Hydrogen production from catalytic steam reforming of benzene as tar model compound of biomass gasification
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- 作者：Ningbo Gaoa ; b ; 1 ; nbogao@xjtu.edu.cn" class="auth_mail" title="E-mail the corresponding author ; Xiao Wangb ; 1 ; Aimin Lib ; Chunfei Wuc ; Zhifan Yinb
- 关键词：Hydrogen production ; Catalyst ; Steam reforming ; Benzene ; Tar
- 刊名：Fuel Processing Technology
- 出版年：2016
- 出版时间：July 2016
- 年：2016
- 卷：148
- 期：Complete
- 页码：380-387
- 全文大小：1436 K
文摘
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A NiO/ceramic foam catalyst was developed for catalytic steam reforming of tar.
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From 700 to 900 °C, the yield of H2 increased from 140.67 to 182.06 g kg− 1.
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The catalytic activity of the catalyst can be regained after regeneration process.
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A kinetic model study shows that the apparent activation energy is 73.38 kJ/mol.