Gasification of biomass: comparison of fixed bed and fluidized bed gasifier

被引:235
作者
Warnecke, R [1 ]
机构
[1] Noell KRC Energie & Umwelttech, Dept Proc Dev, D-97080 Wurzburg, Germany
关键词
biomass; combustion; fixed bed; fluidized bed; Noell; pyrolysis; reactolysis; reactors; thermolysis;
D O I
10.1016/S0961-9534(00)00009-X
中图分类号
S2 [农业工程];
学科分类号
0828 ;
摘要
Gasification as a thermochemical process is defined and limited to combustion and pyrolysis. A systematic overview of reactor designs categorizes fixed bed and fluidized bed reactors. Criteria for a comparison of these reactors are worked out, i.e. technology, use of material, use of energy, environment and economy. A utility analysis for thermochemical processes is suggested. It shows that the advantages of one of the reactor types are marginal. An advantage mainly depends on the physical consistency of the input. As a result there is no significant advantage for the fixed bed or the fluidized bed reactor. (C) 2000 Elsevier Science Ltd. All rights reserved.
引用
收藏
页码:489 / 497
页数:9
相关论文
共 1 条
[1]  
WARNECKE R, 1996, ABFALLWIRTSCHAFTSJOU, V3, P14