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Frontiers of Environmental Science & Engineering

ISSN 2095-2201

ISSN 2095-221X(Online)

CN 10-1013/X

Postal Subscription Code 80-973

2018 Impact Factor: 3.883

Front. Environ. Sci. Eng.    2022, Vol. 16 Issue (5) : 60    https://doi.org/10.1007/s11783-022-1539-2
RESEARCH ARTICLE
CeO2 doping boosted low-temperature NH3-SCR activity of FeTiOx catalyst: A microstructure analysis and reaction mechanistic study
Wei Tan1,2, Shaohua Xie1, Wenpo Shan3,4, Zhihua Lian3,4, Lijuan Xie3, Annai Liu5, Fei Gao2, Lin Dong2, Hong He3,4, Fudong Liu1()
1. Department of Civil, Environmental, and Construction Engineering, Catalysis Cluster for Renewable Energy and Chemical Transformations (REACT), NanoScience Technology Center (NSTC), University of Central Florida, Orlando, FL32816, USA
2. Key Laboratory of Mesoscopic Chemistry of MOE, School of Chemistry and Chemical Engineering, Jiangsu Key Laboratory of Vehicle Emissions Control, School of Environment, Center of Modern Analysis, Nanjing University, Nanjing 210023, China
3. State Key Joint Laboratory of Environment Simulation and Pollution Control, Research Center for Eco-Environmental Sciences, Chinese Academy of Sciences, Beijing 100085, China
4. Key Laboratory of Urban Pollutant Conversion, Institute of Urban Environment, Chinese Academy of Sciences, Xiamen 361021, China
5. Institute of Engineering Technology, Sinopec Catalyst Co. Ltd., Sinopec Group, Beijing 101111, China
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Abstract

• CeO2 doping significantly improved low-temperature NH3-SCR activity on FeTiOx.

• The crystallinity of FeTiOx was decreased dramatically after CeO2 doping.

• Unique Ce-O-Fe structure in FeCe0.2TiOx accounted for its superior redox property.

• Facile activation of NH3 to-NH2 on FeCe0.2TiOx promoted the DeNOx efficiency.

FeTiOx has been recognized as an environmental-friendly and cost-effective catalyst for selective catalytic reduction (SCR) of NOx with NH3. Aimed at further improving the low-temperature DeNOx efficiency of FeTiOx catalyst, a simple strategy of CeO2 doping was proposed. The low-temperature (<250℃) NH3-SCR activity of FeTiOx catalyst could be dramatically enhanced by CeO2 doping, and the optimal composition of the catalyst was confirmed as FeCe0.2TiOx, which performed a NOx conversion of 90% at ca. 200℃. According to X-ray diffraction (XRD), Raman spectra and X-ray absorption fine structure spectroscopy (XAFS) analysis, FeCe0.2TiOx showed low crystallinity, with Fe and Ce species well mixed with each other. Based on the fitting results of extended X-ray absorption fine structure (EXAFS), a unique Ce-O-Fe structure was formed in FeCe0.2TiOx catalyst. The well improved specific surface area and the newly formed Ce-O-Fe structure dramatically contributed to the improvement of the redox property of FeCe0.2TiOx catalyst, which was well confirmed by H2-temperature-programmed reduction (H2-TPR) and in situ XAFS experiments. Such enhanced redox capability could benefit the activation of NO and NH3 at low temperatures for NOx removal. The detailed reaction mechanism study further suggested that the facile oxidative dehydrogenation of NH3 to highly reactive-NH2 played a key role in enhancing the low-temperature NH3-SCR performance of FeCe0.2TiOx catalyst.

Keywords NH3-SCR      CeO2 doping      Low-temperature NOx removal      Improved redox property      In situ XAFS analysis     
Corresponding Author(s): Fudong Liu   
Issue Date: 26 January 2022
 Cite this article:   
Wei Tan,Shaohua Xie,Wenpo Shan, et al. CeO2 doping boosted low-temperature NH3-SCR activity of FeTiOx catalyst: A microstructure analysis and reaction mechanistic study[J]. Front. Environ. Sci. Eng., 2022, 16(5): 60.
 URL:  
https://academic.hep.com.cn/fese/EN/10.1007/s11783-022-1539-2
https://academic.hep.com.cn/fese/EN/Y2022/V16/I5/60
Fig.1  (a) The NH3-SCR activity over FeTiOx and FeCeaTiOx catalysts (a = 0.1, 0.2, 0.6, 1 and 1.6) under GHSV of 50000 h-1. (b) The NOx conversion as a function of reaction time in NH3-SCR reaction over FeCe0.2TiOx catalyst in the presence of 100 ppm SO2 or/and 5% H2O at 250℃ under the GHSV of 50000 h-1.
Fig.2  (a) XRD patterns and (b) Raman spectra for FeTiOx and FeCeaTiOx catalysts with reference oxides.
Fig.3  (a) Normalized XANES spectra of Fe K-edge in Fe2O3, FeTiOx and FeCeaTiOx catalysts, (b) Fourier transforms of filtered EXAFS oscillations k3χ(k) into R space for Fe K-edge in Fe2O3, FeTiOx and FeCeaTiOx catalysts. (c) Normalized XANES spectra of Ce K-edge in CeO2 and FeCeaTiOx catalysts, (d) Fourier transforms of filtered EXAFS oscillations k3χ(k) into R space for Ce K-edge in CeO2 and FeCeaTiOx catalysts (the inserted figure was the inverse Fourier transformed EXAFS oscillations in FeCe0.1TiOx and FeCe0.2TiOx in the R range of ca. 2.3–3.2 Å, in which the dotted lines were related to the calculated EXAFS oscillations of Ce-O-Fe bond using FEFF8.4 code)。
Fig.4  (a) NH3-TPD profiles for FeTiOx and FeCe0.2TiOx catalysts; (b) In situ DRIFTS of NH3 adsorption on FeTiOx and FeCe0.2TiOx catalysts at 150℃ collected in N2 flow.
Fig.5  H2-TPR profiles for FeTiOx and FeCe0.2TiOx catalysts, with TiO2, CeO2 and Fe2O3 as reference samples.
Fig.6  The normalized in situ Fe K-edge XANES for (a) FeTiOx and (b) FeCe0.2TiOx catalysts in the H2-TPR process from room temperature to 900℃ (the inserted figures showed the normalized in situ Fe K-edge XANES with an interval of 50℃ for better discrimination); In situ EXAFS spectra of Fe K-edge for (c) FeTiOx and (d) FeCe0.2TiOx catalysts during the H2-TPR process.
Fig.7  In situ DRIFTS of (a) NO+ O2 reacting with pre-adsorbed NH3 species; (b) NH3 reacting with pre-adsorbed NOx species; (c) NH3-SCR reaction at 150℃ over FeTiOx. The FTIR spectra were collected in varied reactant flow according to the needs of the experiments.
Fig.8  In situ DRIFTS of (a) NO+ O2 reacting with pre-adsorbed NH3 species; (b) NH3 reacting with pre-adsorbed NOx species; (c) NH3-SCR reaction at 150℃ over FeCe0.2TiOx. The FTIR spectra were collected in varied reactant flow according to the needs of the experiments.
Fig.9  (a) In situ DRIFTS of NH3-SCR reaction on FeTiOx and FeCe0.2TiOx at 150℃ collected in the NH3-SCR reaction flow. (b) The scheme of the reaction pathway on FeTiOx and FeCe0.2TiOx at 150℃.
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