首页> 外文会议>American Society of Mechanical Engineers(ASME) Summer Heat Transfer Conference(HT2005) vol.1; 20050717-22; San Francisco,CA(UA) >CHARACTERISATION OF STABILITY CRITERIA FOR PRESSURE DRIVEN FLOWS IN SMALL LENGTH SCALE FLUIDIC DEVICES
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CHARACTERISATION OF STABILITY CRITERIA FOR PRESSURE DRIVEN FLOWS IN SMALL LENGTH SCALE FLUIDIC DEVICES

机译:小长度尺度流体装置中压力驱动流动的稳定性判据

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This paper develops criteria for the prediction of two distinct instabilities in microflows, one isothermal, the other with heat transfer. The engineering objective is to transport droplets that act as micro-reactors and are carried through various processes in a carrier fluid to prepare sample reactants or complete a chemical reaction. The requirement is that the carrier fluid flow be stable so that droplet trajectories can be accurately controlled. The popular two-dimensional microfluidic geometry of three streamlines merging at a junction is chosen for this analysis. A dimensional analysis of the governing flow-field and boundary conditions is undertaken to derive the non-dimensional groups upon which the flow characteristics of the junction are dependent. The emerging parameters are the Grasshof number (Gr) and Reynolds numbers (Re) of both inlet streams. Experimental flow visualisation images are used to determine the relationship between these scaling groups for both isothermal flow and buoyancy opposing mixed convection. The experimental range of inlet Re's is from 1 to 100. It is found that the ratio of the inlet Re's is sufficient to describe isothermal flows and that a parameter referred to as W~* (the product of the Richardson number (Ri) and Re of the centreline stream) provides a good correlation for buoyancy opposing mixed convection. Inertia dominated flow regimes are seen to exist for W~* values below approximately 2 and re-circulation zones are observed when W~* is increased above this value. It was also observed that buckling flow was attainable at a critical Re of 65 for isothermal flow and that this critical Re is significantly reduced as W~* is increased. An analogy is drawn from the results between the flow studied in this paper and that of cross flow over bluff objects such as a cylinder. Finally, based on the results of this work a design envelope is developed for predicting the stability of scaled models of the fluidic junction.
机译:本文为微流中两种明显的不稳定性预测标准,一种是等温的,另一种是传热的。工程目标是运送充当微反应器的液滴,并在载液中通过各种过程进行运输,以制备样品反应物或完成化学反应。要求载流体稳定,以便可以精确地控制液滴轨迹。本分析选择了在交汇处合并的三个流线的流行二维微流体几何形状。对控制流场和边界条件进行了维分析,以得出结点的流动特性所依赖的无维组。新出现的参数是两种进口流的格拉斯霍夫数(Gr)和雷诺数(Re)。实验流动可视化图像用于确定等比例流动和与混合对流相对的浮力的这些比例组之间的关系。入口Re's的实验范围是1到100。发现入口Re's的比足以描述等温流动,并且参数W〜*(​​理查森数(Ri)和Re中心流的流向提供了良好的相关性,以防止混合对流产生的浮力。 W〜*值低于约2时,惯性占主导地位的流动态被发现,当W〜*增大到该值以上时,观察到再循环区域。还观察到,对于等温流,在临界Re为65时可获得屈曲流,并且随着W〜*的增加,该临界Re显着降低。从本文研究的流动与钝性物体(例如圆柱体)上的交叉流动的结果之间可以得出一个类比。最后,根据这项工作的结果,设计了一个设计包络,用于预测流体连接的比例模型的稳定性。

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