Understanding solid particle transport in a gas cyclone separator

IF 3.6 2区 工程技术 Q1 MECHANICS
M. Sommerfeld, M.A. Taborda
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引用次数: 0

Abstract

A cyclone separator is a widespread device used in many industrial areas and daily life for removing fine particulate matter from a gas stream. This separator has been used for more than 100 years due to its simple and robust design, but was continuously further developed and adapted to specific applications. The mostly used configuration is the reverse flow type cyclone exhibiting however, a very complex vortex flow with high turbulence. In the past numerous experimental as well as numerical studies were conducted for optimising cyclone geometry with the goal of improving the separation efficiency. In most of the numerical studies done so far not all the relevant transport mechanisms affecting particle motion were considered. Therefore, a thorough numerical investigation is presented using an LES-point-particle-Euler/Lagrange approach with momentum 2-way coupling for analysing the effects of particle-scale transport processes on the performance of a 290 mm Stairmand type of cyclone. All simulations presented here were conducted for an inlet velocity of 10 m/s. The sub-grid-scale (SGS) turbulence was described by a dynamic Smagorinsky model. Particle transport was computed considering all relevant forces and modelling also SGS dispersion. For the first time, the influence of particle collisions with rough walls, modelled according to the stochastic approach presented by Sommerfeld and Huber (International Journal of Multiphase Flow, Vol. 25, 1457-1489, 1999), was analysed in detail with respect to the performance of a cyclone separator. Moreover, inter-particle collisions were described through the efficient stochastic model introduced by Sommerfeld (International Journal of Multiphase Flow, Vol. 27, 1828-1858, 2001). Specifically, the importance of the interplay between rough wall collisions and inter-particle collisions is highlighted in this contribution. Three different particle size spectra were considered with log-normal size distributions ranging up to 20 μm (mean diameter 5.21 μm), up to 60 μm (mean diameter 15.43 μm), and up to 100 μm (mean diameter 25.71 μm); each case with different mass loading. Naturally, due to their different inertia, the effects of wall collisions and inter-particle collisions are also different for these types of particles. After a thorough validation, the influences of two-way coupling, particle rough wall collisions (three surface roughness degrees) and inter-particle collisions are analysed and elucidated. It is shown that specifically surface roughness has a huge effect on the grade efficiency of a cyclone and cannot be neglected, as done in most numerical cyclone studies done so far. Inter-particle collisions may partly compensate the deterioration of separation by wall roughness.

Abstract Image

了解气体旋风分离器中的固体颗粒传输
旋风分离器是一种广泛应用于许多工业领域和日常生活中的设备,用于去除气流中的微粒物质。这种分离器因其设计简单、坚固耐用,已使用了 100 多年,但仍在不断改进,以适应特定的应用。最常用的配置是反向流型旋风分离器,但这种旋风分离器会产生非常复杂的高湍流涡流。过去,为了优化旋流器的几何形状,进行了大量的实验和数值研究,目的是提高分离效率。在迄今为止进行的大多数数值研究中,并没有考虑到影响颗粒运动的所有相关传输机制。因此,本文采用具有动量双向耦合的 LES-点-颗粒-Euler/Lagrange 方法进行了全面的数值研究,以分析颗粒尺度传输过程对 290 毫米 Stairmand 型旋风分离器性能的影响。本文介绍的所有模拟都是在入口速度为 10 米/秒的条件下进行的。亚网格尺度(SGS)湍流由动态 Smagorinsky 模型描述。计算粒子传输时考虑了所有相关的作用力,并对 SGS 扩散进行了建模。根据 Sommerfeld 和 Huber(《国际多相流杂志》,第 25 卷,1457-1489 年,1999 年)提出的随机方法建模,首次详细分析了颗粒与粗糙壁碰撞对旋风分离器性能的影响。此外,还通过 Sommerfeld(《国际多相流杂志》,第 27 卷,1828-1858 年,2001 年)引入的高效随机模型对粒子间碰撞进行了描述。具体而言,粗糙壁面碰撞和粒子间碰撞之间的相互作用在本文中得到了强调。我们考虑了三种不同的粒度谱,其对数正态粒度分布范围分别为 20 μm(平均直径 5.21 μm)、60 μm(平均直径 15.43 μm)和 100 μm(平均直径 25.71 μm);每种情况下的质量负荷都不同。当然,由于惯性不同,壁面碰撞和颗粒间碰撞对这些类型颗粒的影响也不同。经过全面验证后,分析并阐明了双向耦合、颗粒粗糙壁面碰撞(三种表面粗糙度)和颗粒间碰撞的影响。结果表明,具体来说,表面粗糙度对旋风分离器的分级效率有很大影响,不能像迄今为止的大多数旋风分离器数值研究那样被忽视。颗粒间的碰撞可以部分弥补壁面粗糙度对分离效果的影响。
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来源期刊
CiteScore
7.30
自引率
10.50%
发文量
244
审稿时长
4 months
期刊介绍: The International Journal of Multiphase Flow publishes analytical, numerical and experimental articles of lasting interest. The scope of the journal includes all aspects of mass, momentum and energy exchange phenomena among different phases such as occur in disperse flows, gas–liquid and liquid–liquid flows, flows in porous media, boiling, granular flows and others. The journal publishes full papers, brief communications and conference announcements.
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