Tuning the metal loading of Pt/CeO2 catalysts for the water-gas shift reaction

被引:0
作者
Molinet-Chinaglia C. [1 ]
Cardenas L. [1 ]
Vernoux P. [1 ]
Piccolo L. [1 ]
Loridant S. [1 ]
机构
[1] Université Claude Bernard-Lyon 1, CNRS, IRCELYON, UMR 5256, Villeurbanne
来源
Materials Today Catalysis | 2024年 / 4卷
关键词
Metallic Pt nanoparticles; Oxidized Pt single atoms and clusters; Pt/CeO[!sub]2[!/sub] catalyst; Structural dynamics; Water-gas shift reaction;
D O I
10.1016/j.mtcata.2024.100046
中图分类号
学科分类号
摘要
Identifying active platinum species at the surface of Pt/CeO2 catalysts is still a hot topic in the literature. In this work, an oxidizing pretreatment at 500 °C was applied to generate ultradispersed PtOx species before the reaction. It is shown that the molar activity of such catalysts for the water-gas shift reaction is strongly dependent on the platinum content, increasing by a factor of 2.5 from 0.1 to 0.6 wt% and stabilizing from 0.6 to 1.4 wt%. The tracking of Pt species present under reaction conditions (230 °C, H2O/CO=4) was performed using operando DRIFT spectroscopy, CO-TPR and STEM in connection with the catalytic activity. A major structural change was found for Pt loadings above 0.6 wt% through the formation of metallic Pt0 nanoparticles of ca 1.4 nm from oxidized Pt single atoms and clusters. Conversely, for Pt contents below 0.6 wt%, Pt species possess a stronger interaction with CeO2 as well as a lower nuclearity, limiting their activation under reaction conditions. This strongly suggests that metallic Pt nanoparticles, prevalent at high loading, are more active than oxidic Pt single atoms and small clusters, which are predominantly present at low loading. This study highlights the key role of PtOx reducibility and the importance to optimize the Pt loading to obtain active catalysts for the water-gas shift reaction. © 2024 The Authors
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共 75 条
[1]  
Ratnasamy C., Wagner J.P., Water gas shift catalysis, Catal. Rev., 51, pp. 325-440, (2009)
[2]  
Gradisher L., Dutcher B., Fan M., Catalytic hydrogen production from fossil fuels via the water gas shift reaction, Appl. Energy, 139, pp. 335-349, (2015)
[3]  
Roh H.-S., Jeong D.-W., Kim K.-S., Eum I.-H., Koo K.Y., Yoon W.L., Single stage water–gas shift reaction over supported Pt catalysts, Catal. Lett., 141, pp. 95-99, (2011)
[4]  
Panagiotopoulou P., Papavasiliou J., Avgouropoulos G., Ioannides T., Kondarides D.I., Water–gas shift activity of doped Pt/CeO2 catalysts, Chem. Eng. J., 134, pp. 16-22, (2007)
[5]  
Thinon O., Diehl F., Avenier P., Schuurman Y., Screening of bifunctional water-gas shift catalysts, Catal. Today, 137, pp. 29-35, (2008)
[6]  
Kalamaras C.M., Gonzalez I.D., Navarro R.M., Fierro J.L.G., Efstathiou A.M., Effects of reaction temperature and support composition on the mechanism of water–gas shift reaction over supported-Pt catalysts, J. Phys. Chem. C, 115, pp. 11595-11610, (2011)
[7]  
Aranifard S., Ammal S.C., Heyden A., On the importance of the associative carboxyl mechanism for the water-gas shift reaction at Pt/CeO<sub>2</sub> interface sites, J. Phys. Chem. C, 118, pp. 6314-6323, (2014)
[8]  
Aranifard S., Ammal S.C., Heyden A., On the importance of metal–oxide interface sites for the water–gas shift reaction over Pt/CeO<sub>2</sub> catalysts, J. Catal., 309, pp. 314-324, (2014)
[9]  
Zhai Y., Pierre D., Si R., Deng W., Ferrin P., Nilekar A.U., Peng G., Herron J.A., Bell D.C., Saltsburg H., Mavrikakis M., Flytzani-Stephanopoulos M., Alkali-stabilized Pt-OHx species catalyze low-temperature water-gas shift reactions, Science, 329, pp. 1633-1636, (2010)
[10]  
Vecchietti J., Bonivardi A., Xu W., Stacchiola D., Delgado J.J., Calatayud M., Collins S.E., Understanding the role of oxygen vacancies in the water gas shift reaction on ceria-supported platinum catalysts, ACS Catal., 4, pp. 2088-2096, (2014)