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Theoretical and experimental studies of mixing enhancement in micromixers.

机译:微型混合器中混合增强的理论和实验研究。

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In combination with low processing flow rate, the small physical dimensions of microscale mixers or reactors imply laminar flow, which precludes convective turbulent mixing normally relied upon for effective mixing in conventional-size processing equipment. The objective of this work is to investigate mixing enhancement in microchannel mixers, through a theoretical as well as an experimental study of currently utilized and proposed micromixing configurations. The design of our proposed micromixers for mixing enhancement is based essentially on the mechanisms of fluid multilamination and elongational flow. In these mixing configurations, mixing is enhanced by placing static or passive mixing structures on the mixer channel floor. This geometric constraint leads to the desired reduction in the fluid diffusion path while at the same time increasing significantly the fluid contact areas via creation of folding as well as local and global re-orientation of fluid interfaces.;In order to establish the experimental platform for the mixing studies, preliminary numerical study is conducted first using computational fluid dynamics (CFD) approach. Using the CFD tools, one of the proposed mixing configurations herein referred to as multilaminated/elongational flow micromixer-4 (MEFM-4) is selected based on the set criteria of minimum pressure drop and high mixing performance. The novel multichannel MEFM-4 and a standard T junction micromixer (TjM), fabricated via silicon micro-electromechanical systems (MEMS) technology, are then characterized experimentally for their mixing performance using residence-time distribution (RTD) measure in conjunction with UV-vis absorption spectroscopy detection technique. The RTD measure chosen represents an innovative technique for the characterization of mixing in micromixers/reactors. Using the RTD and its coefficient of variation as measures for evaluating mixing, the proposed MEFM-4 exhibits better mixing performance than the standard TjM. The results from the numerical simulations and experiments are in very good agreement thus establishing the validity of the mathematical model and the associated solution algorithm implemented in the CFD simulations. The CFD code in conjunction with the numerically obtained RTD can then be used as a predictive tool in the design, evaluation, and optimization of micromixers. The present work describes the efficient design, fabrication and characterization of an effective microchannel mixer for microchemical systems' applications.
机译:与低处理流速相结合,微型混合器或反应器的物理尺寸较小,意味着层流,这排除了常规尺寸的处理设备中通常需要有效进行混合的对流湍流混合。这项工作的目的是通过对当前使用和建议的微混合配置进行理论和实验研究来研究微通道混合器中的混合增强。我们提出的用于混合增强的微混合器的设计基本上基于流体多层化和伸长流动的机理。在这些混合配置中,通过将静态或被动混合结构放置在混合器通道地板上来增强混合。这种几何约束导致所需的流体扩散路径减少,同时通过产生折叠以及流体接口的局部和全局重新定向而显着增加流体接触面积。在混合研究中,首先使用计算流体动力学(CFD)方法进行了初步数值研究。使用CFD工具,根据最小压降和高混合性能的设定标准,选择一种提议的混合配置(本文中称为多层/伸长流动微混合器4(MEFM-4))。然后,通过使用停留时间分布(RTD)措施和UV-UV光谱技术,通过硅微机电系统(MEMS)技术制造的新型多通道MEFM-4和标准T结微混合器(TjM)对其混合性能进行实验表征。可见吸收光谱检测技术。所选择的RTD量度是表征微混合器/反应器混合特性的创新技术。使用RTD及其变异系数作为评估混合的方法,提出的MEFM-4的混合性能优于标准TjM。数值模拟和实验的结果非常吻合,从而建立了数学模型以及在CFD仿真中实现的相关求解算法的有效性。然后,将CFD代码与通过数字方式获得的RTD结合起来,可以用作微型混合器设计,评估和优化中的预测工具。本工作描述了用于微化学系统应用的有效微通道混合器的有效设计,制造和表征。

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