Abstract
The degradation of Rhodamine B (RhB) was studied using advanced electrochemical oxidation processes (EAOP): electro-Fenton (EF), anodic oxidation (AO) and electro-Fenton coupled with anodic oxidation (EF/AO) on a carbon felt (CF) cathode paired with either a sub-stoichiometric titanium dioxide Magnéli phase (Ti4O7) anode or a platinized titanium (Ti/Pt) anode. The study revealed that operating conditions significantly impacted the kinetics of electrochemical reactions. Increasing the current density from 10 to 50 mA cm− 2 significantly accelerated the degradation of RhB, with 30 mA cm− 2 identified as the optimal current density, balancing energy consumption and degradation efficiency. The RhB concentration also influenced the degradation kinetics: higher concentrations required longer treatment times. The EF/AO coupling process proved particularly effective in degrading higher concentrations of RhB. Toxicity evaluation using the Microtox® bioluminescence inhibition test showed reduced toxicity during the electrochemical degradation of the pollutant, with EF/AO presenting the most significant reduction. The EF/AO coupling also demonstrated superior total organic carbon (TOC) removal, reaching 90% at pH 3 compared to EF and AO alone, suggesting efficient mineralization of RhB and its by-products. Energy consumption (EC) remained relatively stable across all processes during a 480 min electrolysis period. High-resolution mass spectrometry confirmed the degradation pathways of RhB, involving chain oxidation reactions leading to the formation of intermediate products and mineralization to CO2 and H2O. This study demonstrates the potential of EF, AO and EF/AO coupling as effective methods for mineralizing Rhodamine B (RhB) from wastewater, contributing to sustainable and environmentally friendly wastewater treatment strategies.