A model of coal particle drying in fluidized bed combustion reactor

被引:6
|
作者
Komatina, M.
Manovic, V.
Saljnikov, A.
机构
[1] Nat Resources Canada, CANMET, Energy Technol Ctr, Ottawa, ON K1A 1M1, Canada
[2] Univ Belgrade, Fac Mech Engn, Belgrade, Serbia
关键词
combustion; drying of coal; fluidized bed; single particle; temperature;
D O I
10.1080/00908310600688796
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
Experimental and theoretical investigation on drying of a single coal particle in fluidized bed combustor is presented. Coal particle drying was considered via the moist shrinking core mechanism. The results of the drying test runs of low-rank Serbian coals were used for experimental verification of the model. The temperature of the coal particle center was measured, assuming that drying was completed when the temperature equalled 100 degrees C. The influence of different parameters ( thermal conductivity and specific heat capacity of coal, fluidized bed temperature, moisture content and superheating of steam) on drying time and temperature profile within the coal particle was analyzed by a parametric analysis. The experimentally obtained results confirmed that the moist shrinking core mechanism can be applied for the mathematical description of a coal particle drying, while dependence between drying time and coal particle radius, a square law relationship, implicates heat transfer control of the process and confirms the validity of assumptions used in modeling.
引用
收藏
页码:239 / 250
页数:12
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