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Prediction of gas-particle separation efficiency for cyclones: A time-of-flight model

机译:旋风分离器气体-颗粒分离效率的预测:飞行时间模型

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Modeling the particle separation efficiency has been a topic of interest since the air cyclones was introduced for gas-particle separation in the fields of environmental science and chemical engineering. In this work, a new simple time-of-flight model is theoretically developed to predict the particle separation efficiency in cyclones. In this model, the equivalent volume method is employed to geometrically modify the cylindrical-conical type cyclone as a right cylindrical cyclone in order to overcome the nonuniform effect on the particle separation distance. Based on the analysis of the gas flow pattern and the particle dynamics in the cyclone separator, the differential equation for the time-of-flight model is established according to the principle of particle mass balance. The model can be finally expressed as a simple explicit function including the main cyclone dimensions and operating parameters, without the need for solving complex equation of mathematical physics. The influences of the short-circuit flow near the bottom of cyclone outlet duct and the exchange flow between outer and inner vortex flow are comprehensively considered to revise the effective residence time of gas flow, a key parameter in the present model. By comparisons with experimental data as well as other classical separation models for the cyclones with different geometrical configurations and operating conditions, the results show that the present model has a relatively high predicted accuracy with the mean squared error of 0.0158. It is demonstrated that the present model has considerable availability for predicting the particle separation efficiency for cyclone separators.
机译:自从在环境科学和化学工程领域引入空气旋风分离器以进行气体-颗粒分离以来,对颗粒分离效率进行建模一直是一个令人感兴趣的话题。在这项工作中,理论上开发了一个新的简单飞行时间模型来预测旋风分离器中的颗粒分离效率。在该模型中,采用等效体积法将圆柱圆锥形旋风分离器几何形状修改为右圆柱旋风分离器,以克服对颗粒分离距离的不均匀影响。在分析旋风分离器内的气体流动规律和颗粒动力学的基础上,根据颗粒质量平衡原理,建立了飞行时间模型的微分方程。该模型最终可以表示为一个简单的显式函数,包括主要的旋风分离器尺寸和运行参数,而无需求解复杂的数学物理方程。综合考虑旋流器出口管道底部附近的短路流和内外涡流之间的交换流的影响,以修正气流的有效停留时间,这是本模型的关键参数。通过与实验数据以及具有不同几何构型和运行条件的旋风分离器的其他经典分离模型进行比较,结果表明,该模型具有相对较高的预测精度,均方误差为0.0158。证明了本模型对于预测旋风分离器的颗粒分离效率具有很大的实用性。

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