Abstract2,4,6-Trinitrotoluene(TNT) is one of most common toxic pollutant identified in wastewater generated from ammunitions plants. Due to its potential carcinogenic characteristics, TNT presence in water bodies represents a risk for human health and aquatic life. Among modern treatment methods, TiO2 photocatalysis was successfully applied in order to remove toxic pollutants. Fe-TiO2 assisted photocatalytic degradation of TNT in aqueous media, under UV-VIS irradiation was studied. The effects of operating parameters on photocatalytic process performances, kinetic and mechanism of pollutant degradation were investigated. Solutions with (0.27-2.72) x 10 -4 M TNT content were photo-oxidized using a medium pressure Hg lamp as UV-VIS light source (λ = 320 -550 nm), in the following working conditions: pH = 7; photocatalyst dose = 50 -500 mg/L; irradiation time = 30 -240min. Prior to irradiation, the photocatalyst was added to samples, and resulted suspension was bubbled with air (50 L/h). In order to evaluate the effect of the main active species involved in Fe-TiO2 assisted photocatalytic degradation of TNT we suppressed the free • . OH radicals mediated process by addition of 16 x 10 -3 M iso-propanol (i-PrOH) scavenger. Lock of • . OHads radicals' production on the catalyst surface was assured by addition of 16 x 10 -3 M sodium iodide (NaI). The initial and irradiated samples were analysed for TNT, NO3 -, NO2 -and NH4 + concentrations by Gas Chromatography (GC), and Ion Chromatography respectively. In the tested experimental conditions, at 2.72 x 10 -4 M pollutant concentration, the increase of catalyst load up to 200 mg/L leads to the enhancement of initial TNT degradation rate up to 0.64 x 10 -7 Ms -1 . Since, ten times increase of initial TNT content has a negative effect on pollutant degradation rate constant, in similar experimental condition, prolonged irradiation time from 60 to 240 min was needed in order to assure pollutant advanced degradation efficiencies (≥ 99.9%). The TNT degradation and its inorganic by-products formation obeyed a pseudo-first-order kinetics. The experimental results of the reactive species quenching showed that • . OH radicals was the predominant oxidant species participated in reaction, and the pollutant degradation occurred mainly on the surface of catalyst.