The gas lateral mixing in the distributor region of a fluidised bed is stud
ied by means of injecting a tracer axially in the cold model of an oxychlor
ination reactor. The horizontal spread of the tracer concentration is also
related to the fluidisation regime, which is characrerised by pressure fluc
tuation measurements.
The tracer concentration at the bed wall increases with the fluidising velo
city and reaches its maximum when turbulent fluidisation is approached. The
experimental observations are well explained by the model proposed by Rowe
[1] to characterise gas flow in the entry region of a fluidised bed chemic
al reactor. (C) 2000 Elsevier Science S.A. All rights reserved.