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循环流化床锅炉内颗粒速度分布的实验研究
引用本文:姬广勤,陈新华,金有海,王建军. 循环流化床锅炉内颗粒速度分布的实验研究[J]. 中国粉体技术, 2009, 15(3): 5-8
作者姓名:姬广勤  陈新华  金有海  王建军
作者单位:中国石油大学(华东)机电工程学院,山东,东营,257061
摘    要:为了研究操作参数对循环流化床锅炉内颗粒速度分布的影响,在冷态模型装置上使用PV6A型颗粒速度光纤测量仪、毕托管对循环流化床锅炉炉膛内的颗粒速度进行了测量与分析。结果表明:在流化风速为2.57 m/s、循环质量流率为0.58 kg/(m2.s)、一次风量为2 300 m3/h、二次风量为1 500 m3/h时,循环流化床锅炉炉膛内颗粒浓度分布、压降、流化状态、质量循环都达到一个较稳定的水平,呈现典型的环核分布特征。

关 键 词:循环流化床锅炉  颗粒速度  质量流率

Experimental Study of Particles Velocity Distribution in Circulating Fluidized Bed Boiler
Ji Guangqin,Chen Xinhua,Jin Youhai,Wang Jianjun. Experimental Study of Particles Velocity Distribution in Circulating Fluidized Bed Boiler[J]. China Powder Science and Technology, 2009, 15(3): 5-8
Authors:Ji Guangqin  Chen Xinhua  Jin Youhai  Wang Jianjun
Abstract:In order to study the effect of operation parameter on the particles velocity distribution in the circulating fluidized bed boiler,the particle velocity in circulating fluidized bed furnace was measured and analyzed using PV6A particle velocity measuring instrument and pitot tube.The re-sults showed that the distribution of particle velocity,pressure drop,fluid state and circulating presented a more stable level when the flow speed was 2.57 m/s,the quality of circulation flow rate was 0.58 kg/(m2.s),the first air flow was 2 300 m3/h and the second air flow was 1 500 m3/h.The circulating fluidized bed displayed a bubble area in the bottom,rapid flow area,eddy flow in upper part and a typical core-annulus distribution in the downward flow zone of sidewall.
Keywords:circulating fluidized bed boiler  particle velocity  mass rate
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