Hydrogen production from ethanol using a plasma reactor with an alumite catalyst electrode

被引:11
作者
Iwasaki, Y
Liu, JQ
Zhang, J
Kitajima, T
Sakurai, M
Kameyama, H
机构
[1] Nissan Motor Co Ltd, Nissan Res Ctr, Techol Res Lab 3, Yokosuka, Kanagawa 2378523, Japan
[2] Tokyo Univ Agr & Technol, Dept Chem Engn, Koganei, Tokyo 1848588, Japan
关键词
plasma; synergistic effect; hydrogen; ethanol; alumite catalyst;
D O I
10.1252/jcej.39.216
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
With the aim of developing a non-equilibrium reactor for proton exchange membrane fuel cell (PEMFC) systems and other applications, hydrogen was produced from ethanol using a non-equilibrium plasma reactor combined with a catalyst, which consisted of an alumite catalyst electrode, at atmospheric pressure in a temperature range of 160-300 degrees C under an AC or a pulsed discharge condition. It was found that non-equilibrium plasma and a catalyst had a synergistic effect on the ethanol conversion rate under an AC discharge. For example, the ethanol conversion rate obtained with the plasma reactor with the alumite catalyst (Cu-Ni/gamma-Al2O3) electrode under an AC discharge condition of 3 kV of effective voltage at 2 kHz was 2.4 times as large as the arithmetic sum of the ethanol conversion rate obtained with the plasma reactor with a non-catalytic alumite electrode under the same discharge conditions and the ethanol conversion rate obtained with the alumite catalyst (Cu-Ni/gamma-Al2O3) electrode without any discharge, at 210 degrees C. It was also observed that non-equilibrium plasma and a catalyst had a synergistic effect on the ethanol conversion rate under a pulsed discharge. For example, the ethanol conversion rate obtained with the plasma reactor with the alumite catalyst (Cu-Ni/gamma-Al2O3) electrode under a pulsed discharge of 7.2 kV of peak-to-peak voltage at a pulse number of 5000 s(-1) was 1.9 times as large as the arithmetic sum of the ethanol conversion rate obtained with the plasma reactor with the non-catalytic alumite electrode under the same discharge conditions and the ethanol conversion rate obtained with the alumite catalyst (Cu-Ni/gamma-Al2O3) electrode without any discharge, at 180 degrees C. The energy efficiency, which was defined as mols of hydrogen produced per unit electric power consumption, obtained with the alumite catalyst (Cu-Ni/gamma-Al2O3) electrode at 270 degrees C under conditions of an AC discharge of 3 kV of effective voltage at 2 kHz was 2.9 times higher than that obtained with the noncatalytic alumite electrode at 270 degrees C under the same discharge conditions. The energy efficiency obtained with the alumite catalyst (Cu-Ni/gamma-Al2O3) electrode at 270 degrees C under conditions of a pulsed discharge, pulse number of 5000 s(-1) and peak-to-peak voltage of 7.2 kV was 2.6 times higher than that obtained with the non-catalytic alumite electrode at 270 degrees C under the same discharge conditions. And the energy efficiency obtained with the alumite catalyst (Cu-Ni/gamma-Al2O3) electrode at 270 degrees C under conditions of a pulsed discharge, pulse number of 5000 s(-1) and peak-to-peak voltage of 7.2 kV was 2.7 times higher than that obtained under conditions of an AC discharge, frequency of 2 kHz and effective voltage of 3 kV. The energy efficiency and the conversion rate increased greatly because of the collaborative activity of the catalyst and non-equilibrium plasma. These results indicate the potential for developing a non-equilibrium reactor using an alumite catalyst electrode.
引用
收藏
页码:216 / 228
页数:13
相关论文
共 16 条
[1]   Application of nonthermal plasma to chemical reactions [J].
Futamura, S ;
Kabashima, H ;
Einaga, H .
JOURNAL OF THE JAPAN PETROLEUM INSTITUTE, 2002, 45 (06) :329-341
[2]  
IWASAKI Y, 2004, P 15 WORLD HYDR EN C
[3]  
KAMEYAMA H, 1990, Patent No. 144154
[4]  
KAMEYAMA H, 1997, Patent No. 234361
[5]  
KATO S, 2003, THERMAL SCI ENG, V11, P1
[6]   Employing plasma as catalyst in hydrogen production [J].
Mutaf-Yardimci, O ;
Saveliev, AV ;
Fridman, AA ;
Kennedy, LA .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 1998, 23 (12) :1109-1111
[7]  
NOZAKI T, 2003, KOATSU GAS, V40, P10
[8]  
NOZAKI T, 2002, NIHON KIKAI GAKKAI B, V68, P2593
[9]  
SAKURAI M, 2001, P 34 AUT M SOC CHEM, P727
[10]   Energy performance analysis of heat transport system using methanol decomposition and synthesis [J].
Shiizaki, S ;
Kameyama, H ;
Nagashima, I .
JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 2001, 34 (11) :1449-1454