Mathematical modeling of a fluidized bed straw gasifier: Part I - Model development

被引:24
|
作者
Ergudenler, A
Ghaly, AE
Hamdullahpur, F
Al-Taweel, AM
机构
[1] Tech Univ Nova Scotia, Dept Agr Engn, Halifax, NS B3J 2X4, Canada
[2] Tech Univ Nova Scotia, Dept Mech Engn, Halifax, NS B3J 2X4, Canada
[3] Tech Univ Nova Scotia, Dept Chem Engn, Halifax, NS B3J 2X4, Canada
来源
ENERGY SOURCES | 1997年 / 19卷 / 10期
关键词
bed temperature; bubble characteristics; energy balance; fluidized bed; gas composition; gasifier; gas production rate; higher heating value; homogeneous equilibrium; material balance; mathematical model; straw;
D O I
10.1080/00908319708908908
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 ; 0820 ;
摘要
In this study, a model capable of predicting the steady state performance of a fluidized bed straw gasifier at a wide range of operating conditions was developed. The model was based on the homogeneous equilibrium theory, material and energy balances, and the two-phase theory of gas-solid fluidized beds. The three equilibrium reactions (water-gas shift, methanation and oxidation reactions) were used in the model. The model is kinetic fi ee and capable of predicting the reactor temperature and composition, higher heating value, and production rate of the produced gas.
引用
收藏
页码:1065 / 1084
页数:20
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