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Experimental and CFD Studies of the Hydrodynamics in Wet Agglomeration Process

机译:湿团聚过程中水动力学的实验和CFD研究

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In this study, an experimentally validated computational model was developed to investigate the hydrodynamics in a rotor-stator vortex agglomeration reactor RVR having a rotating disc at the centre with two shrouded outer plates. A numerical simulation was performed using a simplified form of the reactor geometry to compute the 3-D flow field in batch mode operations. Thereafter, the model was validated using data from a 2-D Particle Image Velocimetry (PIV) flow analysis performed during the design of the reactor. Using different operating speeds, namely 70, 90, 110, and 130 rpm, the flow fields were computed numerically, followed by a comprehensive data analysis. The simulation results showed separated boundary layers on the rotating disc and the stator. The flow field within the reactor was characterized by a rotational plane circular forced vortex flow, in which the streamlines are concentric circles with a rotational vortex. Overall, the results of the numerical simulation demonstrated a fairly good agreement between the Computational Fluid Dynamics (CFD) model and the experimental data, as well as the available theoretical predictions. The swirl ratio β was found to be approximately 0.4044, 0.4038, 0.4044, and 0.4043 for the operating speeds of N = 70, 90, 110, and 130 rpm, respectively. In terms of the spatial distribution, the turbulence intensity and kinetic energy were concentrated on the outer region of the reactor, while the circumferential velocity showed a decreasing intensity towards the shroud. However, a comparison of the CFD and experimental predictions of the tangential velocity and the vorticity amplitude profiles showed that these parameters were under-predicted by the experimental analysis, which could be attributed to some of the experimental limitations rather than the robustness of the CFD model or numerical code.
机译:在这项研究中,建立了一个经过实验验证的计算模型,以研究转子-定子涡流团聚反应器RVR中的流体动力学,该反应器RVR的中心为转盘,带有两个带罩的外板。使用反应器几何形状的简化形式进行了数值模拟,以分批模式运行计算3-D流场。此后,使用来自在反应堆设计期间进行的二维粒子图像测速(PIV)流动分析的数据验证模型。使用不同的运行速度(即70、90、110和130 rpm),对流场进行数值计算,然后进行全面的数据分析。仿真结果表明,转盘和定子上的边界层分开。反应器内的流场的特征在于旋转平面的圆形强制涡流,其中流线是具有旋转涡流的同心圆。总体而言,数值模拟的结果表明计算流体动力学(CFD)模型与实验数据以及可用的理论预测之间具有相当好的一致性。对于N = 70、90、110和130rpm的运行速度,发现涡流比β分别为大约0.4044、0.4038、0.4044和0.4043。就空间分布而言,湍流强度和动能集中在反应堆的外部区域,而圆周速度则朝着罩壳方向减小。但是,通过对CFD以及切线速度和涡度振幅分布的实验预测的比较表明,这些参数是通过实验分析预测不足的,这可能归因于某些实验局限性而非CFD模型的鲁棒性或数字代码。

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