Hydrogen from alcohols: IR and flow reactor studies

被引:40
作者
Busca, Guido [1 ]
Montanari, Tania [1 ]
Resini, Carlo [1 ]
Ramis, Gianguido [1 ]
Costantino, Umberto [2 ]
机构
[1] Univ Genoa, Dipartimento Ingn Chim & Proc, Genoa, Italy
[2] Univ Perugia, CEMIN, Ctr Eccellenza Mat Innovat Nanostrutturati, Dipartimento Chim, I-06100 Perugia, Italy
关键词
Hydrogen productions; Renewable sources; Steam reforming; Ethanol steam reforming; Methanol steam reforming; Alcohol steam reforming; CATALYSTS; METHANOL; PRECURSOR; ETHANOL; SURFACE;
D O I
10.1016/j.cattod.2008.09.010
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
The reactions of methanol and ethanol steam reforming (MSR and ESR) have been studied over Cu-ZnOAl(2)O(3) and over Ni-containing catalysts, respectively. Our spectroscopic studies, coupled with flow reactor studies, allowed us to propose mechanisms for both reactions where water takes the role of oxidant of part of the copper and nickel species. The uncompletely reduced catalysts convert the alcohols into formate and acetate species, respectively. plus gas phase hydrogen. Over Cu-ZnO-Al(2)O(3) formates decompose into adsorbed CO which is rapidly oxidized into CO(2) before leaving the surface. This allows CO production lower than forecast from the WGS equilibrium. Over Ni-based catalysts acetates decompose into CO and methane. In fact, the ESR reaction was found to produce, above 700 K, hydrogen, carbon oxides and methane. The formation of hydrogen is limited by the establishing of the WGS (which would likely unavoidably limit the one-step production of hydrogen by ESR) and the methane SR equilibria. Activation of the C2 carbon atom of ethanol or of some of its decomposition products would be needed to avoid methane formation, thus increasing hydrogen yield. Preliminary work on isopropanol SR was performed over a Pd-Cu catalyst. Cracking and production of methane lower significantly the selectivity to Cox and hydrogen.(C) 2008 Elsevier B.V. All rights reserved.
引用
收藏
页码:2 / 8
页数:7
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