The hydrodynamic behaviour of airlift reactors strongly depends on the flow
regime in the riser. Representing the slip velocity of the gas as a functi
on of the overall fluid velocity (U-gr + U-lr) in the riser of an airlift r
eactor allows to distinguish between homogeneous and heterogeneous flow reg
imes. The transition between the flow regimes depends on the resistance to
liquid circulation; this resistance has been varied by changing the downcom
er diameter and by inserting a valve on the downcomer. The flow regime also
strongly depends on the initial gas distribution and on the size of the pl
ant: improving the sparger and increasing the column height lead to a more
homogeneous flow. This is confirmed by estimating the parameters of the cla
ssic Zuber and Findlay model for the present results and for these of liter
ature. (C) 1999 Elsevier Science Ltd. All rights reserved.