Gasification of different biomasses in a dual-bed gasifier system combined with novel catalysts with high energy efficiency

被引:97
作者
Asadullah, M
Miyazawa, T
Ito, SI
Kunimori, K
Yamada, M
Tomishige, K [1 ]
机构
[1] Univ Tsukuba, Inst Mat Sci, Tsukuba, Ibaraki 3058573, Japan
[2] Rajshahi Univ, Dept Appl Chem & Chem Technol, Rajshahi 6205, Bangladesh
[3] Tohoku Univ, Grad Sch Engn, Dept Appl Chem, Aoba Ku, Sendai, Miyagi 9808579, Japan
基金
日本学术振兴会;
关键词
agricultural wastage; biomass; catalytic gasification; synthesis gas; fluidized bed;
D O I
10.1016/j.apcata.2004.02.028
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
Syngas has been produced from the gasification of various biomasses such as jute stick, bagasse, rice straw, and saw dust of cedar wood using a dual-bed gasifier combined with a novel catalyst. The gasification conditions were 150 mg/min of biomass feeding, ER = 0.25, catalyst (3 g) at temperature range of 823-923 K. The carbon conversion to gas and yield of useful gases such as CO, H-2, and CH4 were dependent on the properties of biomass. In terms of the formation rate of useful gases, the biomass quality was in the order of cedar wood > jute stick > bagasse > rice straw. Although the rice straw gasification is comparatively difficult in a single-bed gasifier due to its high ash content (22.6%), it becomes possible in a dual-bed reactor system. The dual-bed gasifier using Rh/CeO2/SiO2 catalyst that has been developed gave higher conversion to gas and higher yield of CO + H-2 + CH4 than did the single-bed gasifier. In the case of cedar wood gasification, although a small amount of coke was formed on the catalyst surface, the tar was not formed at all even at 823 K. However, in the case of other biomass, especially for rice straw, a significant amount of coke on the catalyst surface and tar was formed even at the high temperature (923 K). (C) 2004 Elsevier B.V. All rights reserved.
引用
收藏
页码:95 / 102
页数:8
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