Production of hydrogen and carbon nanotubes from methane decomposition in a two-stage fluidized bed reactor

被引:77
|
作者
Qian, WZ [1 ]
Liu, T
Wang, ZW
Wei, F
Li, ZF
Luo, GH
Li, YD
机构
[1] Tsinghua Univ, Dept Chem Engn, Beijing 100084, Peoples R China
[2] Tianjin Univ, Dept Chem Engn, Tianjin 300072, Peoples R China
基金
中国国家自然科学基金;
关键词
carbon nanotubes; catalyst deactivation; multi-stage fluidized bed reactor; nickel catalyst; methane decomposition;
D O I
10.1016/j.apcata.2003.10.018
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
Methane decomposition over a Ni/Cu/Al2O3 catalyst is studied in a two-stage fluidized bed reactor. Low temperature is adopted in the lower stage and high temperature in the upper stage. This allows the fluidized catalysts to decompose methane with high activity in the high temperature condition: then the carbon produced will diffuse effectively to form carbon nanotubes (CNTs) in both low and high temperature regions. Thus the catalytic cycle of carbon production and carbon diffusion in micro scale can be tailored by a macroscopic method, which permits the catalyst to have high activity and high thermal stability even at 1123 K for hydrogen production for long times. Such controlled temperature condition also provides an increased thermal driving force for the nucleation of CNTs and hence favors the graphitization of CNTs, characterized by high resolution transmission electron microscopy (HRTEM), Raman spectroscopy and XRD. Multistage operation with different temperatures in a fluidized bed reactor is an effective way to meet the both requirements of hydrogen production and preparation of CNTs with relatively perfect microstructures. (C) 2003 Elsevier B.V. All rights reserved.
引用
收藏
页码:223 / 228
页数:6
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