Air gasification of rice husk in a dual distributor type fluidized bed gasifier

被引:126
|
作者
Mansaray, KG
Ghaly, AE
Al-Taweel, AM
Hamdullahpur, F
Ugursal, VI
机构
[1] Dalhousie Univ, Biol Engn Dept, Halifax, NS B3J 2X4, Canada
[2] Dalhousie Univ, Dept Chem Engn, Halifax, NS B3J 2X4, Canada
[3] Dalhousie Univ, Dept Mech Engn, Halifax, NS B3J 2X4, Canada
来源
BIOMASS & BIOENERGY | 1999年 / 17卷 / 04期
关键词
rice husk; gasification; fluidized bed; equivalence ratio; fluidization velocity; gas composition; higher heating value; gas yield; carbon conversion;
D O I
10.1016/S0961-9534(99)00046-X
中图分类号
S2 [农业工程];
学科分类号
0828 ;
摘要
In this study, a dual distributor type fluidized bed gasifier was used for the air gasification of rice husk in view of producing fuel gas. The effects of varying fluidization velocity (0.22, 0.28 and 0.33 m s(-1)) and equivalence ratio (0.25, 0.30 and 0.35) on the gasifier performance were discussed. The steady state temperature varied between 665 and 830 degrees C. The fluidization velocity of 0.22 m s(-1) and equivalence ratio of 0.25 appeared to be the optimum conditions with respect to the quality of gas. The mole fractions of the combustible components reached their maximum values at these conditions with a typical gas composition of 4% H-2, 5% hydrocarbons (CH4, C2H2, C2H4 and C2H6), 15% CO2, 20% CO and 57% N-2. The higher heating value of the gas obtained at these fluidization velocity and equivalence ratio (3.09-5.03 MJ Nm(-3)) compared very well with published data from air-blown biomass gasifiers of similar scale of operation. The gas yield and carbon conversion were in the range of 1.30 to 1.98 Nm(3) kg(-1) and 55.0 to 81.0%, respectively. (C) 1999 Elsevier Science Ltd. All rights reserved.
引用
收藏
页码:315 / 332
页数:18
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