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首页> 外文期刊>Catalysts >In Situ FTIR Analysis of CO-Tolerance of a Pt-Fe Alloy with Stabilized Pt Skin Layers as a Hydrogen Anode Catalyst for Polymer Electrolyte Fuel Cells
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In Situ FTIR Analysis of CO-Tolerance of a Pt-Fe Alloy with Stabilized Pt Skin Layers as a Hydrogen Anode Catalyst for Polymer Electrolyte Fuel Cells

机译:原位FTIR分析PT-Fe合金与稳定的Pt皮肤层作为聚合物电解质燃料电池的氢阳极催化剂

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The CO-tolerance mechanism of a carbon-supported Pt-Fe alloy catalyst with two atomic layers of stabilized Pt-skin (Pt 2AL –PtFe/C) was investigated, in comparison with commercial Pt 2 Ru 3 /C (c-Pt 2 Ru 3 /C), by in situ attenuated total reflection Fourier transform infrared (ATR-FTIR) spectroscopy in 0.1 M HClO 4 solution at 60 °C. When 1% CO (H 2 -balance) was bubbled continuously in the solution, the hydrogen oxidation reaction (HOR) activities of both catalysts decreased severely because the active sites were blocked by CO ad , reaching the coverage θ CO ≈ 0.99. The bands in the IR spectra observed on both catalysts were successfully assigned to linearly adsorbed CO (CO L ) and bridged CO (CO B ), both of which consisted of multiple components (CO L or CO B at terraces and step/edge sites). The Pt 2AL –PtFe/C catalyst lost 99% of its initial mass activity ( MA ) for the HOR after 30 min, whereas about 10% of the initial MA was maintained on c-Pt 2 Ru 3 /C after 2 h, which can be ascribed to a suppression of linearly adsorbed CO at terrace sites (CO L, terrace ). In contrast, the HOR activities of both catalysts with pre-adsorbed CO recovered appreciably after bubbling with CO-free pure H 2 . We clarify, for the first time, that such a recovery of activity can be ascribed to an increased number of active sites by a transfer of CO L, terrace to CO L, step/edge , without removal of CO ad from the surface. The Pt 2AL –PtFe/C catalyst showed a larger decrease in the band intensity of CO L, terrace . A possible mechanism for the CO-tolerant HOR is also discussed.
机译:研究了碳负载的Pt-Fe合金催化剂与稳定的Pt-Ska(Pt 2al -ptFe / c)的两个原子层的共同耐受机理,与商业Pt 2 ru 3 / c相比(C-Pt 2 ru 3 / c),通过原位减弱的全反射傅里叶变换红外(ATR-FTIR)光谱在0.1M HClO 4溶液中在60℃下。当在溶液中连续鼓泡1%CO(H 2 -Balance)时,两种催化剂的氢氧化反应(Hor)活性严重降低,因为通过CO AD阻断活性位点,到达覆盖θCo≈0.99。在两种催化剂上观察到的IR光谱中的条带被成功地分配给线性吸附的CO(COL)和桥接CO(CO B),两者包括多种组分(CO L或CO B处的梯田和阶梯/边缘位点) 。 PT 2AL -PTFE / C催化剂在30分钟后损失其初始质量活性(MA)的99%,而在2小时后约10%的初始MA保持在C-PT 2 Ru 3 / C上可以抑制在露台场所(CO L,露台)的线性吸附的CO。相反,在用无共同纯H 2鼓泡后,两种催化剂的HOR活性与预吸附的CO显着回收。我们首次阐明这种活动的恢复可以通过转移CO L,露台到CO L,步进/边缘,而不从表面移除CO AD的增加的活性部位归因于增加数量的活动场所。 PT 2AL -PTFE / C催化剂显示CO L,露台的带强度较大。还讨论了具有共同耐受性的可能机制。

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