As a preamble to combustion studies, the fluidization characteristics
of heterogeneous auto fluff were investigated in a Plexiglas test faci
lity which simulates the bench-scale combustion/agglomeration unit at
the Institute of Gas Technology (IGT). The latter bench-scale unit (BS
U) has a central jet burner, sloping grid, and classification zone to
control the process of ash agglomeration. A solids feeder system was d
esigned which could successfully feed the heterogeneous auto fluff at
an appropriate uniform feed rate to sustain its combustion with an aux
iliary fuel gas. During some of the tests, it was found that at least
a part of the natural gas fed to the central jet burner and auto fluff
volatiles burned above the bed surface. Venturi and grid gas velociti
es, hot zone and bed temperature levels, turbulence, and solids circul
ation are some of the important parameters that need to be considered
for the formation and controlled growth of ash agglomerates. In order
to establish the influence of operating parameters on the formation of
ash agglomerates, the hot zone and bed temperatures and the venturi t
o grid flow ratios were varied in this work. It was found that operati
ng the bed with venturi gas velocity around minimum spouting created b
etter solids circulation and hot zone conditions for agglomerate growt
h. This was confirmed by run 2 when the bed did not clinker and the av
erage bed particle size was much above that for the other two runs con
ducted implying agglomerate formation. Clinker refers to fused bed mat
erial that blocks gas flow and thereby prevents uniform fluidization.