论文标题
叶轮和杯流变仪的屈服和粘膜流的计算流变计
Computational Rheometry of Yielding and Viscoplastic Flow in Vane-and-Cup Rheometer Fixtures
论文作者
论文摘要
提出了平面二维计算分析,以使传统和分形叶片中的几何形状有资格,以便在有或没有滑移的情况下准确地进行简单的粘质流体的流变。基于自适应增强拉格朗日方案的数值模拟用于研究vane工具内外的屈服压力液的二维流动场,其中n = 3至24臂的趋势范围为bingham数字,b(即,屈服应力比特征性粘性应力的比率)。这允许对具有各种几何形状的叶片周围的速度和应力场进行准确计算,并与通过流变仪测量的输出扭矩的实验观察直接比较,揭示了变化和误差的来源。我们描述了叶片结构对流体速度场的影响,从几臂十字形叶片(n <6)显着扰动从理想的方位角运动学到多臂分形叶片(n> 12)的流动,这些叶片(n> 12)成功地将内部结构特征成功地``clo offercirt)cround。与以前的文献的数据直接比较,与材料流动曲线的数据直接比较,与材料流动的数据直接相比,与流体的环形环不可区分,并导致更精确最后,我们描述了Vane地形和Bingham数字B(B,对``简单''(无弹性)屈服压力流体的测量扭矩和流变准确性的影响。
A planar two-dimensional computational analysis is presented to qualify traditional and fractal vane-in-cup geometries for accurate rheometry of simple viscoplastic fluids with and without slip. Numerical simulations based on an adaptive augmented Lagrangian scheme are used to study the two-dimensional flow field of yield-stress fluids within and around vane tools with N=3 to 24 arms for a wide range of Bingham numbers, B (i.e. the ratio of the yield stress over the characteristic viscous stress). This allows for accurate calculations of the velocity and stress fields around vanes with various geometries, as well as direct comparison to experimental observations of the output torque measured by a rheometer, revealing sources of variation and error. We describe the impact of the vane structure on the fluid velocity field, from few-arm cruciform vanes (N < 6) that significantly perturb the flow away from ideal azimuthal kinematics, to many-arm fractal vanes (N > 12) in which the internal structural features are successfully ``cloaked" by a yield surface. This results in the shearing of an almost-circular ring of viscoplastic fluid that is indistinguishable from the annular ring of fluid deformed around a slip-free rotating cylindrical bob and leads to more accurate rheometric measurements of the material flow curve. Moreover, in direct comparison with data from previous literature, we show that slip conditions on the vane surface do not impact the velocity field or measured overall torque T, whereas slip conditions on the smooth outer wall have significant impact on data, even when using a vane geometry. Finally, we describe the impact of vane topography and Bingham number, B, on the measured torque and rheometric accuracy of vane-in-cup geometries for ``simple" (inelastic) yield-stress fluids described by either the Bingham plastic or Herschel-Bulkley constitutive model.