Abstract

Combined experimental and simulation techniques were applied to evaluate the validity of the commonly applied Tafel-approximation for the calculation of the mass and specific activities. A one dimensional agglomerate-based macro-homogeneous model was developed and solved analytically and numerically to understand the effects of exchange current density, porosity, agglomerate size, Nafion-film thickness and Pt loading on the mass activity. Porosity higher than 60% or agglomerates bigger than 100 nm at higher loadings may cause the loss of the validity of the Tafel-approximation and consequently the mass and specific activities decrease. Since these effect do not fully interpret the measured data, a new structural parameter was introduced. The real pore structure was estimated by using fractal theory. The volumetric catalyst density was corrected by the fractal dimension measured by Hg-porosimetry, which finally gave a good agremment with the experimental values.

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