## Abstract A CFD model is created to analyze methanol transport in a flowing electrolyte direct methanol fuel cell (FE‐DMFC) by solving the 3D advection‐diffusion equation, with consideration of electro‐osmosis. The average methanol flux at the anode and cathode surfaces is simulated and compared
Nanoporous separator and low fuel concentration to minimize crossover in direct methanol laminar flow fuel cells
✍ Scribed by A.S. Hollinger; R.J. Maloney; R.S. Jayashree; D. Natarajan; L.J. Markoski; P.J.A. Kenis
- Book ID
- 104025963
- Publisher
- Elsevier Science
- Year
- 2010
- Tongue
- English
- Weight
- 903 KB
- Volume
- 195
- Category
- Article
- ISSN
- 0378-7753
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✦ Synopsis
Laminar flow fuel cells (LFFCs) overcome some key issues -most notably fuel crossover and water management -that typically hamper conventional polymer electrolyte-based fuel cells. Here we report two methods to further minimize fuel crossover in LFFCs: (i) reducing the cross-sectional area between the fuel and electrolyte streams, and (ii) reducing the driving force of fuel crossover, i.e. the fuel concentration gradient. First, we integrated a nanoporous tracketch separator at the interface of the fuel and electrolyte streams in a single-channel LFFC to dramatically reduce the cross-sectional area across which methanol can diffuse. Maximum power densities of 48 and 70 mW cm -2 were obtained without and with a separator, respectively, when using 1 M methanol. This simple design improvement reduces losses at the cathode leading to better performance and enables thinner cells, which is attractive in portable applications. Second, we demonstrated a multichannel cell that utilizes low methanol concentrations (<300 mM) to reduce the driving force for methanol diffusion to the cathode. Using 125 mM methanol as the fuel, a maximum power density of 90 mW cm -2 was obtained. This multichannel cell further simplifies the LFFC design (one stream only) and its operation, thereby extending its potential for commercial application.
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