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Modeling pulsed blowing systems for active flow control.

机译:为主动流量控制建模脉冲吹塑系统。

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A model for predicting the performance of pulsed-blowing actuator systems commonly used for many flow control applications is presented and compared with experiments. The actuator system consists of a regulated air supply, oscillatory valve, transmission tubing and actuator. The actuator is a chamber and slot at the location in the flow to be controlled. The typical design objective is to achieve the largest possible velocity fluctuation levels at the actuator slot exit for a given fluctuating pressure input. However, the performance of the system is strongly dependent on geometry, flow rate and frequency of pulsation. Lumped-element models are useful for predicting the performance of the actuator chamber and slot, but fail to account for the effects of the transmission tubing. A distributed model for the tubing combined with a lumped-element model for the actuator accurately predicts system resonance and amplitudes. Comparisons with experiment are made for a wide range of tubing lengths, slot widths, mean flow velocities and forcing frequencies. The resonance of a pulsed blowing system is characterized with open-end resonance and closed-end resonance using the reflection coefficient of the system. Unexpected behavior such as reversed flow at the slot exit is predicted by considering the open-end resonance.; The impedance estimation in the lumped-element model for an actuator plays an important role in predicting the pulsed blowing systems. The exit fluctuating velocity is dependent on the thickness of slots or orifices and the forcing frequency in the linear regime if the thickness is finite and St > 8 . However in most active flow control applications the actuator velocity is in the nonlinear regime, where the fluctuating pressure is proportional to the square of the fluctuating velocity. The nonlinear acoustic effects dominate the impedance, which is proportional to the exit velocity. In a pulsed blowing system, the mean velocity is inevitably superimposed on the fluctuating velocity, so that the nonlinear impedance must be estimated with the superimposed mean flow. The nonlinear phenomena of the flows through an orifice or slot can be understood with the Bernoulli equation in which the pressure drop between an orifice or slot is proportional to the velocity squared. When the fluctuating velocity is superposed with a mean flow at the exit of slots or orifices, it was found that the nonlinear resistances for the mean flow and resistance for the fluctuating flow can be different. Furthermore, the nonlinear resistance is independent of the r.m.s. of the fluctuating velocity u, if the minimum of the instantaneous velocity is greater than zero. This is due to the fact that the high acoustic resistance for high instantaneous velocities and the low acoustic resistance for low instantaneous velocities are averaged constant. In this case, the resistance for the fluctuating velocity can be obtained based on experimental measurements of the resistance at steadying blowing conditions.
机译:提出了一种用于预测许多流量控制应用中常用的脉冲吹气执行器系统性能的模型,并将其与实验进行了比较。执行器系统由调节空气供应,振荡阀,变速箱油管和执行器组成。致动器是在要控制的流中的位置处的腔室和狭槽。典型的设计目标是在给定的波动压力输入下,在执行机构槽出口处获得最大可能的速度波动水平。但是,系统的性能在很大程度上取决于几何形状,流速和脉动频率。集总元件模型可用于预测执行器腔室和插槽的性能,但不能考虑传动管的影响。管道的分布式模型与执行器的集总模型相结合,可以准确预测系统共振和振幅。与实验的比较是针对广泛的油管长度,缝隙宽度,平均流速和强制频率。利用系统的反射系数,脉冲吹塑系统的共振具有开放式共振和封闭式共振的特征。通过考虑开放端共振,可以预测意外行为,例如在插槽出口处的反向流动。执行器的集总元件模型中的阻抗估计在预测脉冲吹塑系统中起着重要作用。如果厚度是有限的并且 St 8 <,则出口波动速度取决于缝隙或孔口的厚度以及线性状态下的强迫频率。 / rcd> 。但是,在大多数主动流量控制应用中,执行器速度处于非线性状态,其中波动压力与波动速度的平方成比例。非线性声学效应决定了阻抗,阻抗与出口速度成正比。在脉冲吹风系统中,平均速度不可避免地会叠加在脉动速度上,因此必须使用叠加的平均流量来估算非线性阻抗。可以通过伯努利方程来理解流过孔或缝的非线性现象,在该方程中,孔或缝之间的压降与速度的平方成比例。发现当在槽或孔的出口处脉动速度与平均流叠加时,发现对于平均流的非线性阻力和对于脉动流的非线性阻力可以不同。此外,非线性电阻与r.m.s无关。如果瞬时速度的最小值大于零,则表示脉动速度 u 的大小。这是由于以下事实:对于高瞬时速度的高声阻和对于低瞬时速度的低声阻被平均。在这种情况下,可以基于在稳定的吹风条件下的电阻的实验测量来获得波动速度的电阻。

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