Biomass gasification with pure steam in fluidised bed: 12 variables that affect the effectiveness of the biomass gasifier

被引:69
作者
Corella, Jose [1 ]
Toledo, Jose-Manuel [1 ]
Molina, Gregorio [1 ]
机构
[1] Univ Complutense Madrid, Dept Chem Engn, E-28040 Madrid, Spain
关键词
biomass; gasifier; hydrogen production; renewable energies; biomass gasification; steam gasification; hydrogen; fluidized bed;
D O I
10.1504/IJOGCT.2008.016739
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 [动力工程及工程热物理]; 0820 [石油与天然气工程];
摘要
Biomass gasification in fluidised bed with pure steam has already generated a 60 vol.%, dry basis, H-2 rich gas that was increased to 70-80 vol.% H-2 by using a CO2 sorbent in the gasifier bed. A tar content as low as 0.25 g/Nm(3) has also been reported when an active catalyst is used in the gasifier bed. Biomass gasification in fluidised bed with pure steam, therefore, has some potential interest for the production of a very rich in H-2 clean gas. This work shows in detail 12 operational variables that have already demonstrated a clear influence on the product distribution from the gasifier. Among all the products originating from the gasifier, this study concentrates on the hydrogen and tar contents in the raw gasification gas.
引用
收藏
页码:194 / 207
页数:14
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