity were observed because of increase in
the surface area with decreasing particle size. The EDTR results show
that first, during bunker-blend, as the particle size decreased, the
amount of carbon in ash (CIA) reduced. Moreover, the highest point
of CIA shifted to a low blending ratio (LBR 50%) because a highly
oxygen-deficient environment was rapidly created. In contrast, as
the blending ratio of low rank coal increased, NO
x
emissions gradually increased at all conditions because of
the fuel bonding N content in the coal, and the NO
x
reduction efficiency of a fine particle is larger than that
of a coarse one. Second, during furnace-blend, CIA and NO
x
gradually decreased by approximately 33–52%
(small sizes) and 9–27% (medium sizes) as the length of the
tube increases. However, for the large sizes of coal, the amount of
CIA and NO
x
increased because of the adverse
effects of the greater particle size. The CO and O2 results
among flue gases supported these phenomena. Thus, these results suggest
that using fine particles in furnace-blend can effectively reduce
CIA and NO
x
emissions.