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The role of flow features and chemical kinetics on the reaction yield in a T-shaped micro-reactor

机译:流动特征和化学动力学在T形微反应器中对反应产率的作用

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The effect of flow regimes on the reaction yield of a chemical reaction occurring in a T-shaped micro-reactor is investigated both experimentally and numerically by spanning different Reynolds and Damkohler numbers. The experimental set-up is arranged in order to get in-line information on both fluid dynamics and reaction progress along the mixing channel. Numerical simulations are performed using mesh-adaption cycles to well resolve the mixing between reactants; in this manner, the agreement between experiments and numerical simulations is very satisfactory. For the considered reaction involving two reagents different from water, despite flow regimes are coherent with the ones observed in case of water mixing, significant differences arise because stratification occurs due to the different density of the fluid streams.
机译:通过跨越不同的雷诺和Damkohler数来研究在T形微反应器中发生在T形微反应器中发生的化学反应的反应产率的流动制度。 建立实验组,以便沿着混合通道进入有关流体动力学和反应进展的直线信息。 使用网状适应循环进行数值模拟,以良好地解反应物之间的混合; 以这种方式,实验与数值模拟之间的协议非常令人满意。 对于涉及两种不同于水的试剂的考虑反应,尽管流动制度与在水混合的情况下观察到的流动制度相干,因此出现显着的差异,因为由于流体流的不同密度发生了分层。

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