2008
DOI: 10.1149/1.2982024
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Pt-Free Cathode Catalyst Performance in H2/O2 Anion-Exchange Membrane Fuel Cells (AMFCs)

Abstract: H2/O2 AMFCs enable the use of Platinum Group Metal (PGM) free Membrane Electrode Assemblies (MEAs), especially for the Oxygen Reduction Reaction (ORR). A promising catalysts for the ORR (Acta's "K14"), has been developed and tested using Rotating Disk Electrode (RDE) analysis, showing promising performance. In this paper we characterize current Anion-Exchange Membranes (AMs), show the fuel cell activity of AM-based MEAs prepared with K14 ORR catalyst, and compare their performance with the kinetic and ohmic li… Show more

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Cited by 39 publications
(33 citation statements)
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“…1d) environments. 8,[16][17][18] Similar losses have also been reported for electrolyzers 5,19 (Fig. 1c) and metal-air batteries 13,20 due to the poor kinetics of the oxygen oxidation reaction -more commonly referred to as the oxygen evolution reaction (OER).…”
Section: Introductionsupporting
confidence: 63%
See 1 more Smart Citation
“…1d) environments. 8,[16][17][18] Similar losses have also been reported for electrolyzers 5,19 (Fig. 1c) and metal-air batteries 13,20 due to the poor kinetics of the oxygen oxidation reaction -more commonly referred to as the oxygen evolution reaction (OER).…”
Section: Introductionsupporting
confidence: 63%
“…This mechanism proceeds similarly to Energy & Environmental Science Review the acid-base mechanism, but the evolution of oxygen does not occur through the potentially rate-limiting OOH* species. While such reaction mechanisms have been shown to have large activation barriers on noble metal surfaces, 58 the presence of loosely bound lattice oxygen atoms in oxide surface terminations have been observed to facilitate such reaction steps in the OER by 18 O isotope studies on RuO 2 (ref. 105) and NiCo 2 O 4 .…”
Section: Proposed Reaction Mechanisms On Oxide Surfacesmentioning
confidence: 99%
“…4, may be expressed as Eq. 6: i k (0.8V) = e·(SD FeN2+2 ·ToF FeN2+2 + SD FeN4 ·ToF FeN4 ) [6] The activity of FeAc + NH 3 (or of ClFeTMPP + NH 3 ) is ~ 6 A·g -1 at both pH 1 and pH 13. Applying Equation 6 at pH 1 with i k (0.8V) = 6 A·g -1 , SD FeN2+2 =2.6·10 19 sites·g -1 , SD FeN4 =6.5·10 18 sites·g -1 and the value of ToF FeN4 = 6·10 -3 e·site -1 ·s -1 from our previous ECS Transactions, 25 (1) 117-128 (2009) calculation for ClFeTMPP + Ar, we get a minimum ToF FeN2+2 (pH 1) = 1.5 e·site -1 ·s -1 .…”
Section: Resultsmentioning
confidence: 99%
“…Meanwhile, fuel cell research shifted from basic to acidic electrolytes. While some Fe or Co/N/C catalysts can compete with Pt in alkaline media (6,7), most of them unfortunately still display insufficient activity and poor stability in acid media. This work attempts to better understanding the cause of these shortcomings in the latter in order to overcome the obstacles that they face in the PEM environment, by investigating the behaviors of three different Fe-based catalysts in both acid and alkaline media.…”
Section: Introductionmentioning
confidence: 99%
“…Although studies at RDE setup show the kinetics of HOR and ORR to be sufficiently fast, the performance of AMFC, however, can be limited due to additional problems such as water flooding at anode, water scarcity at cathode, low ionic conductivity of CL, and low mass transport of reactants. Filpi et al evaluated the performance of H 2 /O 2 AMFC and proposed that the difference between estimated performance after kinetic and ohmic correction and measured performance could be due to transport losses such as reactant transport and OH – transport. For a facile mass transport of reactant through the CL, permeability and diffusion coefficient of reactant in ionomer should be high.…”
Section: Introductionmentioning
confidence: 99%