Non-supported bimetallic catalysts of Fe and Co for methane decomposition into H2 and a mixture of graphene nanosheets and carbon nanotubes

被引:26
作者
Al-Fatesh, Ahmed S. [1 ]
Abdelkader, Adel [2 ]
Osman, Ahmed I. [2 ,3 ]
Lanre, Mahmud S. [1 ]
Fakeeha, Anis H. [1 ]
Alhoshan, Mansour [1 ]
Alanazi, Yousef M. [1 ]
Awadallah, Ahmed E. [4 ]
Rooney, David W. [3 ]
机构
[1] King Saud Univ, Coll Engn, Dept Chem Engn, POB 800, Riyadh 11421, Saudi Arabia
[2] South Valley Univ, Fac Sci Qena, Chem Dept, Nanocomposite Catalysts Lab, Qena 83523, Egypt
[3] Queen Univ Belfast, Sch Chem & Chem Engn, David Keir Bldg, Belfast BT9 5AG, Antrim, North Ireland
[4] Egyptian Petr Res Inst EPRI, Cairo 11787, Egypt
关键词
methane decomposition; Methane decomposition; Hydrogen production; Graphene; Carbon nanotubes; Mixed metal oxides; FREE HYDROGEN; RAMAN-SPECTROSCOPY; GRAPHITE; GAS;
D O I
10.1016/j.ijhydene.2022.10.223
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
Herein, non-supported pure and mixed cobalt and iron oxide catalysts were synthesized from nitrate precursors using a simple, environmentally friendly preparation method in which water was the sole solvent. The prepared catalysts were then used to decompose methane into hydrogen and carbon (graphene nanosheets and carbon nanotubes). The fresh and spent catalysts were characterized by employing X-ray diffraction (XRD), Raman spectroscopy, scanning electron microscopy-energy dispersive X-ray analysis (SEM/EDX), transmission electron microscopy (TEM) and N2 adsorption-desorption techniques. In addition, the spent catalysts were subjected to thermo-gravimetric analysis (TGA) in order to measure the quantity of carbon deposits on the spent catalysts. The results indicated that the carbon deposited over these catalysts is a mixture of graphene nanosheets and carbon nanotubes (CNT). The results indicated that the mixed oxide catalysts exhibit higher catalytic activity than the pure oxides and that Fe: Co atomic ratio represents the key factor in the catalytic activity of these mixed oxides. After 420 min under the reaction feed, the 50Fe + 50Co catalyst shows the highest catalytic activity towards methane con-version of about 52.6% compared to 41.6% and 31.8% for 75Fe + 25Co and 25Fe + 75Co catalysts, respectively. & COPY; 2022 The Author(s). Published by Elsevier Ltd on behalf of Hydrogen Energy Publications LLC. This is an open access article under the CC BY license (http://creativecommons.org/ licenses/by/4.0/).
引用
收藏
页码:26506 / 26517
页数:12
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