scholarly journals Syngas production via microwave-assisted dry reforming of methane

2021 ◽  
Vol 362 ◽  
pp. 72-80 ◽  
Author(s):  
Ignacio de Dios García ◽  
Andrzej Stankiewicz ◽  
Hakan Nigar
2020 ◽  
Vol 18 (6) ◽  
pp. 1987-2019
Author(s):  
T. T. Phuong Pham ◽  
Kyoung S. Ro ◽  
Lyufei Chen ◽  
Devinder Mahajan ◽  
Tan Ji Siang ◽  
...  

2018 ◽  
Vol 43 (36) ◽  
pp. 17142-17155 ◽  
Author(s):  
Farah Mesrar ◽  
Mohamed Kacimi ◽  
Leonarda F. Liotta ◽  
F. Puleo ◽  
Mahfoud Ziyad

2017 ◽  
Vol 212 ◽  
pp. 159-174 ◽  
Author(s):  
Axel Löfberg ◽  
Jesús Guerrero-Caballero ◽  
Tanushree Kane ◽  
Annick Rubbens ◽  
Louise Jalowiecki-Duhamel

Cerâmica ◽  
2017 ◽  
Vol 63 (365) ◽  
pp. 77-81 ◽  
Author(s):  
L. C. B. de Araújo ◽  
D. M. de A. Melo ◽  
M. A. de F. Melo ◽  
J. M. de F. Barros ◽  
R. M. Braga ◽  
...  

Abstract Materials such as MgAl2O4 and ZnAl2O4 assessed in the reaction of dry reforming of methane to produce syngas were synthesized by microwave-assisted combustion method using urea as fuel. Samples of synthesized oxides were calcined at 800 °C for 2 h and impregnated with 5% nickel. The impregnated samples were calcined at 850 °C for 4 h to obtain the desired phases. The results of the catalytic tests showed that the catalysts are active for the reaction of dry reforming of methane, and the catalyst that showed the best performance for methane conversion was 5% Ni/MgAl2O4 calcined at 850 °C/4 h.


2021 ◽  
Vol 1016 ◽  
pp. 1585-1590
Author(s):  
Ye Wang ◽  
Yan Nan Wang ◽  
Patrick da Costa ◽  
Chang Wei Hu

In producing syngas, which offers environmental benefits, dry reforming of methane (DRM) could promote the installation of the future carbon tax. This reaction has been already extensively studied and nowadays, no stable catalysts are enough efficient to scale up the process to its industrialization. It has been suggested that basic sites can affect the performance of catalyst. It is known that magnesium promotes the performance of catalyst. In order to understand the effect of Mg for dry reforming of methane, NiO-MgO-ZrO2 catalysts were studied. The activity was carried out at 700 °C in a fixed-bed micro-reactor under CH4:CO2:Ar=1:1:8. It was shown that the introduction of Mg led to an unexpected decrease in the activity when compared to non-promoted catalyst. It was also shown that the surface area, pore-volume, pore diameter, and weak basicity decreased when the Mg was introduced into NiO-ZrO2 catalyst. All these properties can cause a decrease in the activity, selectivity, and stability of NiO-MgO-ZrO2 catalyst for DRM.


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