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T型微反应器中流动非定常性对化学反应产率影响的研究

A Study on the Effect of Flow Unsteadiness on the Yield of a Chemical Reaction in a T Micro-Reactor.

作者信息

Mariotti Alessandro, Antognoli Matteo, Galletti Chiara, Mauri Roberto, Salvetti Maria Vittoria, Brunazzi Elisabetta

机构信息

Dipartimento di Ingegneria Civile e Industriale, Università di Pisa, Largo Lazzarino 2, 56122 Pisa, Italy.

出版信息

Micromachines (Basel). 2021 Feb 27;12(3):242. doi: 10.3390/mi12030242.

Abstract

Despite the very simple geometry and the laminar flow, T-shaped microreactors have been found to be characterized by different and complex steady and unsteady flow regimes, depending on the Reynolds number. In particular, flow unsteadiness modifies strongly the mixing process; however, little is known on how this change may affect the yield of a chemical reaction. In the present work, experiments and 3-dimensional numerical simulations are carried out jointly to analyze mixing and reaction in a T-shaped microreactor with the ultimate goal to investigate how flow unsteadiness affects the reaction yield. The onset of the unsteady asymmetric regime enhances the reaction yield by more than 30%; however, a strong decrease of the yield back to values typical of the vortex regime is observed when the flow undergoes a transition to the unsteady symmetric regime.

摘要

尽管T形微反应器的几何形状非常简单且为层流,但已发现其具有不同且复杂的稳态和非稳态流动状态,这取决于雷诺数。特别是,流动的非稳态会强烈改变混合过程;然而,对于这种变化如何影响化学反应的产率却知之甚少。在本工作中,联合进行了实验和三维数值模拟,以分析T形微反应器中的混合和反应,最终目标是研究流动的非稳态如何影响反应产率。非稳态不对称状态的出现使反应产率提高了30%以上;然而,当流动转变为非稳态对称状态时,观察到产率大幅下降,回到涡旋状态的典型值。

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