A simplified turbulent model and a modified k-<INF></INF> epsilon two equat
ion model are proposed to describe the liquid velocity profiles in a bubble
column taking into consideration of the effect of gas drag force and gas h
old-up. In the simplified model the Reynolds equation of motion was adopted
and the turbulent viscosity was calculated from an empirical correlation w
hich was deduced from our experimental data. The calculated liquid velocity
profiles were compared between the proposed model and the standard k-epsil
on two equation model as well as experimental data. The result shows that t
he proposed model simulates and predicts the liquid velocity held most sati
sfactorily and in good. agreement with the experimental measurement.