2006
DOI: 10.1149/1.2214564
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Hydrogen Peroxide Formation as a Degradation Factor of Polymer Electrolyte Fuel Cells

Abstract: 20wt.% Pt/C catalyst was loaded at different densities (0.28- 56.7 mgcarbon cm-2) on glassy carbon (GC) disk electrode, and the effect of its agglomeration on hydrogen peroxide formation in oxygen reduction reaction (ORR) was investigated by the rotating ring-disk electrode technique. The formation of H2O2 was enhanced with a reduction in agglomeration of Pt/C. Even in the operating potential range of PEFC cathodes (0.6-0.8 V), 20% of hydrogen peroxide was formed on Pt/C loaded at densities lower than … Show more

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Cited by 10 publications
(7 citation statements)
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“…This fact supported the mechanism proposed by LaConti et al . A recent rotating ring−disk electrode study suggested that H 2 O 2 yield exceeds 80% at Pt/C catalysts dispersed highly on a glassy carbon disk in the anode potential range (∼0 V) . The presence of H 2 O 2 has been confirmed in exhaust gas, in drain water, and directly in the membrane during operation of PEMFCs.…”
Section: 3 Chemical Degradation331 Peroxide/radical Degradationmentioning
confidence: 95%
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“…This fact supported the mechanism proposed by LaConti et al . A recent rotating ring−disk electrode study suggested that H 2 O 2 yield exceeds 80% at Pt/C catalysts dispersed highly on a glassy carbon disk in the anode potential range (∼0 V) . The presence of H 2 O 2 has been confirmed in exhaust gas, in drain water, and directly in the membrane during operation of PEMFCs.…”
Section: 3 Chemical Degradation331 Peroxide/radical Degradationmentioning
confidence: 95%
“…It is known that H 2 O 2 formation in oxygen reduction on polycrystalline , and single , crystalline Pt as well as Pt/C catalyst is greatly enhanced in the anode potential region, where atomic hydrogen is adsorbed on Pt. This fact supported the mechanism proposed by LaConti et al .…”
Section: 3 Chemical Degradation331 Peroxide/radical Degradationmentioning
confidence: 99%
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“…In this study, the catalyst loading on the GC rod was fixed at 7.23 (μg-Pt) cm –2 , that is, less than half that specified in the Fuel Cell Commercialization Conference of Japan (FCCJ) protocol. A decrease in the catalyst loading results in the kinetically controlled region at around 0.8 to 1.0 V in a linear sweep voltammetry (LSV) curve shifting to a negative potential. The limiting current, which indicates the diffusion-controlled region, becomes tiny, and the ORR current decreases (see Figure S1). A high-performance catalyst with a large number of active sites shows the early formation of a diffusion-controlled region.…”
Section: Resultsmentioning
confidence: 99%
“…A catalyst with high activity and high selectivity towards the 4e − reduction is needed to overcome the sluggish ORR kinetics occurring at the cathode of a fuel cell [1,2]. Regarding selectivity, the O 2 reduction with 2e − is detrimental for fuel cell performance because reduces its efficiency and the produced H 2 O 2 damages the membrane fuel cell [3]. Nevertheless, high selectivity to 2e − reduction is desired for decentralized H 2 O 2 production as an alternative to the established industrial anthraquinone process [4,5].…”
Section: Introductionmentioning
confidence: 99%