Hydrogen
peroxide (H<sub>2</sub>O<sub>2</sub>) is frequently used
in combination with ultraviolet (UV) light to treat trace organic
contaminants in advanced oxidation processes (AOPs). In small-scale
applications, such as wellhead and point-of-entry water treatment
systems, the need to maintain a stock solution of concentrated H<sub>2</sub>O<sub>2</sub> increases the operational cost and complicates
the operation of AOPs. To avoid the need for replenishing a stock
solution of H<sub>2</sub>O<sub>2</sub>, a gas diffusion electrode
was used to generate low concentrations of H<sub>2</sub>O<sub>2</sub> directly in the water prior to its exposure to UV light. Following
the AOP, the solution was passed through an anodic chamber to lower
the solution pH and remove the residual H<sub>2</sub>O<sub>2</sub>. The effectiveness of the technology was evaluated using a suite
of trace contaminants that spanned a range of reactivity with UV light
and hydroxyl radical (HO<sup>•</sup>) in three different types
of source waters (i.e., simulated groundwater, simulated surface water,
and municipal wastewater effluent) as well as a sodium chloride solution.
Irrespective of the source water, the system produced enough H<sub>2</sub>O<sub>2</sub> to treat up to 120 L water d<sup>–1</sup>. The extent of transformation of trace organic contaminants was
affected by the current density and the concentrations of HO<sup>•</sup> scavengers in the source water. The electrical energy per order
(<i>E</i><sub>EO</sub>) ranged from 1 to 3 kWh m<sup>–3</sup>, with the UV lamp accounting for most of the energy consumption.
The gas diffusion electrode exhibited high efficiency for H<sub>2</sub>O<sub>2</sub> production over extended periods and did not show a
diminution in performance in any of the matrices