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Particle Distribution Studies in Highly Concentrated Solid-Liquid Flows in Pipe using the Mixture Model

机译:使用混合物模型在管中高度浓缩固液流动的颗粒分布研究

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The hydraulic conveying of solid-liquid concentrated suspensions in pipelines corresponds to complex flows where particles with different sizes, concentrations and flow velocities exhibit different flow regimens. Predicting their behavior is fundamental for the adequate design of pumping equipment and flow rigs. In traditional numerical approaches the turbulence production is assumed to be directly dependent on the increase of the particle size; this contradicts data from the literature where small particles cause an augmentation of turbulence and medium size particles attenuate turbulence. Also, in the traditional approach the same drag correlation is assumed to account for particle-fluid interaction in different flow regimes, which, in the case of turbulence augmentation and attenuation can differ considerably. In the present work numerical studies were conducted to simulate highly concentrated flows of settling medium sized particles using a Mixture Model, incorporating a Low Reynolds turbulence closure and a Schiller-Naumann drag correlation to depict the flow of concentrated solid-liquid suspensions. Since not all particle distributions were accurately portrayed, different drag correlations were implemented to provide a more adequate representation of the relative velocity between phases and particle distributions. Amongst the drag correlations implemented the Schiller & Naumann showed the best agreement for the highest particle concentrations at intermediate velocities, whilst the Haider & Levenspiel displayed the best fit with the experimental data for the highest flow velocities and particle concentrations. The Gidaspow-Schiller-Naumann drag correlation was more adequate for low flow velocities and with intermediate particle concentrations. With this work it is shown that using the same drag correlation for the numerical description of experimental data for highly concentrated settling solid-liquid flows does not adequately reproduce the different flow regimes.
机译:固 - 液浓缩悬浮液的管道中对应的液压输送到复杂的流动,其中具有不同大小,浓度和流速颗粒表现出不同的流动方案。预测他们的行为是抽水设备和流量钻机的适当的设计基础。在传统的数值接近湍流的生产被认为是直接取决于粒径的增加;从文献中这一点与数据,其中小颗粒造成的湍流和中等尺寸的颗粒的增强衰减的湍流。此外,在传统的方法相同的阻力相关假定帐户在不同流态,这在湍流增加和衰减的情况下,可以显着不同颗粒的流体相互作用。在目前的工作进行了数值研究,以模拟沉降介质使用混合模型,结合有低雷诺数湍流闭合和席勒瑙曼拖动相关性来描绘浓度固体 - 液体悬浮液的流动大小的颗粒的高度集中的流动。由于不是所有的颗粒分布进行精确地画出,不同阻力相关性进行实施以提供相和颗粒分布之间的相对速度的更充分的代表。之间的相关性的阻力实现的席勒&瑙曼显示在中间速度的最高的粒子浓度的最佳协议,而海德尔&Levenspiel显示的最佳拟合与最高流速和颗粒浓度的实验数据。所述Gidaspow-席勒瑙曼拖动相关性为低流速,并与中间颗粒浓度更充足。与此工作,示出了使用用于高度浓缩的沉淀的固液流的实验数据的数值描述相同的拖动相关并不充分再现不同的流动方式。

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