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首页> 外文期刊>Experiments in Fluids: Experimental Methods and Their Applications to Fluid Flow >Evaluation of a full-scale helium-filled soap bubble generator
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Evaluation of a full-scale helium-filled soap bubble generator

机译:评估全尺寸氦气肥皂泡发生器

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摘要

Various aspects of the design and operation of a full-scale helium-filled soap bubble generator are studied. Shadowgraphy, particle image/tracking velocimetry, hotwire anemometry, and Monte Carlo simulations are employed to investigate bubble production regimes, diameters, production rates, time responses, and the flow quality downstream from the full-scale system. Modifications to internal nozzle geometry are found to greatly impact the production regimes that the nozzles operate within. Specifically, improving the axisymmetry of the air flow within a nozzle leads to desirable bubble formation over a larger range of input combinations and the ability to operate at larger input rates in general. The input of bubble film solution (BFS) is also found to be important for ensuring proper operation, as both small and large inputs lead to undesirable production. A previously defined theoretical relationship (Faleiros et al., Exp Fluids 60:40, 2019) between input parameters and the mean bubble time response is confirmed but found to vary depending on nozzle operation, as spilled BFS and leaked helium during bubble formation cause deviation from theoretical operation. Monte Carlo simulations reveal that the spatial filtering of particle image velocimetry (PIV) reduces the standard deviation of the effective distribution of the bubble time responses by a factor of PPIR-1/2, where PPIR is the number of particles per interrogation region. This power law is used to derive an equation for estimating the minimum time scale of the flow that can be resolved using the bubbles from a given generator during applications of PIV. Finally, the wind tunnel flow downstream from a full-scale generator is found to be affected by the blockage of the structure, with the freestream deficit increasing by at most 1.2% of the mean and the freestream turbulence intensity increasing by at most 0.3% for freestream velocities of 6 m/s or greater.Graphic abstract
机译:研究了全级氦气填充肥皂泡发生器的设计和操作的各个方面。影像,粒子图像/跟踪速度,Hotwire风光仪和蒙特卡罗模拟用于调查气泡生产制度,直径,生产率,时间响应,以及全规模系统下游的流量质量。发现对内部喷嘴几何的修改会大大影响喷嘴在内部操作的生产制度。具体地,改善喷嘴内的空气流的轴对称导致在较大范围的输入组合上的所需气泡形成,并且通常以较大的输入速率操作。还发现气泡膜溶液(BFS)的输入对于确保适当的操作是重要的,因为这两种小输入都导致不希望的生产。先前定义了输入参数和平均气泡时间响应之间的定义了理论关系(Faleiros等人,Exp流体60:40,2019),但发现根据喷嘴操作而变化,如溢出的BFS在气泡形成期间溢出的氦气导致偏差从理论运作。蒙特卡罗模拟表明,粒子图像速度(PIV)的空间滤波降低了PPIR-1/2的泡沫时间响应的有效分布的标准偏差,其中PPIR是每个询问区域的颗粒的数量。该权力法用于导出用于估计可以在PIV的应用期间使用来自给定发电机的气泡来解决的流程的最小时间尺度的等式。最后,发现来自全尺度发电机的下游的风隧道流动受到结构堵塞的影响,自由流缺陷的增加,最多1.2%的平均值和自由流湍流强度最多为0.3% FreeStream速度为6米/秒或更大。图摘要

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