Catalytic H2O and CO2 reforming of CH4 over perovskite-based La0.8Sr0.2Cr0.9Ni 0.1O3: Effects of pre-treatment and co-reactant/CH 4 on its reforming characteristics
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Author list: Chettapongsaphan C., Charojrochkul S., Assabumrungrat S., Laosiripojana N.
Publisher: Elsevier
Publication year: 2010
Journal: Applied Catalysis A: General (0926-860X)
Volume number: 386
Issue number: #
Start page: 194
End page: 200
Number of pages: 7
ISSN: 0926-860X
eISSN: 1873-3875
Languages: English-Great Britain (EN-GB)
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Abstract
The H2O and CO2 reformings of CH4 over perovskite-based La0.8Sr0.2Cr0.9Ni 0.1O3 prepared by precipitation, sol-gel and surfactant-assisted methods (calcined with air, nitrogen and hydrogen) were studied under solid oxide fuel cell (SOFC) conditions. It was found that the catalyst prepared by the surfactant-assisted method and calcined with hydrogen provided the highest specific surface area and reforming reactivity. Under typical conditions (H2O/CH4 and CO2/CH 4 of 1.0), the reforming reactivity of La0.8Sr 0.2Cr0.9Ni0.1O3 was comparable to that of Ni/Al2O3 but relatively less than that of precious-metal Rh/Al2O3. Nevertheless, at specific condition (H2O/CH4 and CO2/CH4 of 0.5-0.7), its activity dramatically increased to the same level as that of Rh/Al2O3. According to the study on the kinetic dependencies of La0.8Sr0.2Cr0.9Ni 0.1O3, the reforming rate was proportional to CH 4 partial pressure with the reaction order increased from 0.50 (at co-reactant/CH4 ratio of 1.0-3.0) to 0.95 (at co-reactant/CH 4 ratio of 0.5). In addition, the rate was inhibited by H2 addition at high inlet co-reactant/CH4 ratio; however the inhibitory effect becomes less pronounced at an inlet co-reactant/CH4 ratio less than 0.7. It is suggested that one of two reforming mechanisms occurred depending on the operating conditions applied. La0.8Sr 0.2Cr0.9Ni0.1O3 behaves like an oxide-based catalyst at high co-reactant/CH4 ratio, whereas it tends to behave more like a metallic-based catalyst at low co-reactant/CH4 ratios resulting in the high reforming reactivity. The study has shown that high surface area perovskite-based La0.8Sr0.2Cr 0.9Ni0.1O3 catalyst has great potential to be applied as a steam reforming catalyst since it requires low inlet steam content, which provides significant benefits in terms of minimizing the water management in reformer and SOFC systems. ฉ 2010 Elsevier B.V. All rights reserved.
Keywords
Reforming, SOFC
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