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Experimental verification of the scaling relationships for bubbling gas-fluidised beds using the PEPT technique

机译:使用PEPT技术对鼓泡气化床结垢关系进行实验验证

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摘要

An experimental verification of the scaling relationships for bubbling gas-fluidised beds has been carried out by measuring particle cycle frequency. The Positron Emission Particle Tracking technique was used, which enabled non-intrusive measurements of solids motion in three dimensions with a spatial resolution of similar to2 mm under the conditions of this work. Three cylindrical beds (70, 141 and 240 mm ID) equipped with multiple orifice-type distributors were tested. It was shown that for geometrically similar beds, the pair of Froude numbers based on the minimum fluidisation and excess gas velocities was sufficient for similarity at the viscous limit. The experimental results showed little influence of the gas-to-particle density ratio, but a small effect of particle-to-bed diameter ratio when the change in the ratio was significant. The experimental results also indicated a possible relaxation of the viscous limit up to a particle Reynolds number of about 100. More experimental studies are needed to confirm the validity of such a relaxation. (C) 2002 Elsevier Science Ltd. All rights reserved. [References: 26]
机译:通过测量颗粒循环频率对鼓泡的气化床的比例关系进行了实验验证。使用了正电子发射粒子跟踪技术,在这项工作的条件下,该技术可对三维空间中的固体运动进行非侵入式测量,其空间分辨率约为2 mm。测试了三个配有多个孔型分配器的圆柱床(内径70、141和240毫米)。结果表明,对于几何相似的床,基于最小流化和过量气体速度的一对Froude数足以满足粘性极限条件下的相似要求。实验结果表明,气体-颗粒密度比的影响很小,但是当比例变化很大时,颗粒-床直径比的影响很小。实验结果还表明,粘滞极限可能会松弛,直至达到约100的雷诺数。需要更多的实验研究来确认这种松弛的有效性。 (C)2002 Elsevier ScienceLtd。保留所有权利。 [参考:26]

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