Widespread application of bubbling fluidised bed reactors to chemical proce
sses has been hindered by some inherent drawbacks, like the high degree of
internal mixing and the low contact efficiency between gas and solid phases
. The staging of fluidised beds through the insertion of horizontal baffles
may overcome these drawbacks, approaching plug-flow and limiting bubble si
ze. The authors, based on theory and experiments, have developed a methodol
ogy to properly design staged fluid bed catalytic reactors, considering gas
and solid backmixing, bubble size, flooding and dynamic forces, which is d
escribed in the paper. (C) 2001 Elsevier Science B.V. All rights reserved.