Electrooxidation using SnO₂‐RuO₂‐IrO₂|Ti and IrO₂‐Ta₂O₅|Ti anodes as tertiary treatment of oil refinery effluent

Abstract In the present work, treatability studies were carried out with oil refinery wastewater (effluent from the secondary treatment) using electrooxidation (EO) process employing two mixed oxide anodes: SnO 2 –RuO 2 –IrO 2 |Ti and IrO 2 –Ta 2 O 5 |Ti. Both electrodes' performance were compared by their capacity to generate active chlorine in a synthetic solution and organic matter mineralization of a sample with an average phenol (C 6 H 6 O) concentration of 100 mg L −1 . Before degradation experiments, surface analysis, and linear sweep voltammetry tests were performed. SnO 2 –RuO 2 –IrO 2 |Ti anode yielded higher active chlorine, reaching an average concentration of 340 mg L −1 at 90 min of electrolysis and 25 mA cm −2 . On the other hand, IrO 2 –Ta 2 O 5 |Ti anode only generated an average concentration of 200 mg L −1 at 90 min and 40 mA cm −2 . Regarding the degradation experiments, SnO 2 –RuO 2 –IrO 2 |Ti anode showed the highest dissolved organic carbon removal, ranging from 26% to 40%. In addition, through a three‐dimensional excitation–emission matrix fluorescence analysis, it was possible to elucidate the degradation of C 6 H 6 O and some possible polycyclic aromatic hydrocarbons present in the effluent. The results suggested that 65%–90% of the hydrocarbons and C 6 H 6 O present in the effluent were degraded with the SnO 2 –RuO 2 –IrO 2 |Ti anode applying 25 mA cm −2 within the first 30 min of electrolysis, reaching almost 99% degradation at 90 min. The EO process using SnO 2 –RuO 2 –IrO 2 |Ti can be an alternative for tertiary treatment of oil refinery wastewater for degradation and mineralization of the remaining organic matter of secondary effluents (biological processes) via active chlorine species.