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CFD simulations of cyclone separators with different diameters: Analysis of gas cyclones with different cylinder diameters

机译:具有不同直径的旋风分离器的CFD模拟:具有不同气瓶直径的气体旋风分离器的分析

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The present work is based on studying the effect of varying cyclone main body diameter on its performance. For this purpose Stairmand high efficiency cyclone with main body diameter of 0.29m has been considered. Three different diameters are considered, viz. 0.9D, 1.0D and 1.1D; with D as the diameter of standard cyclone model and the constants being the scaling factor. Pressure drops and collection efficiencies of all the cyclone models have been predicted using commercially available CFD code FLUENT 6.3.26. High quality block structured hexahedral mesh has been created using industry standard software ICEM CFD, upon which the Navier-Stokes equations are solved iteratively using finite volume methods. Reynolds stress model is used as a closure model to solve Reynolds averaged Navier-Stokes (RANS) equations that solves for stress tensors together with the equation for the dissipation rates. The present study shows remarkable effect of the cyclone diameter on its performance which are discussed in details.
机译:当前的工作是基于研究旋风分离器主体直径变化对其性能的影响。为此,已经考虑了主体直径为0.29m的Stairmand高效旋风分离器。考虑了三个不同的直径,即。 0.9D,1.0D和1.1D; D是标准旋风模型的直径,常数是比例因子。已经使用可商购的CFD代码FLUENT 6.3.26预测了所有旋风分离器模型的压降和收集效率。使用行业标准软件ICEM CFD创建了高质量的块状结构的六面体网格,然后使用有限体积方法迭代求解了Navier-Stokes方程。雷诺应力模型用作闭合模型,用于求解雷诺平均Navier-Stokes(RANS)方程,该方程可求解应力张量以及耗散率方程。本研究表明旋风分离器直径对其性能的显着影响,对此进行了详细讨论。

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