Syngas production from dry reforming of methane over ni/perlite catalysts: Effect of zirconia and ceria impregnation

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

2021 ◽  
Vol 362 ◽  
pp. 72-80 ◽  
Author(s):  
Ignacio de Dios García ◽  
Andrzej Stankiewicz ◽  
Hakan Nigar

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.


Author(s):  
Ahmad Salam Farooqi ◽  
Basem M. Al-Swai ◽  
Farida Hamimi Binti Ruslan ◽  
Noor Asmawati Mohd Zabidi ◽  
R. Saidur ◽  
...  

Author(s):  
Saeid Abbasi ◽  
Mohsen Abbasi ◽  
Firouz Tabkhi ◽  
Benyamin Akhlaghi

Applicability of using Dry Reforming of Methane (DRM) using low-cost Ni-based catalysts instead of Conventional Steam Reformers (CSR) to producing syngas simultaneously with reducing the emission of carbon dioxide was studied. In order to achieving this goal, a multi-tubular recuperative thermally coupled reactor which consists of two-concentric-tubes has been designed (Thermally Coupled Tri- and Dry Reformer [TCTDR]). By employing parameters of an industrial scale CSR, two proposed configuration (DRM with fired-furnace and Tri-Reforming of Methane (TRM) instead of fired-furnace (TCTDR)) was simulated. A mathematical heterogeneous model was used to simulate proposed reactors and analyses were carried out based on methane conversion, hydrogen yield and molar flow rate of syngas for each reactor. The results displayed methane conversion of DRM with fired-furnace was 35.29% and 31.44% for Ni–K/CeO2–Al2O3 and Ni/La2O3 catalysts, respectively, in comparison to 26.5% in CSR. Methane conversion in TCTDR reached to 16.98% by Ni/La2O3 catalyst and 88.05% by NiO–Mg/Ce–ZrO2/Al2O3 catalyst in TRM side. Also, it was 15.88% using Ni–K/CeO2–Al2O3 catalyst in the DRM side and 88.36% using NiO–Mg/Ce–ZrO2/Al2O3 catalyst in TRM side of TCTDR. Finally, the effect of different amounts of supplying energy on the performance of DRM with fired-furnace was studied, and positive results in reducing the energy consumption were observed.


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