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Hydrogen Generation Using a CuO/ZnO-ZrO(2) Nanocatalyst for Autothermal Reforming of Methanol in a Microchannel Reactor
In the present work, a microchannel reactor for autothermal reforming of methanol using a synthesized catalyst porous alumina support-CuO/ZnO mixed with ZrO(2) sol washcoat has been developed and its fine structure and inner surface characterized. Experimentally, CuO/ZnO and alumina support with ZrO...
Autores principales: | , , , , , |
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Formato: | Online Artículo Texto |
Lenguaje: | English |
Publicado: |
MDPI
2011
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Materias: | |
Acceso en línea: | https://www.ncbi.nlm.nih.gov/pmc/articles/PMC6259188/ https://www.ncbi.nlm.nih.gov/pubmed/21217601 http://dx.doi.org/10.3390/molecules16010348 |
Sumario: | In the present work, a microchannel reactor for autothermal reforming of methanol using a synthesized catalyst porous alumina support-CuO/ZnO mixed with ZrO(2) sol washcoat has been developed and its fine structure and inner surface characterized. Experimentally, CuO/ZnO and alumina support with ZrO(2) sol washcoat catalyst (catalyst slurries) nanoparticles is the catalytically active component of the microreactor. Catalyst slurries have been dried at 298 K for 5 h and then calcined at 623 K for 2 h to increase the surface area and specific pore structures of the washcoat catalyst. The surface area of BET N(2) adsorption isotherms for the as-synthesized catalyst and catalyst/ZrO(2) sol washcoat samples are 62 and 108 ± 2 m(2)g(−1), respectively. The intensities of Cu content from XRD and XPS data indicate that Al(2)O(3) with Cu species to form CuAl(2)O(4). The EXAFS data reveals that the Cu species in washcoat samples have Cu-O bonding with a bond distance of 1.88 ± 0.02 Å and the coordination number is 3.46 ± 0.05, respectively. Moreover, a hydrogen production rate of 2.16 L h(−1) is obtained and the corresponding methanol conversion is 98% at 543 K using the CuO/ZnO with ZrO(2) sol washcoat catalyst. |
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