Drinking Water Purification by Electrosynthesis of Hydrogen Peroxide in a Power-Producing PEM Fuel Cell

被引:65
作者
Li, Winton [1 ,2 ]
Bonakdarpour, Arman [1 ,2 ]
Gyenge, Elod [1 ,2 ]
Wilkinson, David P. [1 ,2 ]
机构
[1] Univ British Columbia, Dept Chem & Biol Engn, Vancouver, BC V6T 1Z3, Canada
[2] Univ British Columbia, Clean Energy Res Ctr, Vancouver, BC V6T 1Z3, Canada
基金
加拿大自然科学与工程研究理事会;
关键词
cobalt; fuel cells; heterogeneous catalysis; oxidation; peroxides; CATALYTIC SYNTHESIS; H2O2; OZONE; ELECTROLYSIS; REDUCTION;
D O I
10.1002/cssc.201300225
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
The industrial anthraquinone auto-oxidation process produces most of the world's supply of hydrogen peroxide. For applications that require small amounts of H2O2 or have economically difficult transportation means, an alternate, on-site H2O2 production method is needed. Advanced drinking water purification technologies use neutral-pH H2O2 in combination with UV treatment to reach the desired water purity targets. To produce neutral H2O2 on-site and on-demand for drinking water purification, the electroreduction of oxygen at the cathode of a proton exchange membrane (PEM) fuel cell operated in either electrolysis (power consuming) or fuel cell (power generating) mode could be a possible solution. The work presented here focuses on the H-2/O-2 fuel cell mode to produce H2O2. The fuel cell reactor is operated with a continuous flow of carrier water through the cathode to remove the product H2O2. The impact of the cobalt-carbon composite cathode catalyst loading, Teflon content in the cathode gas diffusion layer, and cathode carrier water flowrate on the production of H2O2 are examined. H2O2 production rates of up to 200molh(-1)cm(geometric) (-2) are achieved using a continuous flow of carrier water operating at 30% current efficiency. Operation times of more than 24h have shown consistent H2O2 and power production, with no degradation of the cobalt catalyst.
引用
收藏
页码:2137 / 2143
页数:7
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