The photocatalytic oxidation of benzoic acid was investigated in a pilot sc
ale-cascade photoreactor. The photoreactor consists of an array of UV lamps
(40 W, 365 nm) illuminating a cascade of three inclined 316 stainless stee
l plates, on which titanium dioxide (TiO2) was immobilized by electrophoret
ic deposition. The percentage removal of total organic carbon (TOC) of liqu
id samples was determined. The photocatalytic process was affected by sever
al operating parameters. Increasing the solution temperature was found to r
educe the dissolved oxygen (DO) level and to decrease the rate of the degra
dation process. The Langmuir-Hinshelwood equation was found to be accurate
for modeling the degradation of benzoic acid with initial concentrations of
50 ppm, 75 ppm and 100 ppm. The rate of removal of TOC was positively affe
cted by UV light intensity, but appeared to be independent of solution flow
rate in the range examined. Control experiments confirmed that the effects
of adsorption of the solute onto the TiO2 catalysts and photolytic degradat
ion were negligible.