Fluidization in tapered vessels

Toshiro Maruyama, Toshio Koyanagi
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引用次数: 17

Abstract

Methods for the prediction of bed height and pressure drop in tapered air-fluidized beds are proposed. A comparison was made with measurements in slugging fluidized beds in the slow bubble regime over a wide range of apex angle from 0° (rectangular) to 45°. The bed height and pressure drop are well predicted by each of the proposed methods using the same constant values of bubble rise velocity and fluctuation ratio as for the rectangular fluidized bed with the same distributor geometry.

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锥形容器中的流化
提出了锥形空气流化床床层高度和压降的预测方法。在0°(矩形)到45°的宽顶角范围内,与慢泡状态下段塞流化床的测量结果进行了比较。对于具有相同分布器几何形状的矩形流化床,采用相同的气泡上升速度和波动比常数值,每种方法都能很好地预测床层高度和压降。
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