The use of ozone in water and wastewater treatment systems has been shown t
o be a process that is limited by mass transfer. The most effective way to
overcome this limitation is to increase the interfacial area available for
mass transfer by decreasing the size of the ozone gas bubbles that are disp
ersed in solution. Electrostatic spraying (ES) of ozone into water was inve
stigated in this work as a method of increasing the rate of mass transfer o
f ozone into a solution and thereby increasing the rate of phenol oxidation
. The studies were conducted in a 30 cm column of 7.5 cm internal diameter,
using deionized water and phenol as the solution phase and an ozone-oxygen
mixture, generated by a corona-discharge ozone generator, as the gas phase
. Results were obtained for ES at input power levels ranging from 0 to 4 kV
and compared with two different pore-size bubble diffusers (10-15 mu m and
40-60 mu m). It was determined that the rate of mass transfer could be inc
reased by as much as 40% when the applied voltage was increased from 0 to 4
kV as a result of the smaller bubbles generated by ES. In addition, ES was
shown to be more effective than the medium-pore-size (10-15 mu m) bubble d
iffuser; the best results were achieved at low gas flow rates. Phenol oxida
tion rates were also compared for ES and the medium-port-size bubble diffus
er, and the results indicate that the increased mass transfer rate achieved
by ES enhances the rate of removal of phenol from solution. (C) 1999 Elsev
ier Science B.V.