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The underpotential deposition of Cd on polycrystalline Pt and Au was studied by voltammetry at stationary and rotating ring-disc electrodes. On Pt, the Cd ads dissolution peaks overlap those related to the oxidation of Hads, thus hindering the precise evaluation of desorption charges. A model proposed to calculate such charges from voltammetry at stationary electrodes revealed a value of 285 muC cm-2 for the monolayer dissolution, which corresponds to a coverage of 90% with Cd ads presenting an electrosorption valence of 0.5. Rotating ring-disc experiments fully confirmed such values. The misfit between atomic radii of Cd and Pt justifies the less-than-100% coverage. On the other hand, on Au, the absence of Hads simplifies the procedure for determination of dissolution charges for the Cd monolayer. Here, a value of only 41 muC cm-2 was calculated, which corresponds to a maximum coverage of 15%, with the electrosorption valence of 0.5. The results obtained in the collecting experiments with the rotating electrode are in complete agreement with those values.

In recent years, there has been an increasingly growing interest regarding the use of electrochemical advanced oxidation processes (EAOPs) which are considered highly promising alternative treatment techniques for addressing environmental issues related to pollutants of emerging concern. In EAOPs, electrogenerated oxidizing agents, such as hydroxyl radical (HO•), can react non-selectively with a wide range of organic compounds, degrading and mineralizing their structures to unharmful molecules like CO 2 , H 2 O, and inorganic ions. To this date, a broad spectrum of advanced electrocatalysts have been developed and applied for the treatment of compounds of interest in different matrices, specifically aiming at enhancing the degradation performance. New combined methods have also been employed as alternative treatment techniques targeted at circumventing the major obstacles encountered in Fenton-based processes, such as high costs and energy consumption, which still contribute significantly toward inhibiting the large-scale application of these processes. First, some fundamental aspects of EAOPs will be presented. Further, we will provide an overview of electrode materials which have been recently developed and reported in the literature, highlighting different anode and cathode structures employed in EAOPs, their main advantages and disadvantages, as well as their contribution to the performance of the treatment processes. The influence of operating parameters, such as initial concentrations, pH effect, temperature, supporting electrolyte, and radiation source, on the treatment processes were also studied. Finally, hybrid techniques which have been reported in the literature and critically assess the most recent techniques used for evaluating the degradation efficiency of the treatment processes. [Display omitted] • Electro-Fenton and Oxidation Processes removing contaminants of emerging concern. • An overview of recently developed electrode materials is provided. • The combination of methods to provide hybrid processes is summarized. • The most recently used techniques to evaluate degradation efficiency are discussed. [ABSTRACT FROM AUTHOR]

The objectives of this study were to determine the viability of removing Orange II (OII) dye by simulated solar photoelectro-Fenton (SSPEF) and to evaluate the stability of a WO 2.72 /Vulcan XC72 gas diffusion electrode (GDE) and thus determine its best operating parameters. The GDE cathode was combined with a BDD anode for decolorization and mineralization of 350 mL of 0.26 mM OII by anodic oxidation with electrogenerated H 2 O 2 (AO-H 2 O 2 ), electro-Fenton (EF) and photoelectro-Fenton (PEF) at 100, 150 and 200 mA cm -2 and SSPEF at 150 mA cm -2 . The GDE showed successful operation for electrogeneration, good reproducibility and low leaching of W. Decolorization and OII decay were directly proportional to the current density (j). AO-H 2 O 2 had a reduced performance that was only half of the SSPEF, PEF and EF treatments. The mineralization efficiency was in the following order: AO-H 2 O 2  < EF < PEF ≈ SSPEF. This showed that the GDE, BDD anode and light radiation combination was advantageous and indicated that the SSPEF process is promising with both a lower cost than using UV lamps and simulating solar photoelectro-Fenton process. The PEF process with the lowest j (100 mA cm -2 ) showed the best performance-mineralization current efficiency., (Copyright © 2019 Elsevier Ltd. All rights reserved.)