The sonolytic degradation of ozone (O-3) was investigated in both closed an
d open continuous-flow systems to examine effects of mass transfer on chemi
cal reactivity in the presence of ultrasound. Degradation of O-3 followed a
pparent first-order kinetics at frequencies of both 20 and 500 kHz in all t
he systems. Degassing of O-3 was observed at 20 kHz due to the effects of r
ectified diffusion and larger resonant radii of the cavitation bubbles than
at 500 kHz. Increased mass transfer of O-3 diffusing into solution due to
ultrasound as measured by the mass transfer coefficient, k(L)a(2), was obse
rved at both frequencies. At 20 kHz, an increase in mass transfer rates in
the presence of ultrasound may be partially attributed to turbulence induce
d by acoustic streaming. However, the main process of increased gas-liquid
mass transfer in the presence of ultrasonic waves appears to be due to the
sonolytic degradation of O-3 creating a larger driving force for gaseous O-
3 to dissolve into solution. From first-order cyclohexene degradation kinet
ics obtained by sonolysis, ozonolysis, sonolytic ozonolysis, and comparing
the large diameter of an O-3 diffusing gas bubble to the size of an active
cavitation bubble, it appears that diffusing gas bubbles containing O-3 are
not directly influenced by ultrasonic fields.