Abstract
The rational design of heterogeneous catalysts is crucial for identifying structure–performance relationships and understanding the nature of active site alteration during catalyst life cycles. In this study, the hydrogenation of CO2 to generate hydrocarbons was performed over a magnetite (Fe3O4)-based catalyst, and the structural evolution of the catalyst during long-term stability testing was comprehensively studied. The transformation of the α-Fe phase into Fe3O4 and χ-Fe5C2 phases after 100 h of reaction, followed by a decline in Fischer–Tropsch synthesis activity after 500 h, was attributed to the blockage of the χ-Fe5C2 phase by carbon deposition. Although oxidation of χ-Fe5C2 is an unavoidable process, the presence of a significant χ-Fe5C2 content after 500 h of reaction indicated that carbon deposition occurs, blocking the active sites and deactivating the catalyst. This behavior was clearly observed using temperature-programmed oxidation and Mössbauer spectroscopy, indicating that the deactivation and structural evolution of catalysts are strongly related during the CO2 hydrogenation reaction.
| Original language | English |
|---|---|
| Pages (from-to) | 648-656 |
| Number of pages | 9 |
| Journal | Journal of Industrial and Engineering Chemistry |
| Volume | 156 |
| DOIs | |
| State | Published - 25 Apr 2026 |
| Externally published | Yes |
Bibliographical note
Publisher Copyright:© 2025 The Korean Society of Industrial and Engineering Chemistry.
UN SDGs
This output contributes to the following UN Sustainable Development Goals (SDGs)
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SDG 13 Climate Action
Keywords
- CO hydrogenation
- Deactivation mechanism
- FeO catalyst
- Fischer–Tropsch synthesis
- Temperature-programmed oxidation
ASJC Scopus subject areas
- General Chemical Engineering
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