Effect of dilute and dense phase operating conditions on bed-to-wall heat transfer mechanism in a circulating fluidized bed combustor

被引:29
作者
Vijay, GN [1 ]
Reddy, BN [1 ]
机构
[1] Univ New Brunswick, Dept Mech Engn, Fredericton, NB E3B 5A3, Canada
基金
加拿大自然科学与工程研究理事会;
关键词
heat transfer mechanism; CFB combustor; particle convection; radiation; dilute phase; dense phase; suspension density; bed temperature;
D O I
10.1016/j.ijheatmasstransfer.2005.03.013
中图分类号
O414.1 [热力学];
学科分类号
摘要
In the present paper investigations are conducted on bed-to-wall heat transfer to water-wall surfaces in the upper region of the riser column of a circulating fluidized bed (CFB) combustor under dilute and dense phase conditions. The bed-to-wall heat transfer depends on the contributions of particle convection, gas convection and radiation heat transfer components. The percentage contribution of each of these components depends on the operating conditions i.e., dilute and dense phase bed conditions and bed temperature. The variation in contribution with operating conditions is estimated using the cluster renewal mechanistic model. The present results contribute some fundamental information on the contributions of particle convection, gas convection and radiation contributions in bed-to-wall heat transfer under dilute and dense phase conditions with bed temperature. This leads to better understanding of heat transfer mechanism to water-wall surfaces in the upper region of the riser column under varying load conditions i.e., when the combustor is operated under dilute and dense phase situations. The results will further contribute to understanding of heat transfer mechanism and will aid in the efficient design of heat transfer surfaces in the CFB unit. (c) 2005 Elsevier Ltd. All rights reserved.
引用
收藏
页码:3276 / 3283
页数:8
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