NONISOTHERMAL, 2-PHASE MODEL OF FLUIDIZED-BED REACTOR FOR COAL-GASIFICATION PROCESS

被引：0
|
作者：
CIESIELCZYK, E [1 ]
GAWDZIK, A [1 ]
机构：
[1] PEDAGOG UNIV OPOLE,INST ENGN,OPOLE,POLAND
来源：
INZYNIERIA CHEMICZNA I PROCESOWA | 1992年 / 13卷 / 03期
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D O I：
暂无
中图分类号：
TQ [化学工业];
学科分类号：
0817 ;
摘要：
Nonisothermal two-phase model of fluidized bed reactor for coal gasification is presented. Model assumptions are discussed and mass and energy balance equations, describing the model, are derived. Effect of the main technological and hydrodynamics parameters on process performance is analyzed. Numerical calculation results of isothermal and nonisothermal two-phase models are compared for evaluating usefulness of considering the temperature distribution in fluidized bed.
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页码：451 / 470
页数：20
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