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Selenium-modulated Pt/Al2O3 electronic structure induces deactivation during catalytic CO oxidation
Journal of Catalysis ( IF 6.5 ) Pub Date : 2024-11-22 , DOI: 10.1016/j.jcat.2024.115857
Tian Tang, Jianing Ma, Jingyu Xue, Xiaoqiang Shen, Jinfei Chen, Linhan Yu, Vladislav Rac, Vesna Rakić, Xinbao Li, Hao Song, Xuesen Du

Industrial sources, such as steel and power activities continue to emit substantial amounts of CO, but have not received the same level of attention as mobile sources due to a lack of relevant regulations. This work reports that a commercial Pt/Al2O3 catalyst used in vehicle CO catalytic converters may face severe selenium (Se) poisoning deactivation from industrial sources. The turnover frequency (TOF) of the Pt/Al2O3 catalyst (250 °C) decreased from 2.18 s−1 to 0.12 s−1 with only 0.49 wt% (ICP) Se deposition. Se deposition causes the Pt 5d orbital shift to a higher energy state, raising the oxidation state of platinum. As a result, the back-donation from the 5d electrons of Pt to the 2π* antibonding orbital of the adsorbed CO molecule is inhibited, weakening the bonding between Pt/Al2O3 and the CO antibonding orbital, thereby significantly reducing CO activation ability. DRIFTS results, combined with apparent and microscopic kinetics, indicate that the surface of Se deposited Pt/Al2O3 catalyst remains O* available (500 K, θO* = 0.16), and the rate-controlling step changes from O2 + 2* → 2O* to CO + * → CO*. The work suggests that the application of CO catalytic oxidation technology for industrial source should fully consider the toxic effect of Se, but is often neglected.

中文翻译:


硒调制的 Pt/Al2O3 电子结构在催化 CO 氧化过程中诱导失活



钢铁和电力活动等工业源继续排放大量一氧化碳,但由于缺乏相关法规,没有得到与移动源同等程度的关注。这项工作报道了用于车用 CO 催化转化器的商用 Pt/Al2O3 催化剂可能面临严重的工业来源硒 (Se) 中毒失活。Pt/Al2O3 催化剂的周转频率 (TOF) (250 °C) 从 2.18 s-1 下降到 0.12 s-1,只有 0.49 wt% (ICP) 的 Se 沉积。Se 沉积导致 Pt 5d 轨道移动到更高的能量态,从而提高铂的氧化态。结果,Pt 的 5d 电子向吸附的 CO 分子的 2π* 反键轨道的反向捐赠受到抑制,削弱了 Pt/Al2O3 与 CO 反键轨道之间的键合,从而显着降低了 CO 活化能力。DRIFTS 结果与表观和微观动力学相结合,表明 Se 沉积的 Pt/Al2O3 催化剂表面保持 O* 可用 (500 K,θO* = 0.16),速率控制步长从 O2 + 2* → 2O* 变为 CO + * → CO*。该工作提示,CO催化氧化技术在工业源中的应用应充分考虑Se的毒性作用,但往往被忽视。
更新日期:2024-11-22
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