首页> 外文期刊>Powder Technology: An International Journal on the Science and Technology of Wet and Dry Particulate Systems >Blade-granule bed stress in a cylindrical high shear granulator: Further characterisation using DEM
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Blade-granule bed stress in a cylindrical high shear granulator: Further characterisation using DEM

机译:圆柱形高剪切造粒机中的叶片颗粒床应力:使用DEM进行进一步表征

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摘要

In high shear granulation, the rotating impeller blades impart forces on the granules which are subsequently transmitted throughout the bed through inter-granule collisions. These affect the granule growth behaviour in several ways the granules could deform, consolidate and/or break under stress. In this paper, the blade granule bed normal stress in a cylindrical, vertical axis high shear granulator is characterised using Discrete Element Method (DEM) simulations. The simulations are compared and validated with the measured blade bed stress and bed surface velocities from our previous studies [1,2]. The blade-bed stresses were previously measured using a novel, custom-built telemetric impeller pressure sensor system. Following experimental validation for impeller speeds up to 350 rpm, higher impeller speeds up to 700 rpm or Fr = 3.88 are simulated to include flow regimes that can occur in most commercial granulators. Parameter study of particle properties, impeller geometries and granulator scales is also carried out. In our previous work, a blade-bed stress equation based on the blade and granule bed inertial forces with a correction factor, B-1 = K-1 1/v(rel), to account for bed fluidisation with increasing impeller speed, was proposed and validated with a range of dry granules [1]. Here, an improved correction factor, B-2 =K-2 1/Fr-rel(0.5) (2h(w)/D)(0.3) theta(-0.5) is introduced to account for different granulator scales, blade widths and blade angles, with a fitted constant K-2. (C) 2016 Elsevier B.V. All rights reserved.
机译:在高剪切造粒中,旋转的叶轮叶片将力施加到颗粒上,随后通过颗粒间碰撞将力传递到整个床层上。这些以多种方式影响颗粒在应力下的变形,固结和/或破裂。在本文中,使用离散元方法(DEM)模拟来表征圆柱形,垂直轴高剪切造粒机中的叶片颗粒床正应力。仿真结果与我们以前的研究中测得的叶片床应力和床表面速度进行了比较和验证[1,2]。之前使用新型定制的遥测叶轮压力传感器系统测量了叶片床应力。在对最高350 rpm的叶轮速度进行实验验证之后,对最高700 rpm或Fr = 3.88的较高叶轮速度进行了模拟,以包括大多数商用制粒机中可能发生的流动状态。还对颗粒性质,叶轮几何形状和制粒机鳞片进行了参数研究。在我们先前的工作中,基于叶片和颗粒床惯性力的修正系数为B-1 = K-1 1 / v(rel)的叶片床应力方程式是随着叶轮速度的增加而考虑床层流化的。提出并用一系列干燥颗粒进行了验证[1]。在这里,引入了改进的校正因子B-2 = K-2 1 / Fr-rel(0.5)(2h(w)/ D)(0.3)theta(-0.5)来解决不同的制粒机规模,叶片宽度和叶片角,安装常数K-2。 (C)2016 Elsevier B.V.保留所有权利。

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