<p>Despite considerable progress in oxide–zeolite (OX–ZEO) bifunctional catalysts for ketene-mediated syngas conversion, the origin of inter-component synergy and its dependence on spatial proximity remain unclear. Here we develop a diffusion-bridged, two-component microkinetic model that incorporates the entire reaction network over the ZnCrO<sub><i>x</i></sub>/mordenite (MOR) catalyst. The model captures the coupled reaction–diffusion dynamics and quantitatively elucidates the synergetic mechanism underlying selective syngas-to-light-olefin conversion. We show that MOR enhances light-olefin selectivity by overcoming the thermodynamic limitation of CH<sub>2</sub>CO formation on the oxide via a more favourable pathway. Furthermore, the model predicts an inverted U-shaped dependence of light-olefin selectivity with proximity, arising from a balance between intermediate transfer and Zn migration, the latter generating [ZnOH]<sup>+</sup> species that promote undesired hydrogenation. More broadly, we establish a general reaction–diffusion coupling kinetic framework that quantifies the optimal combination principles for OX–ZEO systems. The predictions agree well with experimental observations and provide guidance for designing high-performance bifunctional catalysts.</p><p></p>

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The kinetic basis of bifunctional OX–ZEO catalysts for syngas conversion to light olefins

  • Zhuangzhuang Lai,
  • Danfeng Xiong,
  • Peijun Hu,
  • Jianfu Chen,
  • Haifeng Wang

摘要

Despite considerable progress in oxide–zeolite (OX–ZEO) bifunctional catalysts for ketene-mediated syngas conversion, the origin of inter-component synergy and its dependence on spatial proximity remain unclear. Here we develop a diffusion-bridged, two-component microkinetic model that incorporates the entire reaction network over the ZnCrOx/mordenite (MOR) catalyst. The model captures the coupled reaction–diffusion dynamics and quantitatively elucidates the synergetic mechanism underlying selective syngas-to-light-olefin conversion. We show that MOR enhances light-olefin selectivity by overcoming the thermodynamic limitation of CH2CO formation on the oxide via a more favourable pathway. Furthermore, the model predicts an inverted U-shaped dependence of light-olefin selectivity with proximity, arising from a balance between intermediate transfer and Zn migration, the latter generating [ZnOH]+ species that promote undesired hydrogenation. More broadly, we establish a general reaction–diffusion coupling kinetic framework that quantifies the optimal combination principles for OX–ZEO systems. The predictions agree well with experimental observations and provide guidance for designing high-performance bifunctional catalysts.