Abstract
Catalytic methane decomposition is studied in a fixed bed reactor. Two sets of bimetallic catalysts are employed, namely: 30%Fe-X%Ce/Al2O3 and 30%Fe-X%Co/Al2O3, and compared with monometallic 30%Fe/Al2O3 catalyst. The effect of promoting Fe with Ce and Co and reduction temperature are investigated. The results reveal that Ce addition has shown a negative impact on H2 yield while a positive effect on H2 yield and catalyst stability are observed with Co addition. In terms of number of moles of produced hydrogen per active sites, Fe/Al2O3 has shown a higher number of moles of hydrogen compared to bimetallic catalysts. The catalyst reduced at 500 °C exhibits better activity as compared to the catalyst reduced at 950 °C. Carbon nano-tubes are deposited on the catalyst within the range of 14-73 nm diameter. Two types of carbon nanotubes are detected: Cα and Cγ.
Original language | English |
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Article number | 40 |
Journal | Catalysts |
Volume | 6 |
Issue number | 3 |
DOIs | |
State | Published - 8 Mar 2016 |
Externally published | Yes |
Bibliographical note
Publisher Copyright:© 2016 by the authors; licensee MDPI, Basel, Switzerland.
Keywords
- Carbon nano-tubes
- Ceria
- Cobalt
- Hydrogen
- Iron
ASJC Scopus subject areas
- Catalysis
- General Environmental Science
- Physical and Theoretical Chemistry