Gas holdup and liquid circulation of one conventional draft tube and three
different convergence-divergence draft tubes in an internal loop airlift re
actor were investigated. Experiments were carried out in two-phase systems
with air;water and air-CMC (carboxyl methylcellulose) solution and three-ph
ase system with air-water-resin particles. The two-phase drift-flux model w
as used to estimate gas holdup for three-phase Newtonian and two-phase non-
Newtonian systems. It is shown that gas holdup in convergence-divergence dr
aft tubes is higher than that in a conventional draft tube and increases wi
th superficial gas velocity. Variation of the structural parameters of conv
ergence-divergence draft tubes has little effect on gas holdup in the two-p
hase and three-phase system. The mathematical model, which is based on a dr
ift-flux model, was developed to describe the liquid circulation velocity i
n the reactor satisfactorily.