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首页> 外文期刊>Chemical Engineering Research & Design: Transactions of the Institution of Chemical Engineers >INVESTIGATION OF FLOODING,RE-ENTRAINMENT AND GRADE EFFICIENCY IN AXIAL FLOW CYCLONES
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INVESTIGATION OF FLOODING,RE-ENTRAINMENT AND GRADE EFFICIENCY IN AXIAL FLOW CYCLONES

机译:轴流旋流器的溢流,再入流和分级效率研究

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Slotted wall axial flow cyclones with a conventional center-body swirler are found to exhibit significant flooding at low air velocities.This was observed to be due to significant liquid hold-up on the vanes which eliminated the swirl and led to a pulsating frothing behaviour.At higher velocities,the liquid dispersed and separated through the wall slots.The onset of entrainment of liquid was determined visually.In the low velocity frothing region liquid was entrained directly but coalesced and fell back down the vortex finder.At higher gas velocities entrainment occurred due to several mechanisms.Design changes were introduced to improve performance.The center body was replaced by a new design of vane swirler around the periphery of the tube inlet.This significantly increased the swirl in the tube.Adapting four of the vanes to operate as liquid drainage channels eliminated the flooding phenomenon observed at low gas velocity and enabled the tube slot area to be reduced.This,combined with a larger diameter vortex finder,significantly increased the fraction of flow through the vortex finder,with no extra overall pressure drop.Liquid entrainment in the new design was reduced by positioning liquid slots at the top of the tube and by the use of a skirt.Grade efficiency was determined for the improved cyclone design operating over a range of gas flowrates.The cut size for outflow to the vortex finder was found to vary from about 7 mu m at an air velocity of 4.5 ms~(-1)to about 4.5 mu m at 11 ms~(-1).
机译:带有常规中心体旋流器的开槽壁轴流旋风分离器在低风速时会表现出明显的溢流现象,这是由于叶片上大量的液体滞留消除了旋流并导致了脉动的起泡行为。在较高的速度下,液体通过壁槽分散和分离。目视确定液体的夹带开始。在低速起泡区域中,液体被直接夹带但聚结并从涡流发现器中掉落。在较高的气体夹带下发生由于几种机制,引入了设计更改以提高性能。中心体被围绕进风口周围的叶片旋流器的新设计所取代,这显着增加了管道中的涡流。使四个叶片适应于液体排泄通道消除了在低气体速度下观察到的水淹现象,并减小了管槽面积。更大直径的涡流探测器,显着增加了流经涡流探测器的流量,而没有额外的总体压降。通过将液体槽口放置在管子顶部并使用裙缘,减少了新设计中的液体夹带确定了改进的旋风分离器设计的等级效率,该设计在一定的气体流量范围内运行。发现流向旋涡分离器的切割尺寸在4.5 ms〜(-1)的风速下从7微米变化到大约4.5微米(11毫秒〜(-1))。

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