Supported-induced effect on the catalytic properties of Rh and Pt-Rh particles deposited on La 2 O 3 and mixed α-Al 2 O 3 -La 2 O 3 in the dry reforming of methane

2014 ◽  
Vol 485 ◽  
pp. 172-180 ◽  
Author(s):  
Madani Ghelamallah ◽  
Pascal Granger
2017 ◽  
Vol 12 (3-4) ◽  
pp. 174-184 ◽  
Author(s):  
T. F. Sheshko ◽  
Yu. M. Serov ◽  
T. A. Kryuchkova ◽  
I. A. Khayrullina ◽  
I. V. Chislova ◽  
...  

2012 ◽  
Vol 21 (5) ◽  
pp. 595-604 ◽  
Author(s):  
Rafik Benrabaa ◽  
Hamza Boukhlouf ◽  
Axel Löfberg ◽  
Annick Rubbens ◽  
Rose-Nöelle Vannier ◽  
...  

2009 ◽  
Vol 141 (3-4) ◽  
pp. 385-392 ◽  
Author(s):  
S. Barama ◽  
C. Dupeyrat-Batiot ◽  
M. Capron ◽  
E. Bordes-Richard ◽  
O. Bakhti-Mohammedi

2016 ◽  
Vol 164 ◽  
pp. 312-315 ◽  
Author(s):  
A. Lanzini ◽  
C. Guerra ◽  
P. Leone ◽  
M. Santarelli ◽  
F. Smeacetto ◽  
...  

2017 ◽  
Vol 147 (8) ◽  
pp. 2200-2208 ◽  
Author(s):  
Joanna Kamieniak ◽  
Elena Bernalte ◽  
Aidan M. Doyle ◽  
Peter J. Kelly ◽  
Craig E. Banks

Materials ◽  
2021 ◽  
Vol 14 (23) ◽  
pp. 7227
Author(s):  
Adrian Mizera ◽  
Andrzej Kowalczyk ◽  
Lucjan Chmielarz ◽  
Ewa Drożdż

Two series of strontium titanates doped with Ni, Co, or Cu with general formula of SrTi1-xMexO3 for Sr-stoichiometric and Sr0.95Ti1−xMexO3 for Sr-non-stoichiometric materials (where Me = Ni, Co or Cu and x were 0.02 and 0.06) were obtained by the wet chemical method. The samples were calcinated at 900, 950, and 1050 °C and characterized in terms of their structural properties (XRD), the possibility of undergoing the reduction and oxidation reactions (TPR/TPOx), and catalytic properties. All obtained materials were multiphase and although the XRD analysis does not confirm the presence of Ni, Co, and Cu oxides (with one exception for Cu-doped sample), the TPR/TPOx profiles show reduction peaks that can be attributed to the reduction of these oxides which may at first appear in an amorphous form. Catalytic tests in dry reforming of methane reaction showed that the highest catalytic activity was achieved for Ni-doped materials (up to 90% of CH4 conversion) while Co and Cu-doped samples showed only a very slight catalytic effect. Additionally, the decrease in methane conversion with an increasing calcination temperature was observed for Ni-doped strontium titanates.


2019 ◽  
Vol 324 ◽  
pp. 15-26 ◽  
Author(s):  
Won-Jun Jang ◽  
Jae-Oh Shim ◽  
Hak-Min Kim ◽  
Seong-Yeun Yoo ◽  
Hyun-Seog Roh

2013 ◽  
Vol 203 ◽  
pp. 188-195 ◽  
Author(s):  
R. Benrabaa ◽  
A. Löfberg ◽  
A. Rubbens ◽  
E. Bordes-Richard ◽  
R.N. Vannier ◽  
...  

RSC Advances ◽  
2020 ◽  
Vol 10 (55) ◽  
pp. 33059-33070
Author(s):  
Hugo A. Lara-García ◽  
Daniel G. Araiza ◽  
Melissa Méndez-Galván ◽  
Samuel Tehuacanero-Cuapa ◽  
Antonio Gómez-Cortés ◽  
...  

The Nd-doped CeO2 support enhances the reactivity of the catalysts, selectivity toward hydrogen and stability by improving coke deposition resistance.


2016 ◽  
Vol 879 ◽  
pp. 396-401
Author(s):  
Radosław Dębek ◽  
Monika Motak ◽  
Maria Elena Galvez ◽  
Teresa Grzybek ◽  
Patrick da Costa

Mg/Al hydrotalcite-like materials containing ceria were synthesized as catalysts precursors for the reaction of dry methane reforming. The nickel species were introduced into the catalytic systems via adsorption from aqueous solution of [Ni (EDTA)]2- complexes for 4 and 24h and the effect of adsorption time on the catalytic properties of obtained materials was evaluated. The mixed nanooxides were obtained by thermal decomposition of hydrotalcite-like materials at 550°C for 4h and the catalysts were subsequently characterized by XRD, elemental analysis, H2-TPR and low temperature N2 sorption techniques. The adsorption duration of [Ni (EDTA)]2- influenced the properties of the prepared materials, such as textural properties, nickel crystallite size, and thus their catalytic activity in the reaction of dry reforming of methane. The sample which underwent adsorption for 24h turned out to be the most active in DRM reaction. However, over this catalyst RWGS reaction was well developed, which caused the excess of CO in the products of the reaction and faster deactivation of the catalyst.


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