A novel synthesis of NiAl2O4 spinel from a Ni-Al mixed-metal alkoxide as a highly efficient catalyst for hydrogen production by glycerol steam reforming
[Display omitted] •Development of a novel method for the synthesis of NiAl2O4 spinel.•Synthesis of a highly active NiAl2O4 with high reducibility and porosity.•Achieving H2 yield of 76.38 % and glycerol conversion into gas products of 95.42 %.•Suppression of coke formation by the addition of CeO2 an...
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Veröffentlicht in: | Applied catalysis. B, Environmental Environmental, 2020-05, Vol.265, p.118535, Article 118535 |
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Sprache: | eng |
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•Development of a novel method for the synthesis of NiAl2O4 spinel.•Synthesis of a highly active NiAl2O4 with high reducibility and porosity.•Achieving H2 yield of 76.38 % and glycerol conversion into gas products of 95.42 %.•Suppression of coke formation by the addition of CeO2 and formation of CeAlO3.
A novel method was developed for the synthesis of a more easily reducible NiAl2O4 spinel, which was tested as catalyst for hydrogen production by glycerol steam reforming. A Ni-Al mixed-metal alkoxide was firstly prepared through solvothermal method and then calcined using a two-step calcination technique. XRD, N2 physisorption, H2-TPR, XPS, SEM, and TEM results show that this new catalyst is more readily reducible and possesses a more developed porous structure with higher surface area. It therefore exhibits high H2 yield (76.38 %) and glycerol conversion into gaseous products (95.42 %). To avoid or reduce coke formation, 10 wt.% CeO2 was incorporated into the catalyst structure. TGA, TEM, and Raman spectroscopy analyses reveal the suppression of coke by a large extent due to the formation of well-dispersed CeAlO3, which decreases significantly the filamentous carbon formation rate on nickel surface and promotes coke gasification by providing oxidative environment around nickel active sites. |
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ISSN: | 0926-3373 1873-3883 |
DOI: | 10.1016/j.apcatb.2019.118535 |