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Flow patterns and mass transfer performance of miscible liquid-liquid flows in various microchannels: Numerical and experimental studies

机译:各种微通道中可混溶液体流动的流动模式和传质性能:数值和实验研究

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The advantages of miniaturized systems and the laminar flow regime that is present in microfluidic channels have opened a new range of applications in which the use of multiple streams with different reagents is exploited. However, further development of these microdevices needs deeper understanding on the phenomena involved in order to efficiently design such microsystems. In this work, we report the analysis of the solute mass transport performance in Y-Y-shaped microchannels as a function of the coupled influence of both the flow patterns and mass transport kinetics. With this objective, the influence of the following operation variables has been analyzed, the ratio between the residence and diffusion times (gamma) and the volumetric ratio between the fluid phases (alpha), that was determined for three different geometric configurations. The performance of the devices was presented as the solute separation factor in the donor fluid and the concentration factor in the receiving phase. Results showed that the ratio alpha greatly impacts the solute concentration value reported in both phases for the same gamma value, which in turn influences the solute mass flow at the channel outlets. Both the flow patterns and the concentration gradients developed inside the systems were numerically studied by using Computational Fluid Dynamics (CFD) techniques and experimentally analyzed by fluorescence microscopy with fluorescein employed as model solute. This study represents a thorough analysis of the phenomena that determine the performance of the separation of solutes between homogeneous flowing fluids in microdevices where the fluid dynamics are coupled with mass transfer phenomena and facilitates its extension to the general case where separation is enhanced by chemical reactions.
机译:小型化系统的优点和微流体通道中存在的层流变管已经开启了一种新的应用范围,其中利用了使用不同试剂的多个流的使用。然而,这些微生物的进一步发展需要更深入地了解所涉及的现象,以便有效地设计如此微系统。在这项工作中,我们报告了Y-Y形微通道中的溶质大规模运输性能的分析,作为流动模式和质量传输动力学的耦合影响的函数。利用该目的,已经分析了以下操作变量的影响,其居住和扩散时间(γ)之间的比率和用于三种不同的几何构造的流体相(α)之间的流体相(α)之间的体积比。将器件的性能作为供体流体中的溶质分离因子和接收相中的浓度因子呈现。结果表明,比率α大大撞击两个相对于相同伽马值的两相的溶质浓度值,这反过来影响通道出口处的溶质质量流量。通过使用计算流体动力学(CFD)技术和通过用作模型溶质的荧光显微镜进行实验分析,通过使用荧光显微镜进行实验分析来进行数值研究系统内部的流动模式和浓度梯度。该研究代表了确定溶解质在均匀流体中溶解质在微生物中的流动流体与传质现象耦合的情况下进行分离的彻底分析,其中通过化学反应增强分离的一般情况下,促进其延伸。

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