Development of the Fe Anodic Catalyst for Solid Oxide Fuel Cell Operated at Intermediate-temperature Direct Utilizing of Dimethylether Fuel
The Fe, Ni-BaCe0.8Y0.2O3−δ, and Pt catalysts and Pt catalysts were used as the anodic materials of an intermediate-temperature Solid Oxide Fuel Cell (SOFC) for direct utilization of dimethylether (DME) gas fuel. A proton conducting oxide BaCe0.8Y0.2O3−δ (BCY20) was used as the electrolyte (thickness...
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Veröffentlicht in: | Denki kagaku oyobi kōgyō butsuri kagaku 2009/03/05, Vol.77(3), pp.225-228 |
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creator | ISHIDA, Yousuke TAI, Ryosuke UI, Koichi TAKEUCHI, Ken FUJIMOTO, Kenjiro ITO, Shigeru |
description | The Fe, Ni-BaCe0.8Y0.2O3−δ, and Pt catalysts and Pt catalysts were used as the anodic materials of an intermediate-temperature Solid Oxide Fuel Cell (SOFC) for direct utilization of dimethylether (DME) gas fuel. A proton conducting oxide BaCe0.8Y0.2O3−δ (BCY20) was used as the electrolyte (thickness 500 µm) and a Pt was used as the cathode. The cell was operated at 600°C. The maximum power density of the cell with the Fe anodic catalyst was 36.4 mW cm−2 at 70 mA cm−2, while the maximum power density of the cell with a Ni-BCY20 and the Pt anode were 5.5 mW cm−2 at 10 mA cm−2 and 8.4 mW cm−2 at 20 mA cm−2, respectively. DME was mainly decomposed to H2, CO and CH4 by Fe anode. In this study, we investigated the process of anodic reactions with H2 and CO fuel. |
doi_str_mv | 10.5796/electrochemistry.77.225 |
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A proton conducting oxide BaCe0.8Y0.2O3−δ (BCY20) was used as the electrolyte (thickness 500 µm) and a Pt was used as the cathode. The cell was operated at 600°C. The maximum power density of the cell with the Fe anodic catalyst was 36.4 mW cm−2 at 70 mA cm−2, while the maximum power density of the cell with a Ni-BCY20 and the Pt anode were 5.5 mW cm−2 at 10 mA cm−2 and 8.4 mW cm−2 at 20 mA cm−2, respectively. DME was mainly decomposed to H2, CO and CH4 by Fe anode. 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A proton conducting oxide BaCe0.8Y0.2O3−δ (BCY20) was used as the electrolyte (thickness 500 µm) and a Pt was used as the cathode. The cell was operated at 600°C. The maximum power density of the cell with the Fe anodic catalyst was 36.4 mW cm−2 at 70 mA cm−2, while the maximum power density of the cell with a Ni-BCY20 and the Pt anode were 5.5 mW cm−2 at 10 mA cm−2 and 8.4 mW cm−2 at 20 mA cm−2, respectively. DME was mainly decomposed to H2, CO and CH4 by Fe anode. 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A proton conducting oxide BaCe0.8Y0.2O3−δ (BCY20) was used as the electrolyte (thickness 500 µm) and a Pt was used as the cathode. The cell was operated at 600°C. The maximum power density of the cell with the Fe anodic catalyst was 36.4 mW cm−2 at 70 mA cm−2, while the maximum power density of the cell with a Ni-BCY20 and the Pt anode were 5.5 mW cm−2 at 10 mA cm−2 and 8.4 mW cm−2 at 20 mA cm−2, respectively. DME was mainly decomposed to H2, CO and CH4 by Fe anode. In this study, we investigated the process of anodic reactions with H2 and CO fuel.</abstract><cop>Tokyo</cop><pub>The Electrochemical Society of Japan</pub><doi>10.5796/electrochemistry.77.225</doi><tpages>4</tpages><oa>free_for_read</oa></addata></record> |
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subjects | Anode Dimethylether (DME) Proton Conducting Oxide SOFC |
title | Development of the Fe Anodic Catalyst for Solid Oxide Fuel Cell Operated at Intermediate-temperature Direct Utilizing of Dimethylether Fuel |
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