Ce0.70La0.20Ni0.10O2-δ catalyst for methane dry reforming: Influence of reduction temperature on the catalytic activity and stability

2017 ◽  
Vol 218 ◽  
pp. 779-792 ◽  
Author(s):  
Lidia Pino ◽  
Cristina Italiano ◽  
Antonio Vita ◽  
Massimo Laganà ◽  
Vincenzo Recupero
Keyword(s):  
Catalytic Activity ◽  
Dry Reforming ◽  
Reduction Temperature ◽  
Methane Dry Reforming

scholarly journals Nickel-Containing Ceria-Zirconia Doped with Ti and Nb. Effect of Support Composition and Preparation Method on Catalytic Activity in Methane Dry Reforming

Nanomaterials ◽  
2020 ◽  
Vol 10 (7) ◽  
pp. 1281
Author(s):  
Mikhail Simonov ◽  
Yulia Bespalko ◽  
Ekaterina Smal ◽  
Konstantin Valeev ◽  
Valeria Fedorova ◽  
...  
Keyword(s):  
Catalytic Activity ◽  
Structural Changes ◽  
Preparation Method ◽  
Diffuse Reflectance Spectroscopy ◽  
Fluorite Structure ◽  
Lattice Parameter ◽  
Dry Reforming ◽  
Fluorite Phase ◽  
Methane Dry Reforming ◽  
Supercritical Synthesis

Nickel-containing mixed ceria-zirconia oxides also doped by Nb and Ti have been prepared by a citrate route and by original solvothermal continuous flow synthesis in supercritical alcohols. Nickel was subsequently deposited by conventional insipient wetness impregnation. The oxides are comprised of ceria-zirconia solid solution with cubic fluorite phase. Negligible amounts of impurities of zirconia are observed for samples prepared by citrate route and doped by Ti. Supports prepared by supercritical synthesis are single-phased. XRD data, Raman, and UV-Vis DR (diffuse reflectance) spectroscopy suggest increasing lattice parameter and amount of oxygen vacancies in fluorite structure after Nb and Ti incorporation despite of the preparation method. These structural changes correlate with the catalytic activity in a methane dry reforming reaction. Catalysts synthesized under supercritical conditions are more active than the catalysts of the same composition prepared by the citrate route. The catalytic activity of samples doped with Ti and Nb is two times higher in terms of TOF (turnover frequency) and increased stability of these catalysts is attributed with the highest oxygen mobility being crucial for gasification of coke precursors.

scholarly journals Production of CO-rich Hydrogen Gas from Methane Dry Reforming over Co/CeO2 Catalyst

2016 ◽  
Vol 11 (2) ◽  
pp. 210 ◽  
Author(s):  
Bamidele V. Ayodele ◽  
Maksudur R. Khan ◽  
Chin Kui Cheng
Keyword(s):  
Catalytic Activity ◽  
Fixed Bed ◽  
Dry Reforming ◽  
Hydrogen Gas ◽  
Fixed Bed Reactor ◽  
Feed Ratio ◽  
X Ray Diffraction ◽  
Methane Dry Reforming ◽  
X Ray ◽  
Adsorption Desorption

<p>Production of CO-rich hydrogen gas from methane dry reforming was investigated over CeO<sub>2</sub>-supported Co catalyst. The catalyst was synthesized by wet impregnation and subsequently characterized by field emission scanning electron microscope (FESEM), energy dispersion X-ray spectroscopy (EDX), liquid N<sub>2</sub> adsorption-desorption, X-ray diffraction (XRD), Fourier transform infrared spectroscopy (FTIR) and thermogravimetric analysis (TGA) for the structure, surface and thermal properties. The catalytic activity test of the Co/CeO<sub>2</sub> was investigated between 923-1023 K under reaction conditions in a stainless steel fixed bed reactor. The composition of the products (CO<sub>2</sub> and H<sub>2</sub>) from the methane dry reforming reaction was measured by gas chromatography (GC) coupled with thermal conductivity detector (TCD). The effects of feed ratios and reaction temperatures were investigated on the catalytic activity toward product selectivity, yield, and syngas ratio. Significantly, the selectivity and yield of both H<sub>2</sub> and CO increases with feed ratio and temperature. However, the catalyst shows higher activity towards CO selectivity. The highest H<sub>2</sub> and CO selectivity of 19.56% and 20.95% respectively were obtained at 1023 K while the highest yield of 41.98% and 38.05% were recorded for H<sub>2</sub> and CO under the same condition. Copyright © 2016 BCREC GROUP. All rights reserved</p><p><em>Received: 21<sup>st</sup> January 2016; Revised: 23<sup>rd</sup> February 2016; Accepted: 23<sup>rd</sup> February 2016</em></p><p><strong>How to Cite:</strong> Ayodele, B.V., Khan, M.R., Cheng, C. K. (2016). Production of CO-rich Hydrogen Gas from Methane Dry Reforming over Co/CeO<sub>2</sub> Catalyst. <em>Bulletin of Chemical Reaction Engineering &amp; Catalysi</em>s, 11 (2): 210-219 (doi:10.9767/bcrec.11.2.552.210-219)</p><p><strong>Permalink/DOI:</strong> http://dx.doi.org/10.9767/bcrec.11.2.552.210-219</p>

An Overview of Reforming Technologies and the Effect of Parameters on the Catalytic Performance of Mesoporous Silica/Alumina Supported Nickel Catalysts for Syngas Production by Methane Dry Reforming

2020 ◽  
Vol 13 (4) ◽  
pp. 303-322
Author(s):  
M.A. Saad ◽  
N.H. Abdurahman ◽  
Rosli Mohd Yunus ◽  
Mohammed Kamil ◽  
Omar I. Awad
Keyword(s):  
Catalytic Activity ◽  
Mesoporous Silica ◽  
Nickel Catalysts ◽  
Catalytic Performance ◽  
Dry Reforming ◽  
Future Research ◽  
Methane Dry Reforming ◽  
Syngas Production ◽  
Silica Alumina ◽  
Supported Nickel Catalysts

Synthetic gas - a combination of (H2) and (CO) - is an important chemical intermediate for the production of liquid hydrocarbon, olefin, gasoline, and other valuable chemicals. Several reforming methods that use steam, carbon dioxide, and oxygen in the presence of various catalytic systems have been extensively investigated, and this paper reviews the recent research on the state-of-the-art of reforming technologies and the effect of parameters on the catalytic activity of mesoporous silica/alumina supported nickel catalysts for syngas production by methane dry reforming. First, we provide an overview of reforming technologies, including methane dry reforming, steam methane reforming, partial oxidation of CH4, and auto thermal reforming of CH4. Then, we review the literature on dry reforming catalysts. Next, we describe recent findings on the effect of parameters on the catalytic activity of mesoporous silica/alumina supported nickel catalysts for syngas production. Finally, we make proposals for future research. This study can help achieve a better understanding of the reforming technologies and the effects of parameters on catalytic performance for syngas production, thus contributing to the development of green technologies.

Methane dry reforming over hydrotalcite-derived Ni–Mg–Al mixed oxides: the influence of Ni content on catalytic activity, selectivity and stability

2016 ◽  
Vol 6 (17) ◽  
pp. 6705-6715 ◽  
Author(s):  
Radosław Dębek ◽  
Monika Motak ◽  
Dorota Duraczyska ◽  
Franck Launay ◽  
Maria Elena Galvez ◽  
...  
Keyword(s):  
Catalytic Activity ◽  
Mixed Oxides ◽  
Dry Reforming ◽  
Methane Dry Reforming ◽  
Ni Content

Ni-containing hydrotalcite-derived catalysts were prepared using different Ni loadings (from ca. 4 to 60 wt%) at the same MII/MIII ratio equal to 3.

Nickel based catalysts for methane dry reforming: Effect of supports on catalytic activity and stability

2019 ◽  
Vol 44 (52) ◽  
pp. 28065-28076 ◽  
Author(s):  
Cristina Pizzolitto ◽  
Eva Pupulin ◽  
Federica Menegazzo ◽  
Elena Ghedini ◽  
Alessandro Di Michele ◽  
...  
Keyword(s):  
Catalytic Activity ◽  
Dry Reforming ◽  
Methane Dry Reforming

Bi- and trimetallic Ni catalysts over Al2O3 and Al2O3-MO (M = Ce or Mg) oxides for methane dry reforming: Au and Pt additive effects

2014 ◽  
Vol 156-157 ◽  
pp. 350-361 ◽  
Author(s):  
Hongjing Wu ◽  
Giuseppe Pantaleo ◽  
Valeria La Parola ◽  
Anna M. Venezia ◽  
Xavier Collard ◽  
...  
Keyword(s):  
Dry Reforming ◽  
Additive Effects ◽  
Ni Catalysts ◽  
Methane Dry Reforming

scholarly journals Influence of the Reduction Temperature and the Nature of the Support on the Performance of Zirconia and Alumina-Supported Pt Catalysts for n-Dodecane Hydroisomerization

Catalysts ◽  
2021 ◽  
Vol 11 (1) ◽  
pp. 88
Author(s):  
Diana García-Pérez ◽  
Maria Consuelo Alvarez-Galvan ◽  
Jose M. Campos-Martin ◽  
Jose L. G. Fierro
Keyword(s):  
Catalytic Activity ◽  
Surface Area ◽  
Catalytic Properties ◽  
Catalytic Performance ◽  
Major Influence ◽  
Pt Catalysts ◽  
Reduction Temperature ◽  
Metal Dispersion ◽  
Tungsten Oxides ◽  
Supported Pt Catalysts

Catalysts based on zirconia- and alumina-supported tungsten oxides (15 wt % W) with a small loading of platinum (0.3 wt % Pt) were selected to study the influence of the reduction temperature and the nature of the support on the hydroisomerization of n-dodecane. The reduction temperature has a major influence on metal dispersion, which impacts the catalytic activity. In addition, alumina and zirconia supports show different catalytic properties (mainly acid site strength and surface area), which play an important role in the conversion. The NH3-TPD profiles indicate that the acidity in alumina-based catalysts is clearly higher than that in their zirconia counterparts; this acidity can be attributed to a stronger interaction of the WOx species with alumina. The PtW/Al catalyst was found to exhibit the best catalytic performance for the hydroisomerization of n-dodecane based on its higher acidity, which was ascribed to its larger surface area relative to that of its zirconia counterparts. The selectivity for different hydrocarbons (C7–10, C11 and i-C12) was very similar for all the catalysts studied, with branched C12 hydrocarbons being the main products obtained (~80%). The temperature of 350 °C was clearly the best reduction temperature for all the catalysts studied in a trickled-bed-mode reactor.

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