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EFFECTS OF OBSTACLES ON THE MIXING PERFORMANCE IN MICROCHANNELS

机译:障碍对微通航中混合性能的影响

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The mixing of two or more fluid streams in microchannels needs quite long channel lengths. Therefore, in order to improve the mixing performance, obstacles have been placed in the channel to disrupt flow and to reduce the diffusion path. The disruption to flow velocity field alters the flow direction from one fluid to another. Properly designed geometric parameters, such as layout, angle with main flow direction and aspect ratio of obstacles, will be resulted in improving the mixing performance with only little increase of the pressure drop. In this study, T-type rectangular microchannel is used, which has two inlets with W×H×L=100×100×1000 μm~ and one outlet with W×H×L=200× 100×6950 μm~3. Furthermore, the mixing channel has obstacles which are placed with an angle of inclination and with dimensions W×H×L=10×100×h μm~3 on the lower layer. In order to estimate the performance of the mixing, numerical analyses are carried out with water and ethanol. Especially, the diffusion coefficient, D , is set to 10~(-10) m~2/s for simulating two-fluid diffusion-convection flow, the mixing efficiency and the pressure drop of microchannel are investigated with various values of the angle of inclination, aspect ratio (h=αH) of obstacle and Reynolds number. When the flow passes through on the obstacles, rotation flow is observed. This flow pattern is repeated at each cycle. Besides, in each case that obstacles are turned to the center of channel and to the side walls, rotational direction is changed reversely. In case of pressure drop, as the Reynolds number, the angle of obstacle (θ) and the aspect ratio (α ) are increased, the pressure drop is also increased. Results show that the ratio between the maximum and minimum of pressure drop is the order-of-magnitude of 1 at Re= 1.667. Results also show that the angle of inclination of obstacles has more influence on the mixing performance than the height of obstacles and Reynolds number.
机译:微通道中的两个或更多个流体流的混合需要相当长的通道长度。因此,为了提高混合性能,障碍物已放置在通道中以破坏流动并减少扩散路径。流速场的破坏使流动方向从一个流体变为另一个流体。适当设计的几何参数,例如布局,具有主流方向的角度和障碍物的宽高比,将导致改善混合性能,仅增加压降。在该研究中,使用T型矩形微通道,其具有W×H×L = 100×100×100×100×100×100×100×100×100×100×L = 200×100×6950μm〜3的两个入口。此外,混合通道具有以倾斜角度放置的障碍物,并且在下层上具有尺寸W×H×L = 10×100×Hμm〜3。为了估计混合的性能,用水和乙醇进行数值分析。特别是,扩散系数D,用于模拟两个流体扩散 - 对流流量的10〜( - 10)m〜2 / s,以各种角度对微通道的混合效率和压力降障碍物和雷诺数的倾斜度,纵横比(H =αh)。当流动通过障碍物时,观察到旋转流程。在每个循环中重复该流动模式。此外,在每种情况下,障碍物转向通道的中心和侧壁,旋转方向反向变化。在压降的情况下,作为雷诺数,障碍物(θ)和纵横比(α)增加,压降也增加。结果表明,压降的最大和最小值之间的比率是RE = 1.667的级别为1。结果还表明,障碍物的倾斜角度对混合性能的影响比障碍物的高度和雷诺数的高度更多。

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