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CFD Simulation and Analysis of Micro Bubble Generating Nozzles for Microreactors

机译:微气泡微泡微泡的CFD仿真及分析

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Monodisperse micro bubbles (radius ca. 50 μm) are a great benefit for direct fluorination of liquid aromatics. The fluorination process is improved by the large gas-liquid interface compared to slug or jet flow. In this paper we describe a new nozzle concept for monodisperse micro bubble generation which enables a variation of bubble size due to its geometry. The nozzle is a microchannel which is perpendicular to the liquid channel. Snap-off mechanism was described by a measured pressure history inside the nozzle channel. This allows to analyze the size and frequency of bubble generation and therefore, the size of the gas-liquid interface. Quadratic and rectangular geometries were designed and simulated in a three dimensional multiphase system to calculate the formation of fluorine bubbles in toluene. The influence of aspect ratio on the bubble size, generation frequency and liquid flow are presented. It is shown that a rectangular geometry has the fastest snap-off with the smallest bubbles.
机译:单分散微气泡(半径Ca.50μm)是直接氟化液体芳烃的大益处。与SLUG或射流相比,通过大的气液界面改善氟化过程。在本文中,我们描述了一种用于单分散微泡代的新喷嘴概念,其能够在其几何形状引起的气泡尺寸的变化。喷嘴是垂直于液体通道的微通道。通过喷嘴通道内的测量压力历史描述了捕获机构。这允许分析气泡产生的尺寸和频率,因此是气液界面的尺寸。在三维多相体系中设计并模拟了二次和矩形几何形状,以计算甲苯中的氟气泡的形成。呈现了纵横比对气泡尺寸,发电频率和液体流动的影响。结果表明,矩形几何形状具有最快的气泡速度最快。

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