Catalytic steam gasification of pig compost for hydrogen-rich gas production in a fixed bed reactor

被引:28
|
作者
Wang, Jingbo [1 ]
Xiao, Bo [1 ]
Liu, Shiming [1 ]
Hu, Zhiquan [1 ]
He, Piwen [1 ]
Guo, Dabin [1 ]
Hu, Mian [1 ]
Qi, Fangjie [1 ]
Luo, Siyi [2 ]
机构
[1] Huazhong Univ Sci & Technol, Sch Environm Sci & Engn, Wuhan 430074, Peoples R China
[2] Qingdao Technol Univ, Sch Environm & Municipal Engn, Qingdao 266033, Peoples R China
基金
中国国家自然科学基金;
关键词
Pig compost; Hydrogen production; Gasification; Catalyst; MUNICIPAL SOLID-WASTE; FLUIDIZED-BED; BIOMASS GASIFICATION; TAR; PERFORMANCE; OPPORTUNITIES; NAPHTHALENE; PYROLYSIS; MIXTURES; GASIFIER;
D O I
10.1016/j.biortech.2013.01.092
中图分类号
S2 [农业工程];
学科分类号
0828 ;
摘要
The catalytic steam gasification of pig compost (PC) for hydrogen-rich gas production was experimentally investigated in a fixed bed reactor using the developed NiO on modified dolomite (NiO/MD) catalyst. A series of experiments have been performed to explore the effects of catalyst, catalytic temperature, steam to PC ratio and PC particle size on the gas quality and yield. The results indicate that the NiO/MD catalyst could significantly eliminate the tar in the gas production and increase the hydrogen yield, and the catalyst lives a long lifetime in the PC steam gasification. Moreover, the higher catalytic temperature and smaller PC particle size can contribute to more hydrogen production and gas yield. Meanwhile, the optimal ratio of steam to PC (S/P) is found to be 1.24. (C) 2013 Elsevier Ltd. All rights reserved.
引用
收藏
页码:127 / 133
页数:7
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