首页> 外文期刊>The Canadian Journal of Chemical Engineering >STUDY OF FLUID DYNAMIC CONDITIONS IN THE SELECTED STATIC MIXERS PART II-DETERMINATION OF THE RESIDENCE TIME DISTRIBUTION
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STUDY OF FLUID DYNAMIC CONDITIONS IN THE SELECTED STATIC MIXERS PART II-DETERMINATION OF THE RESIDENCE TIME DISTRIBUTION

机译:选定静态混合器中的流体动力学条件研究II部分 - 测定停留时间分布

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摘要

The presented paper is part of the complete description of fluid-dynamic conditions in the selected static mixers: Koflo and Kenics. The research was also performed for an empty pipe used as a reference state. The scope of work included the analysis of the residence time distribution in the mentioned devices for different Reynolds numbers for both laminar and turbulent flow regimes. The report contains a discussion about residence time distribution function E(t), cumulative distribution function F(t), as well as the parameters like the mean residence time tm and the variance sigma(2). The main aim of the presented work was to show the applicability of static mixers as chemical reactors and to present their operation characteristics to evaluate the derogations distinguishing them from well known ideal states (i.e. plug flow or ideal mixing). As a result of the accomplished study it was proved that Reynolds number increase results in narrower RTD in all of the tested devices, however the fluid motion is far from plug flow due to axial and radial mixing and the considered equipment should be treated as non-ideal reactors requiring some additional models for the right description. What is more, in the case of laminar flow, the Kenics static mixer showed the narrowest spread and was considered as the best solution among the studied devices. In the turbulent flow, the difference between E(t) functions for all of the mentioned equipment was so small that the suggestion of small impact of insert type on the RTD was made.
机译:本文是所选静态混合器中的流体动态条件的完整描述的一部分:KOFLO和KENICS。还对用作参考状态的空管道进行了研究。工作范围包括用于层层和湍流的不同雷诺数的所提述装置中提到的装置中的停留时间分布。该报告包含关于居住时间分布功能E(T),累积分布函数F(T)的讨论,以及比例如平均停留时间TM和方差Sigma(2)。本工作的主要目的是展示静态混合器作为化学反应器的适用性,并呈现它们的操作特性,以评估区分其众所周知的理想状态的损失(即塞流或理想混合)。由于完成的研究证明,雷诺数数量增加导致所有测试装置中较窄的RTD,然而,由于轴向和径向混合,流体运动远离塞流,并且所考虑的设备应该被视为非理想的反应堆需要一些额外的型号,以便正确描述。更重要的是,在层流的情况下,Kenics静态混合器显示了最窄的涂抹,并且被认为是研究装置中的最佳解决方案。在湍流中,所有提到设备的E(T)功能之间的差异如此之小,因此制造了插入型在RTD上的少量影响的建议。

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