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Abstract
A three-dimensional particle dynamic analyzer (3D-PDA) was employed to measure the gas-solid two-phase flow in a lab-scale square cyclone
separator with downward gas-exit. Several cases of different inlet velocity and particle concentration were studied. The particle used in the test
was glass bead of mean diameter 30-40 p,m. Discussion was given on the distribution of flow vector, mean velocity, turbulent intensity and kinetic
energy of both gas and particles of different diameter at different position in the separator. It was found that the center of the flow field deviated
from the geometric center of the cyclone. The flow fields had the feature of Rankine eddy, i.e., strongly swirling region in the central part and
pseudo-free eddy region of weak swirling intensity near the cyclone wall. Local vortex existed at the corners where the flow changed its direction
sharply. When the cyclone wall was heated and the suspension temperature was elevated, the flow field became more uniform than that under
room-temperature condition. The local vortexes at the corners were weakened and the swirling intensity became poorer which led to decreased total
mean separation efficiency from about 81 % to 76.5%. The right-side wall facing the suspension inlet gave the major contribution to the separation
efficiency, where the largest downward velocity was measured. Back-flow (upward velocity) was found around the center of the separator above
the gas-exit. The quasi-laminar motion of particles enhanced the turbulent motion at the corners due to particle-particle or particle-wall collision,
which led to the local peak value of the turbulent kinetic energy and turbulent intensity. The corner was one of the major regions to cause pressure
drop and was found to be beneficial to particle separation mainly because the strong fluctuating flow consumed much of the kinetic energy of both
the particle and gas.
⑥2006 Elsevier B.V. All rights reserved.
Keywords: Square-shaped cyclone separator; Circulating fluidized bed; Turbulent flow; Three-dimensional particle dynamic analyzer (3D-PDA)
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  • 摘要 一个三维粒子动态分析仪(三维掌上电脑)是用来测量气体固两相在实验室规模的方型分离器流 分离器与下气退出。不同的进口速度和颗粒浓度几起案件进行了研究。在测试中使用的粒子 平均直径是30-40磷,玻璃珠米讨论上给出的矢量流,平均流速,湍流强度和动能分布 双方天然气和不同直径的粒子的能量在分离器内不同位置。结果发现,该流场中心偏离 从气旋的几何中心。流场有朗肯涡流,即功能,强旋在中部地区 伪自由涡漩强度弱区附近的气旋墙。涡存在于本地角落流动改变了方向 急剧下降。当气旋壁加热,温度升高暂停,流场变得比,均匀下 室温条件。在角落的地方涡漩的强度减弱,日益贫困,而导致降低总 分离效率平均约81%至76.5%。右侧墙面暂停进口了重大贡献的分离 效率,其中最大的下降速度进行了测量。回流(上升速度)被发现围绕上述中心的分隔 气出口。粒子的准层流运动增强了在弯道由于粒子粒子或粒子碰撞壁湍动, 这导致了湍流动能和湍流强度当地峰值。墙角放着的主要地区之一造成压力 下降,被认为是有利于颗粒分离的强烈波动,主要是因为大部分的流量都动能消耗 粒子和气体。 ⑥2006年埃尔塞维尔B.诉保留所有权利。 关键词:方形旋风分离器;循环流化床;紊流;三维粒子动态分析仪(三维掌上电脑)

    2021-09-07 20:37

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    2021-09-06 20:37

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