Laminar mixing of Newtonian and non-Newtonian fluids in SMX static mixer

IF 1.6 4区 工程技术 Q3 ENGINEERING, CHEMICAL Canadian Journal of Chemical Engineering Pub Date : 2024-03-11 DOI:10.1002/cjce.25232
Neelabja Gayen, Srikanth Swamy, Sridhar Hari, Shirish H. Sonawane
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Abstract

This report is focused on understanding the mixing performance of Newtonian and non-Newtonian fluids in an SMX static mixer through computational fluid dynamics (CFD) study in Simcenter STAR-CCM+. For this, the standard SMX mixer with four mixer elements of radius 26 mm was chosen. The aspect ratio (L/D) was taken as 1. The model constructed was compared using pressure drop ratio values available in literature. First, the design was validated for Newtonian fluid, then for shear-thinning fluid (non-Newtonian). Mixing patterns produced through particle tracking approach revealed how blending improved as the fluid moved downstream and interacted with increasing number of mixer elements. A sensitivity study was undertaken to investigate the effect of particle injection mechanism on the mixing process. Two injection methods, vertical and horizontal, were explored to check the influence of injection position on mixing. The results indicate that for the given configuration irrespective of the injection location, at least four mixing elements are needed to achieve good mixing for both Newtonian and shear-thinning fluids investigated in this study. Statistical reports were used to quantify mixing to understand the mixing behaviour for Newtonian and non-Newtonian fluids with change in Reynolds number. At high Reynolds number, non-Newtonian fluids exhibited better mixing abilities. Further, efforts were taken to optimize the various design parameters to produce the most optimum solution with a single mixer element for Newtonian fluid.

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牛顿流体和非牛顿流体在 SMX 静态混合器中的层流混合
本报告的重点是通过 Simcenter STAR-CCM+ 中的计算流体动力学(CFD)研究,了解牛顿流体和非牛顿流体在 SMX 静态混合器中的混合性能。为此,选择了带有四个半径为 26 毫米的混合元件的标准 SMX 混合器。利用文献中的压降比值对所构建的模型进行了比较。首先,对牛顿流体的设计进行了验证,然后对剪切稀化流体(非牛顿流体)的设计进行了验证。通过粒子跟踪方法生成的混合模式显示了当流体向下游移动并与越来越多的混合器元件相互作用时,混合效果是如何改善的。为研究颗粒注入机制对混合过程的影响,进行了一项敏感性研究。研究探讨了垂直和水平两种喷射方法,以检查喷射位置对混合的影响。结果表明,对于本研究中调查的牛顿流体和剪切稀化流体,无论注入位置如何,在给定配置下至少需要四个混合元件才能实现良好的混合。统计报告用于量化混合,以了解牛顿流体和非牛顿流体随雷诺数变化的混合行为。在高雷诺数下,非牛顿流体表现出更好的混合能力。此外,还对各种设计参数进行了优化,以便为牛顿流体提供使用单一混合器元件的最佳解决方案。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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来源期刊
Canadian Journal of Chemical Engineering
Canadian Journal of Chemical Engineering 工程技术-工程:化工
CiteScore
3.60
自引率
14.30%
发文量
448
审稿时长
3.2 months
期刊介绍: The Canadian Journal of Chemical Engineering (CJChE) publishes original research articles, new theoretical interpretation or experimental findings and critical reviews in the science or industrial practice of chemical and biochemical processes. Preference is given to papers having a clearly indicated scope and applicability in any of the following areas: Fluid mechanics, heat and mass transfer, multiphase flows, separations processes, thermodynamics, process systems engineering, reactors and reaction kinetics, catalysis, interfacial phenomena, electrochemical phenomena, bioengineering, minerals processing and natural products and environmental and energy engineering. Papers that merely describe or present a conventional or routine analysis of existing processes will not be considered.
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Issue Information Issue Highlights Table of Contents Issue Highlights Preface to the special issue of the International Conference on Sustainable Development in Chemical and Environmental Engineering (SDCEE-2024)
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