Comparative study on K‐tolerance performance of Fe/ZrO2 and Fe/ZrO2‐W catalysts for NH3‐SCR of NOx

BACKGROUND Selective catalytic reduction (SCR) of nitrous oxides (NOx) with ammonia (NH3) as reductant is used worldwide in mobile and stationary sources to reach strict emission standards. It is a feasible strategy to modify support with acidic metal oxides to improve the alkali metal potassium (K)...

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Veröffentlicht in:Journal of chemical technology and biotechnology (1986) 2023-09, Vol.98 (9), p.2343-2353
Hauptverfasser: Xu, Duo, Han, Zhitao, Li, Yeshan, Lu, Shijian, Pan, Xinxiang
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Sprache:eng
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Zusammenfassung:BACKGROUND Selective catalytic reduction (SCR) of nitrous oxides (NOx) with ammonia (NH3) as reductant is used worldwide in mobile and stationary sources to reach strict emission standards. It is a feasible strategy to modify support with acidic metal oxides to improve the alkali metal potassium (K) tolerance of SCR catalysts. Herein, a comparative investigation was conducted based on iron/zirconium dioxide (Fe/ZrO2)and Fe/ZrO2‐tungsten (W) catalysts to reveal the correlation of support modification with W and K‐tolerance performance. RESULTS The NOx conversion for K‐Fe/ZrO2 catalyst was 80%). CONCLUSION According to the characterization results, it was found that K‐species impose a negative impact on NH3 adsorption on the surface of the Fe/ZrO2 catalyst, especially drastically preventing the adsorption of NH3 species on Brønsted acid sites, thus inhibiting the occurrence of SCR reactions via the Langmuir–Hinshelwood (L‐H) mechanism. By contrast, W modification resulted in more chemisorbed oxygen, stronger redox capacity and an increased Fe3+/(Fe3++Fe2+) ratio on the surface of the Fe/ZrO2‐W catalyst. More importantly, W modification brought about abundant Brønsted acid sites, significantly promoting NH3 adsorption and activation. W modification also weakened the adsorption stability of NOx species to a certain extent. As a result, SCR reactions over the Fe/ZrO2‐W catalyst could proceed via both Eley–Rideal (E‐R) and L‐H pathways. © 2023 Society of Chemical Industry (SCI).
ISSN:0268-2575
1097-4660
DOI:10.1002/jctb.7463