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SOFC characteristics along the flow path
Institution:1. Faculty of Engineering, Kyushu University, Motooka, 744, Nishi-ku, Fukuoka 819-0395, Japan;2. Center of Coevolutionary Research for Sustainable Communities, Kyushu University, Motooka, 744, Nishi-ku, Fukuoka 819-0395, Japan;3. Platform of Inter / Transdisciplinary Energy Research (Q-PIT), Kyushu University, Motooka, 744, Nishi-ku, Fukuoka 819-0395, Japan;4. Next-Generation Fuel Cell Research Center (NEXT-FC), Kyushu University, Motooka, 744, Nishi-ku, Fukuoka 819-0395, Japan;5. International Research Center for Hydrogen Energy, Kyushu University, Motooka, 744, Nishi-ku, Fukuoka 819-0395, Japan;6. International Institute for Carbon-Neutral Energy Research (WPI-I2CNER), Kyushu University, Motooka, 744, Nishi-ku, Fukuoka 819-0395, Japan;1. Forschungszentrum Jülich GmbH, Institute of Energy and Climate Research (IEK-3), Germany;2. Forschungszentrum Jülich GmbH, Central Institute for Engineering, Electronics and Analytics (ZEA-1), Germany;3. Chair for Fuel Cells, RWTH Aachen University, Germany;1. School of Energy and Power, Jiangsu University of Science and Technology, 212003, Zhenjiang, Jiangsu, China;2. School of Mechanical and Engineering, Jiangsu University of Science and Technology, 212003, Zhenjiang, Jiangsu, China
Abstract:Solid oxide fuel cells (SOFCs) in metallic housings were integrally and locally characterised. The tests were performed in counter flow operation for hydrogen concentrations from 2% to 100%, to identify concentration limitations and to optimise fuel utilisation. Cell characterisations were performed by spatially resolved electrochemical impedance spectroscopy (EIS), current density/voltage (iV) and temperature measurements as well as gas chromatography measurements at 16 distinct points across the cell. The results show a substantial variation of current density and voltage distribution along the flow path with varying hydrogen content and fuel utilisation. The fuel utilisation was calculated from the local current densities and compared to the values measured by gas chromatography. Both sets of results showed good agreement. At low hydrogen inlet concentrations the voltage at the fuel outlet drops to values that might be harmful for the stability of the anode since reoxidation of nickel can occur. The impedances obtained by local EIS did not show an overall coherent dependency on the hydrogen concentration. EIS under load revealed two distinct domains: in the range of hydrogen concentrations of 2–10% H2 the impedance decreased significantly with increasing hydrogen content whereas at higher hydrogen contents the impedance was hardly affected. This indicates significant concentration and diffusion overpotential at low hydrogen concentrations. The local data showed differing behaviour in the middle of the cell compared to the fuel outlet. Leakage at the sealing could be identified as a possible reason. As an additional method of investigation, the voltage drop over the contact resistance of the cathode side was measured. Temperature measurements show that local temperatures differ significantly depending on the load applied to the cell. This observation emphasizes the importance of a thermal management adapted to the characteristics on operation conditions of the cells, particularly when the stack itself has only a low mass.
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