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Journal ArticleDOI

Catalytic dry reforming of methane over high surface area ceria

TLDR
In this article, high surface area ceria (CeO 2) was synthesized by a surfactant-assisted approach, which has useful dry reforming activity for H 2 and CO production under solid oxide fuel cells (SOFCs) conditions.
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.

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Citations
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Catalytic steam reforming of ethanol over high surface area CeO2: The role of CeO2 as an internal pre-reforming catalyst

TL;DR: In this paper, high surface area ceria (CeO2) was used as an internal pre-reforming catalyst for ethanol steam reforming in an annular ceramic reactor.
Journal ArticleDOI

Ni-containing Ce-promoted hydrotalcite derived materials as catalysts for methane reforming with carbon dioxide at low temperature – On the effect of basicity

TL;DR: In this article, NiMgAl mixed oxides promoted with cerium species were synthesized from their corresponding hydrotalcite precursors and subsequently characterized by elemental analysis, XRD, H2-TPR, CO 2-TPD and N2 sorption techniques.
Journal ArticleDOI

Production of syngas via autothermal reforming of methane in a fluidized-bed reactor over the combined CeO2–ZrO2/SiO2 supported Ni catalysts

TL;DR: In this paper, a series of combined CeO2-ZrO2/SiO2 supported Ni catalysts were investigated for the production of syngas via autothermal reforming of methane (MATR) in a fluidized bed reactor.
Journal ArticleDOI

Experimental investigation of direct internal reforming of biogas in solid oxide fuel cells

TL;DR: In this article, the authors investigated the behavior of planar solid oxide fuel cells (SOFCs) fed by two different fuel mixtures that simulate biogases coming from anaerobic digestion.
Journal ArticleDOI

Biogas reforming for syngas production over nickel supported on ceria–alumina catalysts

TL;DR: In this paper, a series of 8-wt% nickel catalysts supported on alumina and alumina-modified with different amounts of ceria were prepared and the effect of the supporting ceria loading at the catalytic performance for the biogas reforming reaction was investigated.
References
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Journal ArticleDOI

Ordered mesoporous molecular sieves synthesized by a liquid-crystal template mechanism

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Journal ArticleDOI

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Journal ArticleDOI

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Journal ArticleDOI

The multiple roles for catalysis in the production of H2

TL;DR: A review of the use of catalysis for the current and future production of H2 can be found in this article, where a number of different, largely catalytic approaches for producing H2 are described.
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