2014
DOI: 10.1039/c4ra00355a
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Bimetallic Pt–Ni composites on ceria-doped alumina supports as catalysts in the aqueous-phase reforming of glycerol

Abstract: Adding Ni to a supported Pt catalyst for aqueous phase reforming allowed the Pt content to be reduced to one third, with a slight increase in H2 yield.

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Cited by 40 publications
(25 citation statements)
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“…Moreover, combination of Pt and Ni supported on alumina doped with ceria-doped (CeO 2 eAl 2 O 3 ) allowed the reduction of Pt content from 3 to 1 wt-%, and resulted in a slight increase of the hydrogen production. In addition, no substantial catalyst deactivation was observed [53].…”
Section: Hydrogen Formationmentioning
confidence: 98%
“…Moreover, combination of Pt and Ni supported on alumina doped with ceria-doped (CeO 2 eAl 2 O 3 ) allowed the reduction of Pt content from 3 to 1 wt-%, and resulted in a slight increase of the hydrogen production. In addition, no substantial catalyst deactivation was observed [53].…”
Section: Hydrogen Formationmentioning
confidence: 98%
“…This interpretation is consistent with the fact that other studies have shown coking in steam reforming of hydrocarbons reaction over Pt or Ni-based catalysts. 11,22,24,25 These modes denitely prove that disordered carbonaceous deposits always form on catalyst surface from C-C bond breakage of glycerol and their byproducts. In addition, the defects modes at around 610 cm À1 of Ce-based oxides 14,15 could not be detected due to its low intensity.…”
Section: Catalytic Performances Of the Solids In Steam Reforming Of Gmentioning
confidence: 92%
“…In order to full this, detailed studies of glycerol steam reforming using different catalysts in a xed-bed reactor have been conducted. [8][9][10][11][12][13][14][15][16] In general, one of the reasons of choice between Pt-and Ni-based catalysts is the resistance to phase transformation and tolerance against sulfur compounds, rather than their catalytic activity. Moreover, upon using steam-to-glycerol ratio in the range of 9-12 and reaction temperature at around 600-700 C, the steam reforming of glycerol is likely.…”
Section: Introductionmentioning
confidence: 99%
“…Also, Cu increased Ni reducibility. However, the neither of these studies tested the catalysts for extended (>12 h) use, which is unfortunate because deactivation is a known problem with Ni-based catalysts for APR [15,35,40], and Cu addition has extended the lifetime of Nibased catalysts for other reactions [56]. Therefore, in this study, a number of bimetallic xCue12Ni/MWNT catalysts have been prepared and compared as the APR catalysts to monometallic 12Ni/MWNT catalyst.…”
Section: Introductionmentioning
confidence: 97%
“…Ni is an attractive substitute because it is highly active for reactions involving CeC bond breaking, such as alkane hydrogenolysis [36]; however, Ni is also a good catalyst for CO methanation [29,30,37]. Moreover, it is prone to inactivation by carbon deposition [38], which has been observed on supported Ni catalysts during APR [35,39]. Further, Ni can be oxidized under APR conditions [40].…”
Section: Introductionmentioning
confidence: 99%