Ozonation of wastewater from olive related industries has been carried out
after dilution with synthetic urban wastewater. The advantages of the appli
cation of different acidic and basic cycles during the ozonation process ha
ve been shown. Biodegradability of the final effluent measured as the biolo
gical oxygen demand to chemical oxygen demand ratio has significantly been
increased (100-144% for table olive wastewater and 24-60% for olive oil was
tewater). Aerobic biological experiments conducted by using non-acclimated
microorganisms confirmed the suitability of the biodegradation after the ch
emical oxidation pre-treatment. A kinetic model based on a free radical mec
hanism has been used to simulate experimental results. Both chemical oxygen
demand and dissolved ozone concentration profiles are well fitted by the m
odel. The aerobic biodegradation process has been modeled by utilizing the
Monod equation.