(273d) Effects of Pressure and Fines Content On Bubble Diameter in a Fluidized Bed Studied Using Fast X-Ray Tomography
AIChE Annual Meeting
2012
2012 AIChE Annual Meeting
Particle Technology Forum
Fundamentals of Fluidization II
Tuesday, October 30, 2012 - 1:30pm to 1:50pm
Using a fast X-ray tomography setup the bubble size and
velocity has been measured in a 25 cm diameter fluidized bed of Geldart B
powder and a 24 cm bed of Geldart A powder. The average bubble size has been
determined for a measurement period of 60 seconds. The resolution of this setup
is about 4.5 mm per pixel at a rate of 250 reconstructions per second. It is
possible to detect bubbles as small as 2.2 cm. The Geldart B powder consisted
of polystyrene particles with an average diameter of 607 mm and a bulk density of 625 kg/m3.
This bed was studied at pressures ranging from 1 to 5 bar.
The superficial gas velocities varied from 12 to 32 cm/s for the atmospheric
pressure measurements; for the highest pressure from 10 to 15 cm/s. The bubble
size is significantly reduced at higher pressures for similar gas flows. The
Geldart A powder consist of a base of aluminum oxide
particles with an average diameter of 76 mm
and a bulk density of 680 kg/ m3. Varying amounts of fines were
added to these base particles. The fines consist of aluminum oxide particles with
an average diameter of 38 mm and a bulk
density of 620 kg/ m3. An increase in the fines content from 0 to
50% weight leads to a decrease in the average spherical equivalent
bubble diameter by 20%.
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