催化作用
选择性
烧结
材料科学
金属
铂金
水煤气变换反应
Atom(片上系统)
人口
化学工程
化学
纳米技术
结晶学
冶金
有机化学
计算机科学
人口学
社会学
工程类
嵌入式系统
作者
Ewa Chukwu,Lindsay Molina,Conner Rapp,Luis A. Morales,Zehua Jin,S. Karakalos,Hui Wang,Sungsik Lee,Michael J. Zachman,Ming Yang
标识
DOI:10.1016/j.apcatb.2023.122532
摘要
Increasing the surface population of supported catalytic sites, assuming these sites are stable, is considered a straightforward approach to improving the overall catalytic performance. We report an exception represented by the Pt/α-MoC catalysts featuring atomically dispersed Pt. The Pt/α-MoC catalysts display very high activity for the reverse water gas shift reaction with near 100% CO selectivity for CO2:H2 ratios from 0.25 to 4 and from 250 to 400 °C. Despite the excellent performance, the intrinsic activity per Pt-centric catalytic center declines as the Pt loading increases from 0.1 to 1.0 wt%. With the dispersed Pt evolving from isolated atoms to fully exposed ensembles, the shrinking inter-Pt-atom space impedes CO2 activation at the critical Pt-Mo interfaces, where the Pt shall temporarily take the -O intermediates. The Pt, even as atomically dispersed without noticeable sintering, is underutilized in such a crowded state. This caution for high-loading catalyst design is translational to other systems where the direct catalytic roles of the supports are crucial.
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