TY - JOUR
T1 - Fe-Ce-Al Catalysts for Decomposition of Methane to High Purity Hydrogen and High-Value Carbon
AU - Hantoko, Dwi
AU - Khan, Wasim Ullah
AU - Putra, Achmad Ferdiansyah Pradana
AU - Shoaibi, Ahmed Al
AU - Chandrasekar, Srinivasakannan
AU - Hossain, Mohammad M.
N1 - Publisher Copyright:
© 2024 American Chemical Society.
PY - 2024/11/6
Y1 - 2024/11/6
N2 - 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.
AB - 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.
UR - https://www.scopus.com/pages/publications/85208680790
U2 - 10.1021/acs.iecr.4c02856
DO - 10.1021/acs.iecr.4c02856
M3 - Article
AN - SCOPUS:85208680790
SN - 0888-5885
VL - 63
SP - 18869
EP - 18878
JO - Industrial and Engineering Chemistry Research
JF - Industrial and Engineering Chemistry Research
IS - 44
ER -