In this study, the use of a cocurrent downflow jet pump contactor for
possible ozone disinfection was demonstrated. The results showed that
this type of reactor has an advantage over conventional contactors suc
h as bubble columns and U-tube columns since it showed a high mass tra
nsfer coefficient. Interestingly, the mass transfer coefficient is fou
nd to be nearly independent of the gas to liquid volumetric flow ratio
(Q(G)/Q(L)). The explanation and the empirical correlation for mass t
ransfer coefficient (k(L)a) also are described in this paper.