Abstract
We present an analysis of the mass transport of methanol at the anode of a direct methanol fuel cell (DMFC) and show that the overall mass-transfer coefficient can be determined by measuring the cell limiting current density. We measured the cell limiting current density of an in-house-fabricated DMFC with different flow fields for various methanol concentrations and flow rates of methanol solution. The experimental data showed that the overall mass-transfer coefficient was nearly independent of current density, although the rate of C O2 gas bubble liberation changed with current density. We found that the overall methanol-transfer coefficient in the serpentine flow field could be significantly increased with increased methanol flow rate due to the enhanced under-rib convection. We developed the correlation equations predicting the overall methanol transfer coefficient in terms of the methanol flow rate for a given DMFC hardware. Finally, we showed that the polarization curves predicted based on the correlation equation of the overall mass-transfer coefficient in the DMFC with the serpentine flow field for different flow rates were in fairly good agreement with the experimental data.
| Original language | English |
|---|---|
| Pages (from-to) | A1358-A1364 |
| Journal | Journal of the Electrochemical Society |
| Volume | 153 |
| Issue number | 7 |
| DOIs | |
| State | Published - Jul 2006 |
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SDG 7 Affordable and Clean Energy
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