CH<sub>4</sub> Oxidation on LaFeO<sub>3</sub> Perovskite Catalysts for O<sub>2</sub> Removal from Biomethane

Abstract For the introduction of biomethane into the natural gas grid, the removal of O 2 is mandatory. Thus, the conversion of O 2 with excess CH 4 was investigated using LaFeO 3 catalysts. The variation of calcination temperature led to LaFeO 3 perovskites with different properties as deduced from extensive physical‐chemical characterization. From coupling the characteristics with the catalytic performance, a structure–activity correlation was derived showing that BET surface area and crystalline structure are determining features. Consequently, the most active LaFeO 3 exhibited complete O 2 conversion already at 310 °C. Kinetic modeling based on a Langmuir–Hinshelwood mechanism provided suitable operation parameters for a plug flow reactor. The model was validated by predicting experiments.

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Publication Details

Journal
Chemical Engineering & Technology
Published
2025-03-01
DOI
https://doi.org/10.1002/ceat.12012
Citations
1
Primary Topic
Catalytic Processes in Materials Science
Type
article
Field-Weighted Citation Impact
0.52
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article

CH4 Oxidation on LaFeO3 Perovskite Catalysts for O2 Removal from Biomethane

Hendrik Wollmerstädt, Norman Schreiter, Sven Kureti, Andrej Awgustow
1 citations
Chemical Engineering & Technology
Catalytic Processes in Materials Science
0.52
article

CH4 Oxidation on LaFeO3 Perovskite Catalysts for O2 Removal from Biomethane

Hendrik Wollmerstädt, Norman Schreiter, Sven Kureti, Andrej Awgustow
article en
1 citations

Abstract

Abstract For the introduction of biomethane into the natural gas grid, the removal of O 2 is mandatory. Thus, the conversion of O 2 with excess CH 4 was investigated using LaFeO 3 catalysts. The variation of calcination temperature led to LaFeO 3 perovskites with different properties as deduced from extensive physical‐chemical characterization. From coupling the characteristics with the catalytic performance, a structure–activity correlation was derived showing that BET surface area and crystalline structure are determining features. Consequently, the most active LaFeO 3 exhibited complete O 2 conversion already at 310 °C. Kinetic modeling based on a Langmuir–Hinshelwood mechanism provided suitable operation parameters for a plug flow reactor. The model was validated by predicting experiments.

Chemical Engineering & TechnologyVol. 48(3)
TU Bergakademie Freiberg (DE)
Openalex Percentile: Top 41%
Catalytic Processes in Materials Science
0.52
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