首页> 外文会议>International conference on fuidization: New horizons in fluidization engineering; 20070513-18; Agassiz(CA) >TRANSIENT CHARACTERIZATION OF TYPE B PARTICLES IN A CIRCULATING FLUIDIZED BED RISER
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TRANSIENT CHARACTERIZATION OF TYPE B PARTICLES IN A CIRCULATING FLUIDIZED BED RISER

机译:循环流化床立管中B型颗粒的瞬态表征

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Simple and rapid dynamic tests were used to evaluate fluid dynamic behavior of granular materials in the transport regime. Particles with densities ranging from 189 to 2,500 kg/m~3 and Sauter mean size from 61 to 812 Dm were tested in a 0.305 m diameter, 15.5 m height circulating fluidized bed (CFB) riser. The riser emptying time was linearly related to the Froude number in each of three operating regimes. The flow structure along the height of the riser followed a distinct pattern as tracked through differential pressures. These results are discussed to better understand the transformations that take place when operating over various regimes. The effects of pressure, particle size, and density on test performance are also presented.
机译:简单和快速的动态测试用于评估颗粒状物料在运输状态下的流体动力学行为。在直径为0.305 m,高度为15.5 m的循环流化床(CFB)提升管中测试了密度为189至2,500 kg / m〜3且Sauter平均尺寸为61至812 Dm的颗粒。在三种操作方式的每一种中,冒口的排空时间与弗洛伊德数线性相关。沿立管高度的流动结构遵循通过压差跟踪的独特模式。对这些结果进行了讨论,以更好地理解在各种体制下运行时发生的转换。还介绍了压力,粒度和密度对测试性能的影响。

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