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首页> 外文期刊>Powder Technology: An International Journal on the Science and Technology of Wet and Dry Particulate Systems >Numerical simulation of capture process of fine particles in electrostatic precipitators under consideration of electrohydrodynamics flow
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Numerical simulation of capture process of fine particles in electrostatic precipitators under consideration of electrohydrodynamics flow

机译:静电流体流动静电除尘器捕获过程的数值模拟

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In the present work, a numerical method was adopted to study the capture process of fine particles in two electrostatic precipitators (ESPs) with corrugated and parallel plates, respectively.(1) The simplified models were established to evaluate and predict the distribution of electrostatic field, gas dynamic, particle charging, and transport behavior. The electrohydrodynamic (EHD) flow with different applied voltage at various gas velocities was presented on the basis of two kinds of models, and the detailed influence on particle dynamic, including particle trajectory, migration velocity to collection plates, and particle capture had also been investigated thoroughly.(2) Numerical results indicated that corrugated plate electrostatic precipitator (CP ESP),(3) possessed greater electrostatic field characteristic than parallel plate electrostatic precipitator (PP ESP) and it also had a stronger capacity of resisting the influence of EHD flow, which was beneficial from the particular structure.(4) Besides, the EHD flow would make smaller particle present more apparent fluctuant trajectory near discharge wires when fine particles traveled in ESPs at a low gas velocity or with a high applied voltage, and that caused a more severe movement towards collection plates. Numerical results of the evolution of EHD flow showed that the faster elimination of ionic wind vortexes in CP ESP gave rise to higher collection efficiency. With the increment of gas velocity, the intensity of EHD flow exhibited a declining trend, and the difference of collection efficiency between two ESPs also decreased, which suggested that EHD flow had a significant effect on the <1 mu m particle collection and the structure optimization could provide an available approach to evade the influence of EHD flow. (C) 2019 Elsevier B.V. All rights reserved.
机译:在本作本作中,采用了数值方法来研究两个静电除尘器(ESP)中细颗粒的捕获过程,分别具有波纹状和平行板。(1)建立简化模型来评估和预测静电场的分布,气体动态,粒子充电和运输行为。在两种模型的基础上提出了不同施加电压的电液动力学(EHD)流,以及对颗粒动力学的详细影响,包括颗粒轨迹,收集板的迁移速度和颗粒捕获。彻底。(2)数值结果表明,波纹板静电除尘器(CPESPES),(3)具有比平行板静电除尘器(PP ESP)的静电场特性具有更大的静电场特性,并且它也具有更强的抵抗EHD流量的能力,从特定结构中有益。(4)除了,当在低气体速度或高施加的电压下,当细颗粒或具有高施加电压时,EHD流程将使较小的粒子提出更明显的波动轨迹。对收集板更加严重的运动。 EHD流程演化的数值结果表明,CPES中的离子风涡旋速度更快地产生了更高的收集效率。随着气体速度的增量,EHD流的强度表现出下降的趋势,两个ESP之间的收集效率差异也降低,这表明EHD流对<1μM粒子收集和结构优化具有显着影响可以提供一种可用的方法来逃避EHD流量的影响。 (c)2019年Elsevier B.V.保留所有权利。

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