用计算流体动力学评价静态混合器的混合性能

Kanishk Patel, A. Komrakova
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引用次数: 0

摘要

静态混合器是在线不动的装置,可以放置在管道中,以促进混相流体的混合或不混相液体的分散。这些刀片的特点是混合性能和它们产生的压降。为了满足最终产品的某些要求,不断提出新的静态混合器设计。建议使用计算流体动力学(CFD)来可视化和量化新的刀片设计,而不是制造大量不同设计的原型并进行昂贵的实验来评估刀片的特性。在这项研究中,我们展示了如何有效地使用CFD来量化六元Kenics混合器的混合性能。通过考虑单相不可压缩流和被动标量方程的解,在数值上复制了两种可混溶液体的系统,该系统复制了含有染料的类似液体的注入。采用商用CFD软件包STAR-CCM+、西门子PLM进行仿真。分析了雷诺数为12 000的Kenics混合器的三维、瞬态、不可压缩、单相湍流流动。考虑了三种湍流模型:可实现k-ε模型、EB k-ε模型和雷诺应力模型。为了保证网格独立性,在三个连续细化的结构网格上进行模拟,其中最细的网格由1000万个单元组成。得到的数值数据与已有的实验数据吻合较好,压降估算值的偏差在10%以下。本文还研究了混合对湍流模型选择的弱依赖性。通过评价混合过程中浓度、混合尺度的变化及其特征变化的原因来评价混合性能。提出了量化标量浓度的空间或时间隔离的新定义,以更深入地了解混合。被动标量注入点的位置与混合效率之间也存在很强的相关性,这有助于预测产生最大混合效率的注入位置。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Assessing Mixing Performance of a Static Mixer Using Computational Fluid Dynamics
Static mixers are in-line motionless devices that can be placed into a pipe to promote the blending of miscible fluids or dispersion of immiscible liquids. These inserts are characterized by the mixing performance and the pressure drop they create. New designs of static mixers are continuously proposed to meet certain requirements of the final product. Instead of manufacturing numerous prototypes of different designs and conducting costly experiments to assess the characteristics of the inserts, it is suggested to use computational fluid dynamics (CFD) to visualize and quantify new insert designs. In this study, we demonstrate how CFD can be efficiently used to quantify the mixing performance of a six-element Kenics mixer. A system of two miscible liquids is numerically replicated by considering a single-phase incompressible flow coupled with the solution of a passive scalar equation that replicates the injection of similar fluid with dye in it. A commercial CFD package STAR-CCM+, Siemens PLM was used to perform simulations. Three-dimensional, transient, incompressible, single-phase, turbulent flow across the Kenics mixer, corresponding to a Reynolds number of 12 000 is analyzed. Three turbulence models are considered: realizable k-ε , EB k- ε and Reynolds stress model. To ensure mesh independence, the problem is simulated on three successively refined structured grids with the finest mesh consisting of 10 million cells. The obtained numerical data agree well with the available experimental data: the deviation of the pressure drop estimate is below 10%. A weak dependence of mixing on the choice of turbulence model is also investigated. The mixing performance is assessed by evaluating variation in concentration, mixing scales and the cause for their characteristic changes during the process. Novel definitions to quantify spatial or temporal segregation of scalar concentration are proposed to provide deeper insight into mixing. A strong correlation between the location of the passive scalar injection point and the mixing efficiency was also observed, which helped in predicting the injection location that yields the maximum mixing efficiency.
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