Biodiesel effluents were treated via photo-Fenton oxidation absorbing sunlight through a catalytic reactor connected to a stand-alone photovoltaic system, decreasing of almost 34% the biodiesel contaminants while storing energy to aid the whole process. OCIS codes: (040.5350); (350.5130)The scarcity of petroleum instigated studies suggesting the use of biofuels to substitute diesel [1]. Biodiesel can be added to petroleum diesel or used alone. As long as the generated effluents in biodiesel production are a problem to the environment especially due to the residues and organic pollutants of hard degradation associated with them, new technologies applicable to the treatment of effluents are searched, such as advanced oxidation processes (AOP) [2]. They have the advantage of destroying completely the organic contaminants, converting them into carbon dioxide, water and inorganic salt. Among the AOP, the called Fenton process is a powerful source of hydroxyl radicals (that decompose organic matter), products of the reaction between ferrous iron Fe +2 and hydrogen peroxide (H 2 O 2 ). In the presence of sunlight the efficiency of the process is amplified and it is called, then, photo-Fenton oxidation [3]. Thus there is an increase in the degradation of H 2 O 2 by light absorption and the photolysis of Fe +2 organic complex generated during decomposition. In this work, we report the use of photo-Fenton oxidation to treat biodiesel effluents, based in an experimental setup consisting of a photo catalytic reactor [4], in the center of which there is a transparent pyrex where the effluent pass by and absorbs radiation, as shown if figure 1(a). Distinct samples were formed by different concentrations of H 2 O 2 and Fe +2 solutions added to 1500 ml of biodiesel effluent and the wavelengths used for measurement of radiation intensity were 254 nm and 365 nm. Data about chemical oxygen demand (COD) in each sample during the photo-Feton oxidation allowed the identification of the best conditions for the reduction of this parameter in biodiesel effluent (the smaller COD, less contaminants remain in biodiesel). Results show that the sample (with a flow of 226,8 L/h) with solutions of concentration of 500 mg/L H 2 O 2 + 250 mg/L Fe +2 , had a decrease of 33,7% in its COD, meaning that the contaminants in this biodiesel sample were destroyed at this rate. Fig. 1. Catalytic reactor where biodiesel effluent absorbs light (a), COD variation for the sample with 500mg/L H2O2 + 250mg/L Fe +2 (b) and the isolated photovoltaic system (c).In order to aid the performance of the catalytic reactor, a stand-alone photovoltaic system [5], shown in figure 1(c), was built and coupled with the reactor in order to store energy and convert it in useful power, playing the role of a centrifugal pump of 0.5 hp, what makes the effluent´s samples circulating while the photo-Fenton oxidation occurs. The system dimensionment was realized through a computational tool developed in this work using