Electrochemical treatment of butylated hydroxyanisole: Electrocoagulation versus advanced oxidation.

Highlights • Poor BHA and DOC decays in simulated matrix and urban wastewater by EC with Fe|Fe cell. • Active chlorine formed in simulated matrix accelerates BHA decay in EO-H 2 O 2. • Large mineralization of BHA in simulated matrix by EF and PEF with BDD/air-diffusion cell. • Growing mineralization in urban wastewater at pH 7.9: EO-H 2 O 2 < EF < PEF, greater with BDD. • Better performance of EF and PEF in urban wastewater at pH 3.0 by greater generation of OH. Abstract This work compares the removal of butylated hydroxyanisole (BHA), a ubiquitous antioxidant in food and pharmaceuticals, from water either by electrocoagulation (EC) with an Fe|Fe cell or H 2 O 2 -based electrochemical advanced oxidation processes like electrochemical oxidation (EO-H 2 O 2), electro-Fenton (EF) and photoelectro-Fenton (PEF) with an air-diffusion cathode. BHA degradation by EC was very poor, whereas the dissolved organic carbon (DOC) was more effectively abated in urban wastewater. The effect of pH, number of Fe|Fe pairs and current on the EC performance was examined. The additive was also slowly degraded by EO-H 2 O 2 with a RuO 2 -based or BDD anode in 50 mM Na 2 SO 4 solution. In the simulated matrix, BHA decay by EO-H 2 O 2 was substantially enhanced owing to active chlorine generation from anodic oxidation of Cl−, whereas the OH-mediated oxidation at the BDD surface accounted for DOC decay. In EF and PEF, the OH produced in the bulk upgraded the mineralization, primordially using BDD. In raw urban wastewater at natural pH 7.9, the time course of BHA and DOC contents was affected by NOM oxidation, being accelerated in the order: EO-H 2 O 2 < EF < PEF. The quickest decontamination of urban wastewater occurred in PEF at pH 3.0, because of the higher amounts of OH in the bulk along with UVA photolysis. [ABSTRACT FROM AUTHOR]