Methane dry reforming over ceria-zirconia supported Ni catalysts

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Methane dry reforming over ceria-zirconia supported Ni catalysts

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作者：Astrid Wolfbeisser^a ; ^{astrid.wolfbeisser@tuwien.ac.at" class="auth_mail" title="E-mail the corresponding author} ; Onsulang Sophiphun^b ; ^{onsulang_111@hotmail.com" class="auth_mail" title="E-mail the corresponding author} ; Johannes Bernardi^c ; ^{bernardi@ustem.tuwien.ac.at" class="auth_mail" title="E-mail the corresponding author} ; Jatuporn Wittayakun^b ; ^{jatuporn@sut.ac.th" class="auth_mail" title="E-mail the corresponding author} ; Karin Fö ; ttinger^a ; ^{karin.foettinger@tuwien.ac.at" class="auth_mail" title="E-mail the corresponding author} ; Gü ; nther Rupprechter^a ; ^{guenther.rupprechter@tuwien.ac.at" class="auth_mail" title="E-mail the corresponding author}
关键词：Methane dry reforming ; Nickel nanoparticles ; Ceria-zirconia ; Mixed oxides ; Coke ; Coprecipitation
刊名：Catalysis Today
出版年：2016
出版时间：15 November 2016
年：2016
卷：277
期：part_P2
页码：234-245
全文大小：3262 K

文摘

•: r0005">Ni-ceria/zirconia mixed oxides were applied for methane dry reforming.
•: r0010">Catalysts structure and properties strongly depend on the synthesis procedure.
•: r0015">Catalytic activity depends on preparation rather than nominal composition.
•: r0020">No improvement of catalytic activity by ceria-zirconia support compared to Ni-zirconia, but significantly increased stability against filamentous coke formation.
•: r0025">Less filamentous carbon formation reduces risk of reactor tube blocking.

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