Abstract
Coal syngas, a potential fuel for SOFCs, contains impurities like PH3, which rapidly degrade Ni-based SOFC anodes. Past research showed significant reconstruction of Ni anodes in button cells with degradation rates of ∼0.5 mV∙h−1. It is not evident that these rates correspond to actual stack applications due to major differences in fuel utilization and delivery. Herein, a single planar repeat unit with an active area of 32.64 cm2 is constructed using a Haynes® 242 manifold. The cell operates at 800 °C using dry H2 with and without 10 ppm PH3. The cell employs a co-flow configuration with a fuel utilization of 12.5%. The performance of the cell is evaluated over 440 h by voltage-current measurements and electrochemical impedance spectroscopy. The post-run analysis of the contaminated cell is conducted via XRD, XPS and SEM. The degradation rate for the cell is found to be 3×10−3 mV∙h−1, which is far lower than that reported previously. The cell shows low evidence of significant PH3 poisoning and there is no reconstruction of the Ni-anode microstructure, as seen in button cell testing. Some basic electrochemical and thermodynamic modeling, and microstructural/chemical characterization are presented and related to the cell's relatively stable performance observed in this work.
Original language | English |
---|---|
Pages (from-to) | 185-194 |
Number of pages | 10 |
Journal | Journal of Power Sources |
Volume | 395 |
DOIs | |
State | Published - Aug 15 2018 |
Keywords
- Anodes
- Coal syngas
- Contaminants
- Gasification
- Solid Oxide Fuel Cells (SOFC)
- Thermodynamic analysis