摘要
A two-dimensional multicomponent lattice Boltzmann (LB) model based on kinetic theory for gas mixtures combined with a representative elementary volume (REV) scale LB algorithm based on the Brinkman equation for flows in porous media is developed to simulate the mass transport in the porous anode and cathode of solid oxide fuel cell (SOFC). The concentration overpotential is calculated and compared with that obtained by the extended Fick's model (FM), the dusty gas model (DGM), and the Stefan Maxwell model (SMM), as well as the experimental results. It is concluded that LB method is a much more accurate method for the simulation of mass transfer within fuel cell electrodes. Moreover, the effects of different electrode geometrical and operating parameters on concentration polarization are also investigated.
| 源语言 | 英语 |
|---|---|
| 文章编号 | 061004 |
| 期刊 | Journal of Fuel Cell Science and Technology |
| 卷 | 9 |
| 期 | 6 |
| DOI | |
| 出版状态 | 已出版 - 2012 |
联合国可持续发展目标
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可持续发展目标 7 经济适用的清洁能源
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