Technoeconomic Assessment of Electrochemical Hydrogen Peroxide Production with Gas Diffusion Electrodes under Scenarios Relevant to Practical Water Treatment
Erzhuo Zhao, Guangsen Xia, Yang Li, Juhong Zhan, Gang Yu, Yujue Wang
Abstract
Recent studies have shown that electrochemically producing hydrogen peroxide (H 2 O 2 ) with gas diffusion electrodes (GDEs) directly in the water to be treated by H 2 O 2 -based advanced oxidation processes (AOPs) is problematic in practical applications because of the quick deterioration of GDE stability by oxidation with strong oxidants (e.g., hydroxyl radicals) and fouling by complex water constituents (e.g., Ca 2+ and Mg 2+ ). Therefore, this study tested the electrosynthesis of H 2 O 2 with GDEs in electrolyte solutions in a separate reactor as an alternative for on-site H 2 O 2 production in water treatment. Results show that many reactor configurations and operational parameters (e.g., electrode distance, current densities, electrolytes, and GDE backpressure) intertwine to have complex influences on the overall performance of H 2 O 2 production in terms of H 2 O 2 production rates and current efficiencies, GDE stability, operating cost, and GDE capital cost. Under optimized conditions determined in this study (4 mm electrode distance, 150–200 mA/cm 2 current densities, 1 M Na 2 SO 4, and 30 kPa GDE backpressure), ∼29,000–34,000 mg/L of H 2 O 2 could be produced with production rates of 57.3–68.3 mg/h/cm 2 and apparent current efficiencies of 55%–61% during H 2 O 2 electrosynthesis with a divided cell, and the GDEs maintained stable H 2 O 2 production over ∼350–1000 h before water penetrated the GDEs due to the electrocapillary effect. The operating cost, including the electricity, electrolytes, water, and oxygen consumed in the process, was ∼1.32–1.48 $/kg H2O2, and the capital cost was ∼0.30–0.46 $/kg H2O2 . The results of this study suggest that it is technoeconomically feasible to scale up H 2 O 2 electrosynthesis with GDEs in electrolytes to produce H 2 O 2 on site in some water treatment applications, e.g., micropollutant removal in drinking water treatment by H 2 O 2 -based AOPs. Additional studies are needed to further extend the GDE lifetime by improving GDE fabrications and operations to prevent water penetration during H 2 O 2 electrosynthesis.