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Hydrogen-rich gas production by air-steam gasification of rice husk using supported nano-NiO/γ-Al2O3 catalyst
被引:74
作者:
Li, Jianfen
[1
]
Liu, Jianjun
[1
]
Liao, Shiyan
[1
]
Yan, Rong
[1
,2
]
机构:
[1] Wuhan Polytech Univ, Sch Chem & Environm Engn, Wuhan 430023, Peoples R China
[2] Nanyang Technol Univ, Inst Environm Sci & Engn, Singapore 637723, Singapore
基金:
中国国家自然科学基金;
关键词:
Air-steam gasification;
Rice husk;
Catalyst;
Gas yield;
Hydrogen production;
PALM OIL WASTES;
BIOMASS GASIFICATION;
FLUIDIZED-BED;
TAR REMOVAL;
GASIFIER;
OPTIMIZATION;
COMBUSTION;
D O I:
10.1016/j.ijhydene.2010.04.108
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 air-steam catalytic gasification of rice husk for hydrogen-rich gas production was experimentally investigated in a combined fixed bed reactor with the newly developed nano-NiO/gamma-Al2O3 catalyst. A series of experiments have been performed to explore the effects of catalyst presence, catalytic reactor temperature, the equivalence ratio (ER), and steam to biomass ratio (S/B) on the composition and yield of gasification gases. The experiments demonstrated that the developed nano-NiO/gamma-Al2O3 catalyst had a high activity of cracking tar and hydrocarbons, upgrading the gas quality, as well as yielding a high hydrogen production. Catalytic temperature was crucial for the overall gasification process, a higher temperature contributed to more hydrogen production and gas yield. Varying ER demonstrated complex effects on rice husk gasification and an optimal value of 0.22 was found in the present study. Compared with biomass catalytic gasification under air only, the introduction of steam improved the gas quality and yield. The steam/biomass ratio of 1.33 was found as the optimum operating condition in the air steam catalytic gasification. (C) 2010 Professor T. Nejat Veziroglu. Published by Elsevier Ltd. All rights reserved.
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页码:7399 / 7404
页数:6
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