2 research outputs found

    Electrochemical Production of Hydrogen Coupled with the Oxidation of Arsenite

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    The production of hydrogen accompanied by the simultaneous oxidation of arsenite (AsĀ­(III)) was achieved using an electrochemical system that employed a BiO<sub><i>x</i></sub>ā€“TiO<sub>2</sub> semiconductor anode and a stainless steel (SS) cathode in the presence of sodium chloride (NaCl) electrolyte. The production of H<sub>2</sub> was enhanced by the addition of AsĀ­(III) during the course of water electrolysis. The synergistic effect of AsĀ­(III) on H<sub>2</sub> production can be explained in terms of (1) the scavenging of reactive chlorine species (RCS), which inhibit the production of H<sub>2</sub> by competing with water molecules (or protons) for the electrons on the cathode, by AsĀ­(III) and (2) the generation of protons, which are more favorably reduced on the cathode than water molecules, through the oxidation of AsĀ­(III). The addition of 1.0 mM AsĀ­(III) to the electrolyte at a constant cell voltage (<i>E</i><sub>cell</sub>) of 3.0 V enhanced the production of H<sub>2</sub> by 12% even though the cell current (<i>I</i><sub>cell</sub>) was reduced by 5%. The net effect results in an increase in the energy efficiency (EE) for H<sub>2</sub> production (Ī”EE) by 17.5%. Furthermore, the value Ī”EE, which depended on AsĀ­(III) concentration, also depended on the applied <i>E</i><sub>cell</sub>. For example, the Ī”EE increased with increasing AsĀ­(III) concentration in the micromolar range but decreased as a function of <i>E</i><sub>cell</sub>. This is attributed to the fact that the reactions between RCS and AsĀ­(III) are influenced by both RCS concentration depending on <i>E</i><sub>cell</sub> and AsĀ­(III) concentration in the solution. On the other hand, the Ī”EE decreased with increasing AsĀ­(III) concentration in the millimolar range due to the adsorption of AsĀ­(V) generated from the oxidation of AsĀ­(III) on the semiconductor anode. In comparison to the electrochemical oxidation of certain organic compounds (e.g., phenol, 4-chlorophenol, 2-chlorophenol, salicylic acid, catechol, maleic acid, oxalate, and urea), the Ī”EE obtained during AsĀ­(III) oxidation (17.5%) was higher than that observed during the oxidation of the above organic compounds (Ī”EE = 3.0ā€“15.3%) with the exception of phenol at 22.1%. The synergistic effect of AsĀ­(III) on H<sub>2</sub> production shows that an energetic byproduct can be produced during the remediation of a significant inorganic pollutant

    Effects of Anodic Potential and Chloride Ion on Overall Reactivity in Electrochemical Reactors Designed for Solar-Powered Wastewater Treatment

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    We have investigated electrochemical treatment of real domestic wastewater coupled with simultaneous production of molecular H<sub>2</sub> as useful byproduct. The electrolysis cells employ multilayer semiconductor anodes with electroactive bismuth-doped TiO<sub>2</sub> functionalities and stainless steel cathodes. DC-powered laboratory-scale electrolysis experiments were performed under static anodic potentials (+2.2 or +3.0 V NHE) using domestic wastewater samples, with added chloride ion in variable concentrations. Greater than 95% reductions in chemical oxygen demand (COD) and ammonium ion were achieved within 6 h. In addition, we experimentally determined a decreasing overall reactivity of reactive chlorine species toward COD with an increasing chloride ion concentration under chlorine radicals (ClĀ·, Cl<sub>2</sub><sup>ā€“</sup>Ā·) generation at +3.0 V NHE. The current efficiency for COD removal was 12% with the lowest specific energy consumption of 96 kWh kgCOD<sup>ā€“1</sup> at the cell voltage of near 4 V in 50 mM chloride. The current efficiency and energy efficiency for H<sub>2</sub> generation were calculated to range from 34 to 84% and 14 to 26%, respectively. The hydrogen comprised 35 to 60% by volume of evolved gases. The efficacy of our electrolysis cell was further demonstrated by a 20 L prototype reactor totally powered by a photovoltaic (PV) panel, which was shown to eliminate COD and total coliform bacteria in less than 4 h of treatment
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