Effect of Support Particle Size in Steam Reforming of Ethanol over Co/CeO2 Catalysts

Effect of Support Particle Size in Steam Reforming of Ethanol over Co/CeO2 Catalysts
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DOI:
10.1021/cs3004159
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发表时间:
2012-11-01
期刊:
影响因子:
12.9
通讯作者:
Ozkan, Umit S.
Ozkan, Umit S.
中科院分区:
化学1区
文献类型:
--
作者:
Soykal, I. Ilgaz;Sohn, Hyuntae;Ozkan, Umit S.

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Co catalysts supported on ceria supports with two different particle sizes, one in the micro- and the other in the nano range, were investigated for their ethanol and ethylene steam reforming performance. Pre- and post reaction characterization techniques, including high resolution transmission electron microscopy, temperature programmed oxidation, dispersion, pore size measurements, in situ X-ray diffraction (XRD) and X-ray absorption fine structure spectroscopy (XAFS) studies were performed to examine the reducibility of the catalysts. Steady-state-activity testing has shown nanoparticles to have a higher reforming activity for ethanol, but also high ethylene yields. In spite of the high ethylene yields, catalysts supported on nanoparticles proved to be highly resistant to coking while the catalysts supported on larger ceria particles suffered from coke formation. Reforming experiments performed with ethylene showed significant differences in activity and stability. Bare supports were also tested for activity and the nanoparticle support was seen to have high dehydration activity. Operando DRIFTS experiments performed during ESR showed differences in surface species. Pulse experiments performed to use methanol oxidation as a probe reaction suggested differences in the relative abundance of redox sites and basic sites. The bare ceria supports also exhibited significant activity for ethanol dehydration, but not for C C cleavage. The superior performance of the catalysts supported on nanoparticles is thought to be due to a combination of factors, including increased reducibility, improved metal dispersion, and a difference in relative abundance of redox sites on the surface. All of these properties and, in turn, the catalytic performance, appear to be affected by the particle size of the support