Abstract
An improved electrochemical model is developed to study the ammonia fed solid oxide fuel cell based on proton conducting electrolyte (SOFC-H). Including the chemical reaction kinetics of NH3catalytic thermal decomposition, the present model can be used to predict the performance of the NH3fed SOFC-H at an intermediate temperature (i.e. 773 K). Comparison between the simulation results using the present model and experimental data from literature validates the accuracy of this model. Parametrical analyses reveal that at a high operating temperature (i.e. 1073 K), the NH3fuel is completely decomposed to H2and N2within a very thin layer (30 μm) near the anode surface of an SOFC-H. It is also found that operating the NH3fed SOFC-H at an intermediate temperature of 773 K is feasible due to sufficiently high rate of NH3decomposition. However, further decreasing the temperature to 673 K is not recommended as less than 10% NH3fuel can be decomposed to H2and N2in the SOFC-H. The effects of current density and electrode microstructure on the performance of the NH3fed SOFC-H are also studied. It is found that increasing electrode porosity and pore size is beneficial to increase the partial pressure of H2at the anode-electrolyte interface. The model developed in this paper can be extended to 2D or 3D models to study practical tubular or planar SOFCs.
Original language | English |
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Pages (from-to) | 233-240 |
Number of pages | 8 |
Journal | Journal of Power Sources |
Volume | 185 |
Issue number | 1 |
DOIs | |
Publication status | Published - 15 Oct 2008 |
Externally published | Yes |
Keywords
- Ammonia catalytic decomposition
- Ammonia fuel
- Electrochemical model
- Mass transfer
- Proton conducting ceramics
- Solid oxide fuel cell (SOFC)
ASJC Scopus subject areas
- Renewable Energy, Sustainability and the Environment
- Energy Engineering and Power Technology
- Physical and Theoretical Chemistry
- Electrical and Electronic Engineering