摘要
Developing highly efficient, stable, and wide-temperature NH 3 -SCR catalysts is one of the major challenges in industrial NO x emission control. Herein, we present an oxide-zeolite (OXZEO) hybrid design strategy for overcoming the challenge by spatially separating the NH 3 storage and redox functions via isolated zeolitic Brønsted (B) acid sites, in contrast to conventional regulation strategies that rely on Lewis acid sites. Through a combination of in situ spectroscopy, in situ mass spectrometry, ab initio molecular dynamics, and density functional theory, we identify a previously unrecognized denitrification (deNO x ) mechanism unique to the OXZEO system. Zeolitic B acid sites act as highly regulated NH 3 storage, and the stored NH 3 desorbs and migrates to oxide active sites as NH 3 and NH 4 + , the latter effectively suppressing high-temperature NH 3 over-oxidation. Using CeSnO x /Beta as the main model system for mechanistic investigation, we further demonstrate that this strategy can be generally extended to diverse zeolite topologies (BEA, CHA, MFI, FAU) and Ce-/Mn-based oxides, affording catalysts that achieve >80% NO x conversion and ~100% N 2 selectivity over a temperature window exceeding 300 °C. This work highlights zeolite-mediated NH 3 storage in deNO x , providing mechanistic insight into OXZEO structure-property relationships and guiding the development of next-generation NH 3 -SCR catalysts.
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