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MEAN VELOCITY MEASUREMENTS IN A 3'-HYDROCYCLONE USING LASER DOPPLER ANEMOMETRY.

机译:使用激光多普勒比色法测量3英寸双液力旋流器中的平均速度。

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Within the class of inertial separators, the hydrocyclone is especially noteworthy because of its simplicity of operation and its many diverse applications. Although a good qualitative understanding of solid-liquid separations in hydrocyclones is presently available, the relative importance of the various secondary motions on the separation efficiency of a hydrocyclone has not been quantitatively considered.; In the absence of a particulate phase and an air core, a quantitative study of the axial and tangential components of the mean velocity in a glass 3''-hydrocyclone using laser doppler anemometry has revealed multiple reverse flows in the vortex core. Flow visualization by dye injection shows that these flows are coherent over a significant portion of the hydrocyclone and that little radial mixing occurs between these secondary flows and the outer helical flow, although the Reynolds number based on the entrance diameter and feed flow rate exceeded 10,000. Several different vortex finder designs were studied, including one which satisfies standard optimal scaling rules. It was discovered that a 2:1 contraction in the vortex finder causes four distinct simultaneous countercurrent flows in the conical section of the hydrocyclone. Moreover, for low backpressure operation (< 2 psig), a recirculation zone was detected in the upper part of the hydrocyclone with as many as six reverse flows. For some hydrocyclone designs and operating conditions, a jet-like flow on the axis occurs from the apex region to the vortex finder. This phenomenon partially explains why the design criteria of Rietema are optimal. The measured tangential velocity profiles were independent of axial location, and showed a characteristic "forced" and "free" vortex behavior in the inner and outer regions, respectively. The addition of 100 wppm Separan AP-30 decreased the tangential velocity and reduced the magnitude of the reverse flows in the core region. For the hydrocyclone studied, a split ratio from zero to infinity and a feed rate from 150-500 cm('2)/sec have little effect on the vortex diameter ((TURNEQ) 3 mm) and the conical locus of zero axial velocity in the outer flow domain.
机译:在惯性分离器类别中,水力旋流器因其操作简单和多种应用而特别引人注目。尽管目前对旋液分离器中的固液分离已有很好的定性理解,但是各种二次运动对旋液分离器分离效率的相对重要性尚未得到定量考虑。在没有颗粒相和空芯的情况下,使用激光多普勒风速计对玻璃3''-水力旋流器中平均速度的轴向和切向分量进行了定量研究,结果表明涡旋芯中存在多个反向流动。通过染料注入的流动可视化显示,尽管在入口直径和进料流速的基础上,雷诺数超过10,000,但在水力旋流器的很大一部分上这些流是连贯的,并且在这些次级流和外部螺旋流之间几乎没有径向混合。研究了几种不同的涡流探测器设计,其中包括一种满足标准最佳缩放比例的设计。已经发现,在涡流探测器中的2:1收缩会在水力旋流器的锥形部分中引起四个截然不同的同时逆流。此外,对于低背压操作(<2 psig),在水力旋流器的上部检测到一个回流区,其中有多达六个反向流。对于某些水力旋流器设计和操作条件,从顶点区域到涡流收集器在轴上发生喷射状流动。这种现象部分解释了为什么Rietema的设计标准是最佳的。测得的切向速度分布与轴向位置无关,并且分别在内部和外部区域显示出特征性的“强迫”和“自由”涡旋行为。添加100 wppm Separan AP-30会降低切向速度,并减小核心区域中反向流动的幅度。对于所研究的水力旋流器,从零到无穷大的分流比和150-500 cm('2)/ sec的进给速度对涡旋直径((TURNEQ)3 mm)和零轴向速度的圆锥轨迹几乎没有影响。外流域。

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