Renewable hydrogen from glycerol steam reforming using Co-Ni-MgO based SBA-15 nanocatalysts

被引:37
作者
Al-Salihi, S. [2 ]
Abrokwah, R. [1 ,4 ]
Dade, W. [1 ]
Deshmane, V [1 ,2 ]
Hossain, T. [1 ,2 ]
Kuila, D. [1 ,3 ,4 ]
机构
[1] North Carolina A&T State Univ, Dept Chem, Greensboro, NC 27411 USA
[2] North Carolina A&T State Univ, Dept Chem Engn, Greensboro, NC 27411 USA
[3] North Carolina A&T State Univ, Joint Sch Nanosci & Nanoengn, Dept Nanoengn, Greensboro, NC 27411 USA
[4] North Carolina A&T State Univ, Energy & Environm Syst, Greensboro, NC 27411 USA
基金
美国国家科学基金会;
关键词
One-pot hydrothermal synthesis; Impregnation; Glycerol steam reforming; Mesoporous silica; Co-Ni bimetallic Catalysts; MgO modified-SBA-15 catalysts; SURFACE-AREA; FUEL-CELLS; CATALYSTS; NICKEL; ETHANOL; CU; STRATEGIES; OXIDES; PERFORMANCE; ADSORPTION;
D O I
10.1016/j.ijhydene.2020.03.149
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
Steam reforming of glycerol was carried out using Si-based mesoporous SBA-15 catalysts. Different mesoporous catalysts- Co-SBA-15, Ni-SBA-15, Co-MgO-SBA-15, Ni-MgO-SBA-15, and Co-Ni-SBA-15 were prepared using a one-pot hydrothermal method. An incipient wetness impregnation method was used only for the bimetallic Co-Ni-SBA-15 catalyst (catalyst designated as Co-Ni-SBA-15-IMPG) to compare its activity to that prepared by the one-pot method. The catalysts were characterized using XRD, TPR, TEM, TGA-DSC, ICP-OES and N-2 adsorption-desorption analytical techniques. A high surface area in the range of 540 -750 m(2)/g was observed depending on the catalyst composition. The glycerol steam reforming (GSR) activity of the catalysts was studied in the reaction temperature range of 450 degrees C-700 degrees C for hydrogen production. Results from the GSR studies for continuous 40 h showed that both Co-Ni-SBA-15-IMPG (impregnation) and Co-Ni-SBA-15 (one-pot) were resistant to deactivation, and both yielded 100% glycerol conversion for the entire 40 h. 10% Co-5%Ni-SBA-15 and 10%Co-5%Ni-SBA-15-IMPG produced (70-78) % and (60-78) % H-2 selectivity, respectively. Addition of MgO to Co-SBA-15 and Ni-SBA-15 increased the activity and stability of the catalysts. The catalyst stability performance followed the trend 10%Co-5%Ni > 10%Co-5%MgO >10%Co-5%Ni-IMPG. > 15%Co > 10%Ni-5%MgO >15%NiSBA-15. Thermal analyses of the spent catalyst showed a substantial amount of coke deposition which could be the major factor responsible for catalysts deactivation. Bimetallic catalysts prepared by one-pot method (10%Co-5%Ni-SBA-15) and incipient wetness impregnation (10%Co-5%Ni-SBA-15-IMPG) exhibited remarkable GSR activity compared to their monometallic counterparts. The GSR activity was observed in the order: 10%Co-5% Ni-IMPG > 10%Co-5%Ni > 10%Co-5%MgO >15%Co > 15%Ni > 10%Ni-5%MgO. (C) 2020 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:14183 / 14198
页数:16
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