The mass transfer in the air-water system was investigated for various sing
le- and twin-impeller systems including the standard Rushton impellers, pit
ched-blade impellers, concave-blade impellers and comb-blade impellers. For
twin-impeller systems, the effects of the two impellers operating at vario
us speed combinations, opposite impeller rotation and alternate impeller ro
tation were investigated. Results showed that although slightly better perf
ormance was achieved by using the concave-blade and comb-blade impellers, a
ll the volumetric mass transfer coefficients, k(L)a, obtained were mainly d
etermined by the specific power consumption (P/V) and the superficial gas v
elocity (U-s) and correlated reasonably well by a single correlation due to
van't Riet. The possible reason for the better performance of the comb-bla
de impellers is discussed.