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HERO ID
1702734
Reference Type
Journal Article
Title
Catalytic dry reforming of methane over high surface area ceria
Author(s)
Laosiripojana, N; Assabumrungrat, S
Year
2005
Is Peer Reviewed?
Yes
Journal
Applied Catalysis B: Environmental
ISSN:
0926-3373
Publisher
Elsevier
Volume
60
Issue
1-2
Page Numbers
107-116
DOI
10.1016/j.apcatb.2005.03.001
Web of Science Id
WOS:000232328900012
URL
https://linkinghub.elsevier.com/retrieve/pii/S0926337305001268
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Abstract
High surface area ceria (CeO(2) (HSA)), synthesized by a surfactant-assisted approach, was found to have useful dry reforming activity for H(2) and CO production under solid oxide fuel cells (SOFCs) conditions. The catalyst provides significantly higher reforming reactivity and excellent resistance toward carbon deposition compared to Ni/Al(2)O(3) and conventional low surface area ceria (CeO(2) (LSA)) under dry reforming conditions. These enhancements are due to the high redox property of CeO(2) (HSA). During the dry reforming process, the redox reactions between the gaseous components in the system and the lattice oxygen (O(x)) take place on ceria surface. Among these reactions, the rapid redox reactions of carbon compounds such as CH(4), and CO with lattice oxygen (CH(4) + O(x) -> CO + H(2) + O(x-1) and CO + O(x) = CO(2) + O(x-1)) can prevent the formation of carbon species from the methane decomposition and Boudard reactions even at low inlet carbon dioxide concentration.
In particular, the dry reforming rate over CeO(2) (HSA) is proportional to the methane partial pressure and the operating temperature. Carbon dioxide presents weak positive impact on the methane conversion, whereas both carbon monoxide and hydrogen inhibit the reforming rate. The activation energies and reforming rates under the same methane concentration for CeO(2) toward the dry reforming are almost equal to the steam reforming as previously reported [1-4]. This result suggests the similar reaction mechanisms for both the steam reforming and the dry reforming over CeO(2); i.e., the dry reforming rate is governed by the slow reaction of adsorbed methane, or surface hydrocarbon species, with oxygen in CeO(2), and a rapid gas-solid reaction between CO(2) and CeO(2) to replenish the oxygen. (c) 2005 Elsevier B.V. All rights reserved.
Keywords
ceria; dry reforming; high surface area; hydrogen; SOFC
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