Pressures in a circulation loop under various conditions were measured in a
cold mode (a riser of 35 mm I.D. x 5450 mm high and a fluidized reactor of
160 mm I.D. x 1250 mm high) with particles of mean diameter of 78 mum, and
bulk, and particle densities of 1.03, and 1.90 g/cm(3), respectively, Soli
d circulation rates were measured with a load cell hopper. The particle hol
d-ups at various sections were analyzed from differential pressure data. Th
e voidage in the riser reactor increases with the increase in gas velocity,
even though the solid circulation rate increases with gas velocity. The so
lid circulation rate increases to a maximum with gas velocity at the riser,
and levels off because the non-mechanical valve adopts the role of solid r
ate determining step in the circulation loop of the system. Particle hold-u
p in the riser reaction zone increases by using an underflow standpipe loop
seal below the fluidized reactor instead of an overflow standpipe loopseal.