Abstract
The present model is validated against literature experimental results and it shows good agreement. In addition, we also investigate effects of operating and structural parameters on the cell voltage. Results exhibit that the cell voltage is increased with the reactant concentration, including formate, hydroxide ions, and oxygen, which originates from the reduced activation polarization and concentration polarization. Moreover, it is also shown that increasing the exchange current density much reduces electrode overpotentials and thus upgrades the cell performance. The model is further used to examine how the anode diffusion layer and the membrane affect the cell performance. It is found that the cell performance is upgraded with increasing the porosity of the anode diffusion layer and decreasing the thickness of the anode diffusion layer or membrane.
Original language | English |
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Pages (from-to) | 232-240 |
Number of pages | 9 |
Journal | Applied Thermal Engineering |
Volume | 124 |
DOIs | |
Publication status | Published - 1 Jan 2017 |
Keywords
- Direct formate fuel cell
- Fuel cell
- Mass transport
- Mathematical modeling
- Polarization
ASJC Scopus subject areas
- Energy Engineering and Power Technology
- Industrial and Manufacturing Engineering