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Modeling the gas and particle flow inside cyclone separators

机译:模拟旋风分离器内的气体和颗粒流

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This paper reviews the models developed for the flow field inside inverse-flow cyclone separators. In a first part, traditional algebraic models and their foundations are summarized in a unified manner, including the formulae for tangential velocity and pressure drop. The immediate application to the prediction of collection efficiency is also reviewed. The approach is the classical, treating first the dilute limit (clean-gas correlations), and afterwards correcting for "mass loading" effects. Although all these methods have had a remarkable success, more advanced ideas are needed to model cyclones. This is put forward by exploring the work done on the so-called "natural" length of the cyclone, that has led to the discovery of instability and secondary flows. The resort to computational fluid dynamics (CFD) in this case is difficult, however, due to the very nature of the flow structure. A closing section on the subject reviews past and recent CFD simulations of cyclones, both single- and two-phase, steady and unsteady, aiming at delineating the state-of-the-art, present limitations and perspectives of this field of research.
机译:本文回顾了针对逆流旋风分离器内部流场开发的模型。在第一部分中,以统一的方式总结了传统的代数模型及其基础,包括切向速度和压降的公式。还回顾了在收集效率预测中的直接应用。该方法是经典方法,首先处理稀释极限(清洁气体相关性),然后校正“质量负载”效应。尽管所有这些方法都取得了显著成功,但仍需要更高级的思想来模拟旋风分离器。通过探索在旋风的所谓“自然”长度上所做的工作来提出这一问题,这导致了不稳定和二次流动的发现。但是,由于流动结构的本质,在这种情况下很难采用计算流体动力学(CFD)。该主题的结尾部分回顾了过去和最近的CFD模拟旋流器,包括单相和两相,稳态和非稳态的旋风分离器,旨在描绘出最新的技术,并提出了该研究领域的局限性和观点。

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