Abstract
A solid oxide fuel cell (SOFC) stack can exhibit both
anodic and cathodic leakages, i.e. a fuel leak from the
anode side and an air leak from the cathode side of the
stack, respectively. This study describes the results of
an in-situ leakage analysis conducted for a planar SOFC
stack during 2000 hours of operation in an actual system
environment. The leakages are quantified experimentally
at nominal system operating conditions by conducting
composition analysis and flow metering of gases for both
fuel and air subsystems. Based on the calculated atomic
hydrogen-to-carbon ratio of the fuel and air gases, it is
found that the fuel leakages are mostly selective by
nature: the leaking fuel gas does not have the same
composition as the fuel system gas. A simple diffusive
leakage model, based on the leakage being driven by
concentration differences weighted by diffusion
coefficients, is applied to quantify the amount of
leakages. The leakage model provides a good
correspondence with the experimental results of the gas
analysis.
Original language | English |
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Pages (from-to) | 434-444 |
Journal | Fuel Cells |
Volume | 15 |
Issue number | 2 |
DOIs | |
Publication status | Published - 2015 |
MoE publication type | A1 Journal article-refereed |
Keywords
- diagnosis
- experimental results
- fuel cell system
- leakage
- mass transport
- solid oxide fuel cell
- stack
- testing