Particle Size and PdO–Support Interactions in PdO/CeO<sub>2</sub>-γ Al<sub>2</sub>O<sub>3</sub> Catalysts and Effect on Methane Combustion

In this study, we investigated the effects of sequential impregnation in two PdO/CeO<sub>2</sub>/Al<sub>2</sub>O<sub>3</sub> nanocatalysts (4Pd-20CeO<sub>2</sub>/Al<sub>2</sub>O<sub>3</sub> and 20CeO<sub>2</sub>-4Pd/...

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Main Authors: Domenica R. Fertal, Maxim P. Bukhovko, Yong Ding, Mehmet Z. Billor, Anil C. Banerjee
Format: Article
Language:English
Published: MDPI AG 2020-08-01
Series:Catalysts
Subjects:
Online Access:https://www.mdpi.com/2073-4344/10/9/976
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spelling doaj-9762f9b9a8b04999bc60b80ee6b83a932020-11-25T03:35:00ZengMDPI AGCatalysts2073-43442020-08-011097697610.3390/catal10090976Particle Size and PdO–Support Interactions in PdO/CeO<sub>2</sub>-γ Al<sub>2</sub>O<sub>3</sub> Catalysts and Effect on Methane CombustionDomenica R. Fertal0Maxim P. Bukhovko1Yong Ding2Mehmet Z. Billor3Anil C. Banerjee4Department of Chemistry, Columbus State University, Columbus, GA 31907, USADepartment of Chemical and Biomolecular Engineering, Georgia Institute of Technology, Atlanta, GA 30332, USASchool of Materials Science and Engineering, Georgia Institute of Technology, Atlanta, GA 30332, USADepartment of Geosciences, Auburn University, Auburn, AL 36849, USADepartment of Chemistry, Columbus State University, Columbus, GA 31907, USAIn this study, we investigated the effects of sequential impregnation in two PdO/CeO<sub>2</sub>/Al<sub>2</sub>O<sub>3</sub> nanocatalysts (4Pd-20CeO<sub>2</sub>/Al<sub>2</sub>O<sub>3</sub> and 20CeO<sub>2</sub>-4Pd/Al<sub>2</sub>O₃) on catalytic properties, particle sizes, and metal oxide–support interactions. Pulse chemisorption indicated significantly higher dispersion and smaller particle size in the 20CeO<sub>2</sub>-4Pd/Al<sub>2</sub>O₃ catalyst. STEM images of the 4Pd-20CeO<sub>2</sub>/Al<sub>2</sub>O₃ catalyst showed PdO nanoparticles on the surface of crystalline Al<sub>2</sub>O₃. In the 20CeO<sub>2</sub>-4Pd/Al<sub>2</sub>O<sub>3</sub> catalyst, PdO nanoparticles were strongly embedded on ceria indicating PdO-ceria interactions. Both supports were on separate sites in the two catalysts suggesting weak interactions. PdO particle sizes were 6–12 nm in the 4Pd-20CeO<sub>2</sub>/Al<sub>2</sub>O₃ catalyst and 4–8 nm in the 20CeO<sub>2</sub>-4Pd/Al<sub>2</sub>O₃ catalyst. Methane conversion was 100% at 275 °C after a 20-min run with the 4Pd-20CeO<sub>2</sub>/Al<sub>2</sub>O<sub>3</sub> catalyst compared to 25% conversion by the 20CeO<sub>2</sub>-4Pd/Al<sub>2</sub>O₃ catalyst under same conditions. The support alumina could stabilize the PdO species and facilitated oxygen migration on the surface and from the bulk in the 4Pd-20CeO<sub>2</sub>/Al<sub>2</sub>O<sub>3</sub> catalyst. The lower activities in the 20CeO<sub>2</sub>-4Pd/Al<sub>2</sub>O₃ catalyst could be due to inaccessibility of PdO active sites at low temperature due to embedment of PdO nanoparticles on ceria. We could infer from our data that sequence of impregnation in catalyst synthesis could significantly influence catalytic properties and methane combustion due to PdO–support interactions.https://www.mdpi.com/2073-4344/10/9/976sequential impregnationcatalyst preparation methodPdO–support interactionsparticle sizeparticle size distributionmethane combustion
collection DOAJ
language English
format Article
sources DOAJ
author Domenica R. Fertal
Maxim P. Bukhovko
Yong Ding
Mehmet Z. Billor
Anil C. Banerjee
spellingShingle Domenica R. Fertal
Maxim P. Bukhovko
Yong Ding
Mehmet Z. Billor
Anil C. Banerjee
Particle Size and PdO–Support Interactions in PdO/CeO<sub>2</sub>-γ Al<sub>2</sub>O<sub>3</sub> Catalysts and Effect on Methane Combustion
Catalysts
sequential impregnation
catalyst preparation method
PdO–support interactions
particle size
particle size distribution
methane combustion
author_facet Domenica R. Fertal
Maxim P. Bukhovko
Yong Ding
Mehmet Z. Billor
Anil C. Banerjee
author_sort Domenica R. Fertal
title Particle Size and PdO–Support Interactions in PdO/CeO<sub>2</sub>-γ Al<sub>2</sub>O<sub>3</sub> Catalysts and Effect on Methane Combustion
title_short Particle Size and PdO–Support Interactions in PdO/CeO<sub>2</sub>-γ Al<sub>2</sub>O<sub>3</sub> Catalysts and Effect on Methane Combustion
title_full Particle Size and PdO–Support Interactions in PdO/CeO<sub>2</sub>-γ Al<sub>2</sub>O<sub>3</sub> Catalysts and Effect on Methane Combustion
title_fullStr Particle Size and PdO–Support Interactions in PdO/CeO<sub>2</sub>-γ Al<sub>2</sub>O<sub>3</sub> Catalysts and Effect on Methane Combustion
title_full_unstemmed Particle Size and PdO–Support Interactions in PdO/CeO<sub>2</sub>-γ Al<sub>2</sub>O<sub>3</sub> Catalysts and Effect on Methane Combustion
title_sort particle size and pdo–support interactions in pdo/ceo<sub>2</sub>-γ al<sub>2</sub>o<sub>3</sub> catalysts and effect on methane combustion
publisher MDPI AG
series Catalysts
issn 2073-4344
publishDate 2020-08-01
description In this study, we investigated the effects of sequential impregnation in two PdO/CeO<sub>2</sub>/Al<sub>2</sub>O<sub>3</sub> nanocatalysts (4Pd-20CeO<sub>2</sub>/Al<sub>2</sub>O<sub>3</sub> and 20CeO<sub>2</sub>-4Pd/Al<sub>2</sub>O₃) on catalytic properties, particle sizes, and metal oxide–support interactions. Pulse chemisorption indicated significantly higher dispersion and smaller particle size in the 20CeO<sub>2</sub>-4Pd/Al<sub>2</sub>O₃ catalyst. STEM images of the 4Pd-20CeO<sub>2</sub>/Al<sub>2</sub>O₃ catalyst showed PdO nanoparticles on the surface of crystalline Al<sub>2</sub>O₃. In the 20CeO<sub>2</sub>-4Pd/Al<sub>2</sub>O<sub>3</sub> catalyst, PdO nanoparticles were strongly embedded on ceria indicating PdO-ceria interactions. Both supports were on separate sites in the two catalysts suggesting weak interactions. PdO particle sizes were 6–12 nm in the 4Pd-20CeO<sub>2</sub>/Al<sub>2</sub>O₃ catalyst and 4–8 nm in the 20CeO<sub>2</sub>-4Pd/Al<sub>2</sub>O₃ catalyst. Methane conversion was 100% at 275 °C after a 20-min run with the 4Pd-20CeO<sub>2</sub>/Al<sub>2</sub>O<sub>3</sub> catalyst compared to 25% conversion by the 20CeO<sub>2</sub>-4Pd/Al<sub>2</sub>O₃ catalyst under same conditions. The support alumina could stabilize the PdO species and facilitated oxygen migration on the surface and from the bulk in the 4Pd-20CeO<sub>2</sub>/Al<sub>2</sub>O<sub>3</sub> catalyst. The lower activities in the 20CeO<sub>2</sub>-4Pd/Al<sub>2</sub>O₃ catalyst could be due to inaccessibility of PdO active sites at low temperature due to embedment of PdO nanoparticles on ceria. We could infer from our data that sequence of impregnation in catalyst synthesis could significantly influence catalytic properties and methane combustion due to PdO–support interactions.
topic sequential impregnation
catalyst preparation method
PdO–support interactions
particle size
particle size distribution
methane combustion
url https://www.mdpi.com/2073-4344/10/9/976
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