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Laminar-to-turbulent transition of pipe flows through puffs and slugs

机译:管道的层流到湍流过渡通过抽吸和塞子

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Laminar-to-turbulent transition of pipe flows occurs, for sufficiently high Reynolds numbers, in the form of slugs. These are initiated by disturbances in the entrance region of a pipe flow, and grow in length in the axial direction as they move downstream. Sequences Of Slugs merge at some distance from the pipe inlet to finally form the state of fully developed turbulent pipe flow. This formation process is generally known, but the randomness in time of naturally occurring slug formation does not permit detailed study of slug flows. For this reason, a special test facility was developed and built for detailed investigation of deterministically generated slugs in pipe flows. It is also employed to generate the puff flows at lower Reynolds numbers. The results reveal a high degree of reproducibility with which the triggering device is able to produce puffs. With increasing Reynolds number, 'puff splitting' is observed and the split puffs develop into slugs. Thereafter, the laminar-to-turbulent transition occurs in the same way as found for slug flows. The ring-type obstacle height, h, required to trigger fully developed laminar flows to form first slugs or puffs is determined to show its dependence on the Reynolds number, Re = DU/v (where D is the pipe diameter, U is the mean velocity in the axial direction and v is the kinematic viscosity of the fluid). When correctly normalized, h(+) turns out to be independent of Re-tau (where h(+) = hU(tau)/v, Re, = DU tau/v and U tau = root tau w/rho; tau(w) is the wall shear stress and rho is the density of the fluid).
机译:对于足够高的雷诺数,以团块的形式发生管道流动的层流到湍流的过渡。这些是由管道流入口区域的扰动引起的,并随着它们向下游移动而沿轴向长度增加。弹头序列在距管道入口一定距离处合并,最终形成充分发展的湍流管道状态。这种形成过程是众所周知的,但是自然产生的团块形成时间的随机性不允许对团块流动进行详细研究。因此,开发并建造了一个专门的测试设备,用于详细研究确定性地产生的管塞中的团块。它也被用来以较低的雷诺数产生粉扑流。结果显示出触发装置能够产生抽吸的高度再现性。随着雷诺数的增加,观察到“粉扑分裂”,并且已分裂的粉扑发展成。此后,层流到湍流的过渡与对于团状流的发现相同。确定触发完全展开的层流以形成第一段塞子或抽吸所需的环形障碍物高度h,以表明其对雷诺数的依赖性Re = DU / v(其中D为管道直径,U为均值轴向速度(v是流体的运动粘度)。正确归一化后,h(+)会独立于Re-tau(其中h(+)= hU(tau)/ v,Re,= DU tau / v和U tau =根tau w / rho; tau( w)是壁面剪应力,rho是流体密度)。

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