2011
DOI: 10.1016/j.cattod.2011.02.057
|View full text |Cite
|
Sign up to set email alerts
|

Rh–Ni/CeO2–Al2O3 catalysts for methane dry reforming

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
3
1
1

Citation Types

2
52
0
3

Year Published

2012
2012
2023
2023

Publication Types

Select...
8
1

Relationship

0
9

Authors

Journals

citations
Cited by 120 publications
(57 citation statements)
references
References 33 publications
2
52
0
3
Order By: Relevance
“…The addition of small amounts of noble metals, mainly Rh, to the catalyst formulation increased the Ni 2+ reducibility [3][4][5][6][7][8][9] and Ni 0 dispersion [10][11][12], retarded the sintering [9,13], avoided Ni 0 oxidation under steam or oxygen atmosphere [11,14,15], and decreased the activation energy for CH 4 dissociation in Rh/Ni alloys [16]. Consequently, enhanced activities were reported not only in conventional and commercial H 2 and syngas processes such as steam reforming [17,18], autothermal reforming [7,12,17,19,20] and oxyreforming [21][22][23][24], but also in more prone to carbon formation processes such as dry reforming [9,[25][26][27][28][29][30][31], ethanol reforming [32][33][34], biogas reforming [35] and, lastly, in fuel cell devices [17], in which large hydrocarbons were fed in systems operating under transient conditions [36,37]. Indeed, Rh promoted the gasification of adsorbed carbon by steam in the autothermal reforming of isooctane [38] and...…”
Section: Introductionmentioning
confidence: 89%
“…The addition of small amounts of noble metals, mainly Rh, to the catalyst formulation increased the Ni 2+ reducibility [3][4][5][6][7][8][9] and Ni 0 dispersion [10][11][12], retarded the sintering [9,13], avoided Ni 0 oxidation under steam or oxygen atmosphere [11,14,15], and decreased the activation energy for CH 4 dissociation in Rh/Ni alloys [16]. Consequently, enhanced activities were reported not only in conventional and commercial H 2 and syngas processes such as steam reforming [17,18], autothermal reforming [7,12,17,19,20] and oxyreforming [21][22][23][24], but also in more prone to carbon formation processes such as dry reforming [9,[25][26][27][28][29][30][31], ethanol reforming [32][33][34], biogas reforming [35] and, lastly, in fuel cell devices [17], in which large hydrocarbons were fed in systems operating under transient conditions [36,37]. Indeed, Rh promoted the gasification of adsorbed carbon by steam in the autothermal reforming of isooctane [38] and...…”
Section: Introductionmentioning
confidence: 89%
“…Another possibility is the reduction of Ni 2þ ions from non-stoichiometric NiAl x O y and stoichiometric NiAl 2 O 4 species. The third peak centred at 884 C could be attributed to ceria strongly interacting with alumina e.g., CeO 2 eAl 2 O 3 [24,25]. Also, the reduction of the latter species provides Ce 3þ surface, which form solid solutions as CeAlO 3 .…”
Section: Fresh Catalyst Characterizationsmentioning
confidence: 94%
“…This result highlights the key role of the active component in promoting support reduction. Rh-containing samples displayed the lowest temperature for consumption peaks, due to the improved catalyst reducibility upon Rh addition [42]. Conversely, the support doping by alkali addition (especially in the case of potassium) was accompanied by a leftward shift peaks, which attested that catalyst basification may increase the metals-support interactions and retard oxide reduction [43].…”
Section: Textural/structural Properties and H 2 -Tpr Measurementsmentioning
confidence: 99%