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The turbulent characteristics of the gas-solid suspension in a square cyclone separator

机译:方形旋风分离器中气固悬浮液的湍流特性

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Three-dimensional particle dynamics analyzer was employed to Study the gas-solid flow in a square-shaped cyclone separator which was designed for large CFB application. Distribution of flow vector, fluctuating velocity, turbulent kinetic energy, turbulent intensity and particle concentration were discussed. The swirling flow inside the cyclone showed the Rankine vortex characteristics, i.e., strong swirling vortex at the central region of the cross-section and weak swirling quasi-free vortex near the wall. The quasi-laminar motion of particles enhanced the turbulent movement at the corners due to particle-particle/wall collision, which led to the local peak value of the turbulent kinetic energy and turbulent intensity. The corner is one of the major region to cause pressure drop because the suspension at the corners consumed more energy of the flow. The corners were found to be beneficial to particle separation mainly because the strong fluctuating flow consumed much of the kinetic energy of both the particle and the gas. (c) 2005 Published by Elsevier Ltd.
机译:使用三维粒子动力学分析仪研究了方形旋风分离器中的气固流,该旋风分离器是为大型CFB应用而设计的。讨论了流动矢量的分布,脉动速度,湍动能,湍流强度和颗粒浓度。旋风分离器内部的旋流表现出兰金旋涡特征,即在横截面的中心区域具有强旋涡,而在壁附近具有弱旋准准涡。颗粒的准层运动由于颗粒-颗粒/壁的碰撞而增强了拐角处的湍流运动,这导致了湍动能和湍流强度的局部峰值。拐角是引起压降的主要区域之一,因为拐角处的悬浮液消耗了更多的流动能量。发现拐角有利于颗粒分离,这主要是因为强烈的脉动流消耗了颗粒和气体的大部分动能。 (c)2005由爱思唯尔有限公司出版。

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