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Mechanisms of lobed jet mixing: About circularly alternating-lobe mixers

机译:裂片喷射混合机理:关于圆形交替叶混合器

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Two configurations of circularly arranged alternating-lobe nozzles were adopted to form lobed mixers with/without a mixing duct. The jet mixing of each mixer was numerically simulated with the unchanged initial conditions of the primary and secondary streams, except the altered initial velocity of the secondary stream. The jet-mixing mechanisms of the circularly alternating-lobe mixers were synthetically analysed by combining the evolution of the flow field structures and the process of heat and mass transfer in the mixing field. It is found that the transverse flow is usually caused by the lobed geometry, and the entrainment of the primary stream also plays a role in certain circumstances. There are two mechanisms for the deflection of the transverse flow at the lobe peaks and troughs. One of these mechanisms is to be suppressed to deflect the flow while the other is deflected by the reaction force and induction effect. The primary and secondary streams deflect to bring the transverse interval between them, and subsequently, the streamwise vortex core appears at the transverse interval. The deflected flow consistently "digging" in the radial and circumferential radiation increases the dimension of the streamwise vortices. The transverse flow velocity decreases and the direction becomes unstable leading to the breakdown of the streamwise vortices. The transverse flow brings the heat and mass transfer. Under the two mechanisms, the frontiers of the primary and secondary streams deflect. Initially, the primary and secondary streams flow around the streamwise vortex core. Subsequently, the mixed stream flows around the vortex core, and the mixing stream area gradually expands outward. The heat and mass transfer decrease in scale when the streamwise vortices break down. Because of the velocity gradient at the interface, shear instability occurs to generate the normal vortex ring. The heat and mass transfer pushes the interface, which leads to the stretch of the normal vortex ring. The mixing speed varies due to the heat and mass transfer. The velocity gradient decreases fast in the rapid mixing segment, where the normal vortex ring breaks first. (C) 2019 Elsevier Masson SAS. All rights reserved.
机译:采用两种圆形布置的交替叶喷嘴构造以形成具有/没有混合管道的裂片混合器。除了次流的改变的初始速度之外,每种混合器的喷射混合用初级和次生流的不变初始条件进行数值模拟。通过组合流场结构的演变和混合场中的热量和质量传递过程来合成圆形交替叶混合器的喷射混合机制。结果发现,横向流通常由裂片的几何形状引起,并且在某些情况下,主流的夹带也起着作用。存在叶片峰和槽上的横向流的两个机制。将抑制这些机构中的一种以使流动偏转,而另一个机构被反作用力和感应效果偏转。初级和辅助流偏转以使它们之间的横向间隔带来,然后,流动涡流核心出现在横向间隔。偏转的流动在径向和周向辐射中一致“挖掘”增加了流动涡流的尺寸。横向流速降低,方向变得不稳定,导致流动涡流的击穿。横向流动带来了热量和传质。在两个机制下,初级和次级流的前沿偏转。最初,初级和次级流围绕流涡流核心流动。随后,混合流围绕涡旋芯流动,并且混合流面积逐渐向外扩展。当流动涡流中断时,热量和质量传递的变化降低。由于界面处的速度梯度,发生剪切不稳定性以产生正常的涡旋环。热量和传质推动界面,这导致正常涡旋环的拉伸。混合速度由于热量和传质而变化。快速混合段中的速度梯度减少,其中正常涡旋环首先断裂。 (c)2019年Elsevier Masson SAS。版权所有。

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