A novel pilot-plant scale sonochemical reactor (UES 4000 C Pilotstation) ha
s been specifically developed for degrading a variety of water contaminants
in large-scale applications. We report here the sonochemical degradation o
f three chemical compounds in aqueous solution: the chlorinated volatile co
ntaminants dichloromethane (DCM) and trichloroethylene (TCE) and the nonvol
atile azo dye methyl orange (MO). The flow-through reactor in the Pilotstat
ion consists of four 612 kHz piezoelectric transducers which are driven by
a power source operating at 3kW. The sonochemical reaction chamber has a vo
lume of 6 L, while the total capacity of the Pilotstation, including a heat
-exchanger unit and a reservoir tank varies from a minimum volume of 7.25 L
to a maximum over 45 L. The observed reaction rates for the degradation of
these contaminants in the Pilotstation were compared with values determine
d under similar conditions in small-scale bench reactors in order to evalua
te its performance over a wide range of power densities. The pseudo-first-o
rder degradation rate for TCE in the Pilotstation was found to be more than
4 times higher than corresponding smaller values measured in lab-scale rea
ctors. Furthermore, the observed rates for DCM degradation also exceeded th
ose of the small-scale reactors by factors from 3 to 7. The degradation rat
e of these two chlorinated compounds was faster with decreasing initial con
centration in all cases. Experiments with 10 muM MO (aq) in the Pilotstatio
n operating at different total volumes exhibited a linear dependence betwee
n the observed rate constants for sonolysis and the applied power density (
PD), in the range 67 < PD (W/L) < 414. Steady-state . OH (aq) radical conce
ntrations in each reactor were calculated and were shown to correlate with
the applied power, density in the vessel. A power budget analysis for the P
ilotstation indicates that nearly one-third of the applied power is convert
ed in sonochemical activity.