Microwave-assisted catalytic decomposition of methane over activated carbon for CO2-free hydrogen production

被引:143
作者
Dominguez, A. [1 ]
Fidalgo, B. [1 ]
Fernandez, Y. [1 ]
Pis, J. J. [1 ]
Menendez, J. A. [1 ]
机构
[1] CSIC, Inst Nacl Carbon, E-33080 Oviedo, Spain
关键词
methane; hydrogen; microwave; catalytic decomposition; carbon nanofibres;
D O I
10.1016/j.ijhydene.2007.07.041
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
The aim of this work was to combine microwave heating with the use of low-cost granular activated carbon as a catalyst for the production Of CO2-free hydrogen by methane decomposition in a fixed bed quartz-tube flow reactor. In order to compare the results achieved, conventional heating was also applied to the catalytic decomposition reaction of methane over the activated carbon. It was found that methane conversions were higher under microwave conditions than with conventional heating when the temperature measured was lower than or equal to 800 degrees C. However, when the temperature was increased, the difference between the conversions under microwave and conventional heating was reduced. The influence of volumetric hourly space velocity (VHSV) on the conversion tests using both microwave and conventional heating was also studied. In general, there is a substantial initial conversion, which declines sharply during the first stages of the reaction but tends to stabilise with time. An increase in the VHSV has a negative effect on CH4 conversion, and even more so in the case of microwave heating. Nevertheless, the conversions obtained in the microwave device at the beginning of the experiments are, in general, better than the conversions reported in other works which also use a carbonaceous-based catalyst. Additionally, the formation of carbon nanofibres in one of the microwave experiments is also reported. (c) 2007 International Association for Hydrogen Energy. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:4792 / 4799
页数:8
相关论文
共 32 条
[1]   Hydrogen production by methane decomposition over coal char [J].
Bai, Zongqing ;
Chen, Haokan ;
Li, Wen ;
Li, Baoqing .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2006, 31 (07) :899-905
[2]   Catalytic decomposition of methane over activated carbon [J].
Bai, ZQ ;
Chen, H ;
Li, BQ ;
Li, W .
JOURNAL OF ANALYTICAL AND APPLIED PYROLYSIS, 2005, 73 (02) :335-341
[3]   Hydrogen from methane in a single-step process [J].
Balasubramanian, B ;
Ortiz, AL ;
Kaytakoglu, S ;
Harrison, DP .
CHEMICAL ENGINEERING SCIENCE, 1999, 54 (15-16) :3543-3552
[4]   CATALYTIC PARTIAL OXIDATION OF NATURAL-GAS TO SYNGAS [J].
BHARADWAJ, SS ;
SCHMIDT, LD .
FUEL PROCESSING TECHNOLOGY, 1995, 42 (2-3) :109-127
[5]   CO2 reforming of CH4 [J].
Bradford, MCJ ;
Vannice, MA .
CATALYSIS REVIEWS-SCIENCE AND ENGINEERING, 1999, 41 (01) :1-42
[6]   Reforming catalysts for hydrogen generation in fuel cell applications [J].
Cheekatamarla, Praveen K. ;
Finnerty, C. M. .
JOURNAL OF POWER SOURCES, 2006, 160 (01) :490-499
[7]   Production of COx-free hydrogen and nanocarbon by direct decomposition of undiluted methane on Ni-Cu-alumina catalysts [J].
Chen, JL ;
Li, YD ;
Li, ZQ ;
Zhang, XX .
APPLIED CATALYSIS A-GENERAL, 2004, 269 (1-2) :179-186
[8]   Frequency effects in the catalytic oligomerization of methane via microwave heating [J].
Conde, LD ;
Marún, C ;
Suib, SL ;
Fathi, Z .
JOURNAL OF CATALYSIS, 2001, 204 (02) :324-332
[9]   Production of hydrogen from methane and methane/steam in a microwave irradiated char-loaded reactor [J].
Cooney, DO ;
Xi, ZP .
FUEL SCIENCE & TECHNOLOGY INTERNATIONAL, 1996, 14 (08) :1111-1141
[10]   Preparation and evaluation of porous nickel-alumina spheres as catalyst in the production of hydrogen from decomposition of methane [J].
de Almeida, Rusiene M. ;
Fajardo, Humberto V. ;
Mezalira, Daniela Z. ;
Nuernberg, Giselle B. ;
Noda, Lucia K. ;
Probst, Luiz F. D. ;
Carreno, Neftali L. V. .
JOURNAL OF MOLECULAR CATALYSIS A-CHEMICAL, 2006, 259 (1-2) :328-335