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Computational simulation of mixing flow of shear thinning non-Newtonian fluids with various impellers in a stirred tank

机译:搅拌罐中剪切稀化非牛顿流体与各种叶轮混合流的计算模拟

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摘要

The main features of the flow generated by three axial flow impellers installed on the side of cylindrical tanks filled with pseudoplastic solutions exhibiting yield stress were exposed using computational fluid dynamics (CFD). The numerical results were evaluated using velocity vector maps obtained from particle image velocimetry (PIV) experiments. The models were able to predict macroscale flow structures and global mixing parameters under different operating conditions. However, limitations of the model to predict the symmetric flow observed during the experiments were identified at high rotational speeds. The operating conditions included angular speeds from 327 rpm to 684 rpm, and yield stresses and viscosity levels provided by three carbopol solutions (0.075, 0.09 and 0.1 w/w%). These conditions create mainly laminar flow inside the mixing domain. The results indicated that the operating conditions and the blade angle establish the structure of the impeller discharge, which in turn defines the shear rate distribution, some physical cavern properties, and the formation of segregated regions. (C) 2015 Elsevier B.V. All rights reserved.
机译:使用计算流体力学(CFD)揭示了三个轴向叶轮产生的流量的主要特征,这些轴向叶轮安装在装有屈服应力的假塑性溶液填充的圆柱罐侧面。使用从粒子图像测速(PIV)实验获得的速度矢量图评估了数值结果。该模型能够预测不同操作条件下的宏观流动结构和整体混合参数。然而,在高转速下,模型的局限性在于预测实验期间观察到的对称流动。操作条件包括从327 rpm到684 rpm的角速度,以及三种卡波姆溶液(0.075、0.09和0.1 w / w%)提供的屈服应力和粘度水平。这些条件主要在混合区域内产生层流。结果表明,工作条件和叶片角度确定了叶轮排放的结构,进而确定了剪切速率分布,某些物理洞穴性质和隔离区域的形成。 (C)2015 Elsevier B.V.保留所有权利。

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