Abstract
Catalytic methane decomposition is a promising technique for COx-free hydrogen production and carbon nanomaterials. In this research, iron-supported catalysts, prepared by successive wetness impregnation, were studied for methane decomposition at 700 °C. The results showed that Fe0 turned out to be the active site and greater metal-support interaction led to the formation of iron aluminate (FeAl2O4), both of which played a role in the catalytic activity performance. The 30Fe/Ce-Al catalyst performed the best catalytic activity in terms of maximum methane conversion (76%) and hydrogen production rate (1.04 mol/gMetal/s/surface area). The observation also suggested that the 10Fe/Ce-Al catalyst significantly deactivated due to metal particle agglomeration, as evidenced by negligible weight loss in thermogravimetric analysis. In contrast, the 20Fe/Ce-Al and 30Fe/Ce-Al catalysts were deactivated from both agglomeration and carbon deposition. The surface morphology analysis of the spent catalyst indicated that the deposited carbon was multiwalled carbon nanotubes that followed the base-growth mechanism.
Original language | English |
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Pages (from-to) | 18869-18878 |
Number of pages | 10 |
Journal | Industrial and Engineering Chemistry Research |
Volume | 63 |
Issue number | 44 |
DOIs | |
State | Published - 6 Nov 2024 |
Bibliographical note
Publisher Copyright:© 2024 American Chemical Society.
ASJC Scopus subject areas
- General Chemistry
- General Chemical Engineering
- Industrial and Manufacturing Engineering