The entrainment and mixing processes in an axisymmetric vertical turbulent buoyant jet and its transition from a jet to a plume have been studied. The ambient fluid is of uniform density and calm except for the flow induced by the jet, and the density variations are assumed small.ududA systematic set of experiments was carried out to examine turbulent buoyant jet behavior over a wide range of initial jet Richardson numbers. All experiments were performed in a glass wall tank with dimensions 1.15m x 1.15m x 3.30m deep, equipped with a jet flow source and an instrument carriage to enable the velocity and concentration measurements in the entire jet flow field.ududThe axial and radial velocity components and the concentration of a Rhodamine 6G dye were measured simultaneously at the same point of the jet flow field using a two-reference beam laser-Doppler velocimeter combined with a laser induced fluorescence measuring device. From the time signals of the axial and radial velocity components (w) and (u) and the concentration (c) of the Rhodamine 6G dye, information was obtained concerning the mean values, turbulent fluctuations and correlations between w, u and c, up to 100 jet and 80 plume diameters downstream of the jet exit.ududMore specifically, the mean flow (including the spread rate of the mean velocity and tracer concentration profiles and distribution along the jet axis) and the turbulent structure (including the profile of turbulence intensity, turbulent mass flux of a tracer and turbulent momentum flux) were investigated as a function of distance from jet origin made dimensionless by a characteristic length scale based on jet buoyancy and momentum fluxes. The results from a detailed dimensional analysis were verified experimentally. It was determined that the turbulent flux of a tracer (or buoyancy) varied from 6-10% for jets and was 15-20% of the total for plumes. The turbulent momentum flux was found to be 15% of the local momentum flux transported by the mean flow.ududWhile the profiles of w and c and the turbulent velocity profiles are found to be much the same for both jets and plumes, the turbulence intensity profiles of the concentration take higher values in plumes than in jets. More rapid dilutions were obtained in buoyancy driven plumes than in momentum driven jets.ududUseful information concerning engineering applications is provided from the experimental constants derived.
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机译:研究了轴对称垂直湍流浮力射流的夹带和混合过程以及从射流到羽流的过渡过程。除了射流引起的流动外,环境流体的密度均匀且稳定,并且假定密度变化较小。 ud ud进行了一套系统的实验,以检查在较宽的初始射流范围内的湍流浮力行为理查森数字。所有实验均在尺寸为1.15mx 1.15mx 3.30m深的玻璃壁储罐中进行,该储罐配有喷射流源和仪器托架,可在整个喷射流场中进行速度和浓度测量。使用两参考束激光多普勒测速仪结合激光诱导荧光测量装置,同时在射流流场的同一点测量速度成分和若丹明6G染料的浓度。从罗丹明6G染料的轴向和径向速度分量(w)和(u)的时间信号以及浓度(c)的时间信号中,可以获得有关平均值,湍流涨落以及w,u和c之间的相关性的信息。射流出口下游有100个射流和80个羽流直径。 ud ud更具体地说,是平均流量(包括平均速度和示踪剂浓度分布的扩散率以及沿射流轴的分布)和湍流结构(包括分布湍流强度,示踪剂的湍流质量通量和湍流动量通量的变化)是根据距射流起点的距离的函数而变化的,该距离是通过基于射流浮力和动量通量的特征长度尺度而无量纲的。详细的尺寸分析结果通过实验得到验证。已确定示踪剂(或浮力)的湍流通量对于喷气机为6-10%,对于羽流为总通量的15-20%。发现湍流动量通量是通过平均流传输的局部动量通量的15%。 ud ud尽管发现w和c的分布以及湍流速度分布对于射流和羽流几乎相同,但浓度的湍流强度分布在羽状流中比在喷射流中具有更高的值。在浮力驱动的羽流中获得的稀释比在动量驱动的喷气流中得到的稀释更快。 ud ud有关工程应用的有用信息可从得出的实验常数中获得。
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