Decomposition of methane to hydrogen using nanosecond pulsed plasma reactor with different active volumes, voltages and frequencies

被引:87
作者
Khalifeh, Omid [1 ]
Mosallanejad, Amin [1 ]
Taghvaei, Hamed [1 ]
Rahimpour, Mohammad Reza [1 ,2 ]
Shariati, Alireza [1 ]
机构
[1] Shiraz Univ, Sch Chem & Petr Engn, Dept Chem Engn, Shiraz 71345, Iran
[2] Univ Calif Davis, Dept Chem Engn & Mat Sci, Davis, CA 95616 USA
关键词
Non-thermal plasma; Nanosecond pulsed plasma; Hydrogen production; Methane decomposition; Active volume; BARRIER DISCHARGE REACTOR; CO2-CONTAINING NATURAL-GAS; GLIDING ARC SYSTEM; NONTHERMAL PLASMA; HIGHER HYDROCARBONS; PARTIAL OXIDATION; CARBON-DIOXIDE; DIRECT CONVERSION; LOW-TEMPERATURE; CATALYTIC REACTOR;
D O I
10.1016/j.apenergy.2016.02.017
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
In this paper, the methane conversion into hydrogen is investigated experimentally in a nanosecond pulsed DBD reactor. In order to achieve pure hydrogen production with minimum power consumption, effects of some operating parameters including external electrode length, applied voltage and pulse repetition frequency have been evaluated. Results show that although higher CH4 conversion and H-2 concentration can be obtained at longer electrode lengths, higher applied voltages and pulse repetition frequencies, these parameters should be optimized for efficient hydrogen production. Actually, the maximum CH4 conversion of 87.2% and maximum hydrogen percentage of 80% are obtained at the external electrode length, discharge power, voltage and frequency of 15 cm, 268.92 W, 12 kV and 10 kHz, respectively. However, the maximum efficiency of 7.23% is achieved at the external electrode length of 15 cm, applied voltage of 6 kV, pulse repetition frequency of 0.9 kHz and discharge power of 4 W. Furthermore, at this condition, due to low temperature of discharge zone very little amount of solid carbon was observed on the inner electrode surface of the reactor. (C) 2016 Published by Elsevier Ltd.
引用
收藏
页码:585 / 596
页数:12
相关论文
共 88 条
[21]  
Indarto A., 2005, J NAT GAS CHEM, V14, P13
[22]   Hydrogen production from methane in a dielectric barrier discharge using oxide zinc and chromium as catalyst [J].
Indarto, Antonius .
JOURNAL OF THE CHINESE INSTITUTE OF CHEMICAL ENGINEERS, 2008, 39 (01) :23-28
[23]   A brief catalyst study on direct methane conversion using a dielectric barrier discharge [J].
Indarto, Antonius ;
Choi, Jae-Wook ;
Lee, Hwaung ;
Song, Hyung Keun .
JOURNAL OF THE CHINESE CHEMICAL SOCIETY, 2007, 54 (04) :823-828
[24]  
Indarto A, 2006, ENERGY, V31, P2986, DOI 10.1016/j.energy.2005.10.034
[25]   Co-generation of synthesis gas and C2+ hydrocarbons from methane and carbon dioxide in a hybrid catalytic-plasma reactor:: A review [J].
Istadi ;
Amin, NAS .
FUEL, 2006, 85 (5-6) :577-592
[26]   Naphtha cracking through a pulsed DBD plasma reactor: Effect of applied voltage, pulse repetition frequency and electrode material [J].
Jahanmiri, A. ;
Rahimpour, M. R. ;
Shirazi, M. Mohamadzadeh ;
Hooshmand, N. ;
Taghvaei, H. .
CHEMICAL ENGINEERING JOURNAL, 2012, 191 :416-425
[27]   Atmospheric pressure microwave plasma source for hydrogen production [J].
Jasinski, M. ;
Czylkowski, D. ;
Hrycak, B. ;
Dors, M. ;
Mizeraczyk, J. .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2013, 38 (26) :11473-11483
[28]   Effect of gas temperature on partial oxidation of methane in plasma reforming [J].
Jo, Sungkwon ;
Lee, Dae Hoon ;
Song, Young-Hoon .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2013, 38 (31) :13643-13648
[29]   Numerical study on influences of barrier arrangements on dielectric barrier discharge characteristics [J].
Kang, WS ;
Park, JM ;
Kim, Y ;
Hong, SH .
IEEE TRANSACTIONS ON PLASMA SCIENCE, 2003, 31 (04) :504-510
[30]   Plasma-Enhanced Methane Direct Conversion over Particle-Size Adjusted MOx/Al2O3 (M = Ti and Mg) Catalysts [J].
Kasinathan, Palraj ;
Park, Sunyoung ;
Choi, Woon Choon ;
Hwang, Young Kyu ;
Chang, Jong-San ;
Park, Yong-Ki .
PLASMA CHEMISTRY AND PLASMA PROCESSING, 2014, 34 (06) :1317-1330