The helical flow promoter (HFP), inserted in the downcomer of an airlift re
actor (ALR), generates a helical flow pattern in the circulating gas-liquid
(solid) mixture. Data on the fluidization capacity, gas holdup, liquid vel
ocity and mass transfer rate for two- and three-phase systems with two diff
erent carboxymethylcellulose solutions collected in a 58 L ALR-HFP are pres
ented and compared with those of common pneumatic reactors. Generally, an i
ncreasing solid concentration led to a slight decrease in gas holdup and li
quid velocity but to a considerable decrease in mass transfer rates. Insert
ion of HFPs produced a significantly enhanced fluidization capacity of soli
d particles compared to the common systems.