首页> 外文期刊>Advanced Powder Technology: The internation Journal of the Society of Powder Technology, Japan >Improvement of dry float-sink separation of smaller sized spheres by reducing the fluidized bed height
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Improvement of dry float-sink separation of smaller sized spheres by reducing the fluidized bed height

机译:通过降低流化床高度,改善较小尺寸球体的干式浮沉分离

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In this study, the influence of the fluidized bed height on the float-sink of different sized spheres in a gas-solid fluidized bed was investigated. Fluidized beds with heights h = 200,150,100 and 50 mm were prepared using a cylindrical column of inner diameter = 290 mm and a mixture of zircon sand and iron powder as the fluidized medium. Float-sink experiments were carried out using density adjusted spheres of diameter D_(sp) = 40, 30, 20 and 10 mm. It was found that the float-sink performance at D_(sp)≥ 20 mm is not affected by the height of the bed, and the sharpness of separation (the density range where spheres neither float nor sink completely) is less than or equal to 200 kg/m~3. In the case of D_(sp) =10 mm, the sharpness of separation is a larger value (1100 kg/m~3 at h = 200 mm), whereas it decreases with decreasing h and is 400 kg/m~3 at h = 50 mm. The fluctuation of the surface height of the fluidized bed was visually recorded. The fluctuation is reduced by reducing h. The fluctuation vs. h correlates with the sharpness of separation at D_(sp) =10 mm vs. h. These results indicate that the dry float-sink separation of smaller sized spheres is improved as the fluctuation of fluidized bed surface is decreased by reducing the fluidized bed height.
机译:在这项研究中,研究了流化床高度对气固流化床中不同尺寸球体的浮沉的影响。使用内径= 290 mm的圆柱柱和锆石砂和铁粉的混合物作为流化介质,制备高度为h = 200,150,100和50 mm的流化床。使用直径D_(sp)= 40、30、20和10 mm的密度调整球体进行浮沉实验。发现D_(sp)≥20 mm时的浮沉性能不受床高的影响,分离的锐度(球体既不漂浮也不沉的密度范围)小于或等于200公斤/米〜3。在D_(sp)= 10 mm的情况下,分离的锐度是一个较大的值(在h = 200 mm时为1100 kg / m〜3),而随着h的减小而减小,在h时为400 kg / m〜3 = 50毫米。目视记录流化床表面高度的波动。通过减小h减小波动。相对于h的波动与D_(sp)= 10 mm相对于h的分离锐度相关。这些结果表明,通过减小流化床高度来减小流化床表面的波动,可以改善较小尺寸球体的干式浮沉分离效果。

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