4.7 Article

Effect of Catalyst Crystallinity on V-Based Selective Catalytic Reduction with Ammonia

Journal

NANOMATERIALS
Volume 11, Issue 6, Pages -

Publisher

MDPI
DOI: 10.3390/nano11061452

Keywords

selective catalytic reduction; V-based catalyst; NOX removal efficiency; crystallinity; isotropic heating

Funding

  1. Korea Institute of Industrial Technology (KITECH) [JA200009]
  2. Ministry of Trade, Industry and Energy, South Korea (MOTIE) [20005721]
  3. National Research Foundation of Korea [NRF-2020R1C1C1013900, NRF-2017M3A7B4049466]
  4. Korea Evaluation Institute of Industrial Technology (KEIT) [20005721] Funding Source: Korea Institute of Science & Technology Information (KISTI), National Science & Technology Information Service (NTIS)
  5. National Research Council of Science & Technology (NST), Republic of Korea [JA200009] Funding Source: Korea Institute of Science & Technology Information (KISTI), National Science & Technology Information Service (NTIS)

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This study synthesized V2O5-WO3/TiO2 catalysts with different crystallinities using different heating methods and investigated the impact of crystallinity on acidity, surface species, and catalytic performance. The results showed that crystalline structure significantly enhanced the catalytic activity and stability of the catalyst.
In this study, we synthesized V2O5-WO3/TiO2 catalysts with different crystallinities via one-sided and isotropic heating methods. We then investigated the effects of the catalysts' crystallinity on their acidity, surface species, and catalytic performance through various analysis techniques and a fixed-bed reactor experiment. The isotropic heating method produced crystalline V2O5 and WO3, increasing the availability of both Bronsted and Lewis acid sites, while the one-sided method produced amorphous V2O5 and WO3. The crystalline structure of the two species significantly enhanced NO2 formation, causing more rapid selective catalytic reduction (SCR) reactions and greater catalyst reducibility for NOX decomposition. This improved NOX removal efficiency and N-2 selectivity for a wider temperature range of 200 degrees C-450 degrees C. Additionally, the synthesized, crystalline catalysts exhibited good resistance to SO2, which is common in industrial flue gases. Through the results reported herein, this study may contribute to future studies on SCR catalysts and other catalyst systems.

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