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首页> 外文期刊>Advanced Powder Technology: The internation Journal of the Society of Powder Technology, Japan >Influence of air bubble size on float-sink of spheres in a gas-solid fluidized bed
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Influence of air bubble size on float-sink of spheres in a gas-solid fluidized bed

机译:气泡大小对气固流化床中球体浮沉的影响

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摘要

The float-sink of density adjusted spheres of different diameter (10-40 mm) in a gas-solid fluidized bed was investigated at various bed heights (50-200 mm). The maximum density of floating spheres (pnoat) and the minimum density of sinking spheres (ρ_(sink)) were determined by the float-sink experiments. The fluidized bed density (ρ_(fb) was measured using the height and cross section of the fluidized bed and total weight of the fluidized media. The diameter of air bubbles at the bed surface was measured at each bed height, and was normalized by the sphere diameter. It was found that the value of ρ_(fb)-ρ_(float) approaches zero as the normalized bubble diameter decreases from 4 to 0.5 regardless of the sphere diameter. The value of ρ_(sink)-ρ_(fb) for sphere diameter = 10 mm approaches zero as the normalized bubble diameter decreases from 4 to 1.5, whereas the value for sphere diameter = 20-40 mm rises from zero as the normalized bubble diameter decreases from 1.5 to 0.5. The float and sink of spheres basically tend to follow the fluidized bed density with decreasing the normalized bubble diameter. However, relatively larger spheres do not sink based on the density difference as the normalized bubble diameter decreases, which may be due to that the fluidized bed viscosity becomes larger as the normalized bed diameter decreases.
机译:在不同的床层高度(50-200mm)下研究了气固流化床中不同直径(10-40mm)的密度调节球的浮沉。通过浮沉实验确定了浮球的最大密度(pnoat)和下沉球的最小密度(ρ_(sink))。使用流化床的高度和横截面以及流化介质的总重量测量流化床密度(ρ_(fb),在每个床高测量床表面气泡的直径,并通过研究发现,随着归一化气泡直径从4减小到0.5,无论球形直径如何,ρ_(fb)-ρ_(fb)的值都接近零。当标准化气泡直径从4减小到1.5时,球直径= 10 mm接近零,而当标准化气泡直径从1.5减小到0.5时,球直径= 20-40 mm的值从零增加。会随着标准化气泡直径的减小而遵循流化床密度,但是,随着标准化气泡直径的减小,相对较大的球体不会根据密度差而下沉,这可能是由于流化床粘度变大了归一化床直径减小。

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