首页> 外文会议>Proceedings of the 11th International Conference on Fluidized Bed Technology >FLOW CHARACTERISTICS ACCORDING TO THE MASS RATIO OF TERNARY SOLIDS IN THE GAS-SOLID CFB RISER
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FLOW CHARACTERISTICS ACCORDING TO THE MASS RATIO OF TERNARY SOLIDS IN THE GAS-SOLID CFB RISER

机译:气固式CFB冒口中三元固体质量比的流量特征

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The effect of fine particle mass ratio on flow characteristics of ternary mixture of particles with different densities and wide (flat) size distribution were studied in 0.1m diameter riser of a circulating fluidized bed.As the gas superficial velocity gradually increases, the bed undergoes the fixed-bed, partial fluidized-bed and fully fluidized-bed region.Then, Uif, Ucf and Umf for all mixtures are determined.This study focuses on mixing and segregation behavior in complete fluidized bed region (above Ucf).At low gas velocity, bed behaves like bubbling bed and at high gas velocity bed similar to fast fluidized bed.
机译:在循环流化床直径0.1m的立管中研究了细颗粒质量比对不同密度和宽(平坦)尺寸分布的颗粒三元混合物流动特性的影响。随着气体表观速度逐渐增加,该床经历了固定床,部分流化床和完全流化床区域,然后确定所有混合物的Uif,Ucf和Umf,本研究着重于在低气速下完全流化床区域(Ucf以上)的混合和分离行为,床的行为就像鼓泡床,而在高气速床中的行为类似于快速流化床。

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