Production of hydrogen by methane catalytic decomposition over Ni-Cu-Fe/Al2O3 catalyst

被引:100
作者
Chesnokov, Vladimir V. [1 ]
Chichkan, Alexandra S. [1 ]
机构
[1] RAS, Boreskov Inst Catalysis SB, Novosibirsk, Russia
关键词
Hydrogen production; Methane decomposition; Natural gas; Ni-Cu-Fe/Al2O3; catalyst; FILAMENTOUS CARBON; ACTIVATED CARBONS; NANOFIBERS; CRACKING; NI/SIO2;
D O I
10.1016/j.ijhydene.2009.01.074
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
Catalysts with high nickel concentrations 75%Ni-12%Cu/Al2O3, 70%Ni-10%Cu-10%Fe/Al2O3 were prepared by mechanochemical activation and their catalytic properties were studied in methane decomposition. It was shown that modification of the 75%Ni-12%Cu/Al2O3 catalyst with iron made it possible to increase optimal operating temperatures to 700-750 degrees C while maintaining excellent catalyst stability. The formation of finely dispersed Ni-Cu-Fe alloy particles makes the catalysts stable and capable of operating at 700-750 degrees C in methane decomposition to hydrogen and carbon nanofibers. The yield of carbon nanofibers on the modified 70%Ni-10%Cu-10%Fe/Al2O3 catalyst at 700-750 degrees C was 150-160 g/g. The developed hydrogen production method is also efficient when natural gas is used as the feedstock. An installation with a rotating reactor was developed for production of hydrogen and carbon nanofibers from natural gas. It was shown that the 70%Ni-10%Cu-10%Fe/Al2O3 catalyst could operate in this installation for a prolonged period of time. The hydrogen concentration at the reactor outlet exceeded 70 mol%. (C) 2009 International Association for Hydrogen Energy. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:2979 / 2985
页数:7
相关论文
共 34 条
[11]  
CHESNOKOV VV, 1995, CATALYST METHOD ITS
[12]   Ni/SiO2 and Fe/SiO2 catalysts for production of hydrogen and filamentous carbon via methane decomposition [J].
Ermakova, MA ;
Ermakov, DY .
CATALYSIS TODAY, 2002, 77 (03) :225-235
[13]  
Ione K.G., 2003, CHEM SUSTAINABLE DEV, V11, P907
[14]   Hydrogen production by catalytic decomposition of methane over activated carbons: kinetic study [J].
Kim, MH ;
Lee, EK ;
Jun, JH ;
Kong, SJ ;
Han, GY ;
Lee, BK ;
Lee, TJ ;
Yoon, KJ .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2004, 29 (02) :187-193
[15]  
Kireev V., 1970, METHODS PRACTICAL CA
[16]  
Korovin N. V., 1984, ELECTROKNIMIYA, V20, P1258
[17]  
KUVSHINOV GG, 1996, P 11 WORLD HYDR EN C, P655
[18]   Catalytic decomposition of methane over carbon blacks for CO2-free hydrogen production [J].
Lee, EK ;
Lee, SY ;
Han, GY ;
Lee, BK ;
Lee, TJ ;
Jun, JH ;
Yoon, KJ .
CARBON, 2004, 42 (12-13) :2641-2648
[19]   Thermocatalytic hydrogen production from the methane in a fluidized bed with activated carbon catalyst [J].
Lee, KK ;
Han, GY ;
Yoon, KJ ;
Lee, BK .
CATALYSIS TODAY, 2004, 93-5 :81-86
[20]   Metal-support interaction effects on the growth of filamentous carbon over CO/SiO2 catalysts [J].
Li, XN ;
Zhang, Y ;
Smith, KJ .
APPLIED CATALYSIS A-GENERAL, 2004, 264 (01) :81-91