Low-temperature catalytic conversion of greenhouse gases (CO2 and CH4) to syngas over ceria-magnesia mixed oxide supported nickel catalysts

被引:33
作者
Al-Swai, Basem M. [1 ]
Osman, Noridah Binti [1 ,2 ]
Ramli, Anita [2 ,3 ]
Abdullah, Bawadi [1 ,4 ]
Farooqi, Ahmad Salam [1 ,4 ]
Ayodele, Bamidele Victor [5 ]
Patrick, David Onoja [1 ,2 ]
机构
[1] Univ Teknol PETRONAS, Dept Chem Engn, Seri Iskandar 32610, Perak, Malaysia
[2] Univ Teknol PETRONAS, Inst Self Sustainable Bldg, Dept Chem Engn, Ctr Biofuel & Biochem Res, Seri Iskandar 32610, Perak, Malaysia
[3] Univ Teknol PETRONAS, Dept Fundamental & Appl Sci, Seri Iskandar 32610, Perak, Malaysia
[4] Univ Teknol PETRONAS, Inst Contaminant Management Oil & Gas, Ctr Contaminant Control & Utilizat CenCoU, Seri Iskandar 32610, Perak, Malaysia
[5] Univ Malaysia Pahang, Fac Chem & Nat Resources Engn, Lebuhraya Tun Razak, Gambang Kuantan 26300, Malaysia
关键词
Dry reforming of methane; Low-temperature catalytic reaction; Syngas; CeO2-MgO; Ni loading coke formation; HYDROTALCITE-DERIVED CATALYSTS; HYDROGEN-PRODUCTION; NI/MGO CATALYST; COKE FORMATION; METHANE; NI; CEO2; PERFORMANCE; CARBON; LA;
D O I
10.1016/j.ijhydene.2020.04.233
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
Running dry reforming of methane (DRM) reaction at low-temperature is highly regarded to increase thermal efficiency. However, the process requires a robust catalyst that has a strong ability to activate both CH4 and CO2 as well as strong resistance against deactivation at the reaction conditions. Thus, this paper examines the prospect of DRM reaction at low temperature (400-600 degrees C) over CeO2-MgO supported Nickel (Ni/CeO2-MgO) catalysts. The catalysts were synthesized and characterized by XRD, N-2 adsorption/desorption, FE-SEM, H-2-TPR, and TPD-CO2 methods. The results revealed that Ni/CeO2-MgO catalysts possess suitable BET specific surface, pore volume, reducibility and basic sites, typical of heterogeneous catalysts required for DRM reaction. Remarkably, the activity of the catalysts at lower temperature reaction indicates the workability of the catalysts to activate both CH4 and CO2 at 400 degrees C. Increasing Ni loading and reaction temperature has gradually increased CH4 conversion. 20 wt% Ni/CeO2-MgO catalyst, CH4 conversion reached 17% at 400 degrees C while at 900 degrees C it was 97.6% with considerable stability during the time on stream. Whereas, CO2 conversions were 18.4% and 98.9% at 400 degrees C and 900 degrees C, respectively. Additionally, a higher CO2 conversion was obtained over the catalysts with 15 wt% Ni content when the temperature was higher than 600 degrees C. This is because of the balance between a high number of Ni active sites and high basicity. The characterization of the used catalyst by TGA, FE-SEM and Raman Spectroscopy confirmed the presence of amorphous carbon at lower temperature reaction and carbon nanotubes at higher temperature. (C) 2020 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:24768 / 24780
页数:13
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