New Insight into the Interplay of Method of Deposition, Chemical State of Pd, Oxygen Storage Capability and Catalytic Activity of Pd-Containing Perovskite Catalysts for Combustion of Methane

Elaboration of Pd-supported catalysts for catalytic combustion is, nowadays, considered as an imperative task to reduce the emissions of methane. This study provides new insight into the method of deposition, chemical state of Pd and oxygen storage capability of transition metal ions and their effec...

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Bibliographic Details
Main Authors: Silva Stanchovska, Georgy Ivanov, Sonya Harizanova, Krasimir Tenchev, Ekaterina Zhecheva, Anton Naydenov, Radostina Stoyanova
Format: Article
Language:English
Published: MDPI AG 2021-11-01
Series:Catalysts
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Online Access:https://www.mdpi.com/2073-4344/11/11/1399
Description
Summary:Elaboration of Pd-supported catalysts for catalytic combustion is, nowadays, considered as an imperative task to reduce the emissions of methane. This study provides new insight into the method of deposition, chemical state of Pd and oxygen storage capability of transition metal ions and their effects on the catalytic reactivity of supported catalysts for the combustion of methane. The catalyst with nominal composition La(Co<sub>0.8</sub>Ni<sub>0.1</sub>Fe<sub>0.1</sub>)<sub>0.85</sub>Pd<sub>0.15</sub>O<sub>3</sub> was supported on SiO<sub>2</sub>-modified/γ-alumina using two synthetic procedures: (i) aerosol assisted chemical vapor deposition (U-AACVD) and (ii) wet impregnation (Imp). A comparative analysis shows that a higher catalytic activity is established for supported catalyst obtained by wet impregnation, where the PdO-like phase is well dispersed and the transition metal ions display a high oxygen storage capability. The reaction pathway over both catalysts proceeds most probably through Mars–van Krevelen mechanism. The supported catalysts are thermally stable when they are aged at 505 °C for 120 h in air containing 1.2 vol.% water vapor. Furthermore, the experimentally obtained data on La(Co<sub>0.8</sub>Ni<sub>0.1</sub>Fe<sub>0.1</sub>)<sub>0.85</sub>Pd<sub>0.15</sub>O<sub>3</sub>—based catalyst, supported on monolithic substrate VDM<sup>®</sup>Aluchrom Y Hf are simulated by using a two-dimensional heterogeneous model for monolithic reactor in order to predict the performance of an industrial catalytic reactor for abatement of methane emissions.
ISSN:2073-4344