Timberlake Brian D, Morris Jeffrey F
School of Chemical Engineering, Georgia Institute of Technology, Atlanta, GA 30332-0100, USA.
Philos Trans A Math Phys Eng Sci. 2003 May 15;361(1806):895-910. doi: 10.1098/rsta.2003.1174.
The film depth of a free-surface suspension flowing in a partially filled horizontal concentric-cylinder, or Couette, device has been studied in order to assess its role in the axial concentration banding observed in this flow. The flow is driven by rotation of the inner cylinder. The banding phenomenon is characterized by particle-rich bands which under flow appear as elevated regions at the free surface separated axially by regions dilute relative to the mean concentration. The concentric cylinders studied had outer radius R(o) = 2.22 cm and inner radii R(i) = 0.64, 0.95 and 1.27 cm; the suspension, of bulk particle volume fraction phi = 0.2 in all experiments described, was composed of particles of either 250-300 microm diameter or less than 106 microm diameter, with the suspending fluid an equal density liquid of viscosity 160 P. The ratio of the maximum to the minimum particle volume fraction along the axis in the segregated condition varies from O(1) to infinite. The latter case implies complete segregation, with bands of clear fluid separating the concentrated bands. The film depth has been varied through variation of the filled fraction, f, of the annular gap between the cylinders and through the rotation rate. Film depth was analysed by edge detection of video images of the free surface under flow, and the time required for band formation was determined for all conditions at which film depth was studied. The film depth increases roughly as the square root of rotation speed for f = 0.5. Band formation is more rapid for thicker films associated with more rapid rotation rates at f = 0.5, whereas slower formation rates are observed with thicker films caused by large f, f > 0.65. It is observed that the film depth over the inner cylinder grows prior to onset of banding, for as yet unknown reasons. A mechanism for segregation of particles and liquid in film flows based upon 'differential drainage' of the particle and liquid phase in the gravity-driven flow within the film over the inner cylinder is formulated to describe the onset of concentration fluctuations. This model predicts that suspension drainage flows lead to growth of fluctuations in phi under regions of negative surface curvature.
为了评估自由表面悬浮液在部分填充的水平同心圆柱(即库埃特)装置中流动时液膜深度在该流动中观察到的轴向浓度条带形成过程中的作用,对其进行了研究。该流动由内圆柱的旋转驱动。条带现象的特征是富含颗粒的条带,在流动状态下,这些条带在自由表面表现为凸起区域,在轴向上被相对于平均浓度较稀的区域分隔开。所研究的同心圆柱的外半径(R(o)=2.22)厘米,内半径(R(i)=0.64)、(0.95)和(1.27)厘米;在所有所述实验中,悬浮液的总体颗粒体积分数(\phi = 0.2),由直径为(250 - 300)微米或小于(106)微米的颗粒组成,悬浮流体为密度相等、粘度为(160)泊的液体。在分离状态下,沿轴的最大颗粒体积分数与最小颗粒体积分数之比从(O(1))变化到无穷大。后一种情况意味着完全分离,清澈流体带将浓缩带分隔开。通过改变圆柱之间环形间隙的填充分数(f)以及旋转速率来改变液膜深度。通过对流动状态下自由表面视频图像进行边缘检测来分析液膜深度,并针对研究液膜深度的所有条件确定条带形成所需的时间。对于(f = 0.5),液膜深度大致随旋转速度的平方根增加。对于(f = 0.5),与较快旋转速率相关的较厚液膜条带形成更快,而对于由大的(f)((f > 0.65))导致的较厚液膜,观察到条带形成速率较慢。可以观察到,在内圆柱上的液膜深度在条带形成开始之前就会增加,原因尚不清楚。基于在内圆柱上方液膜内重力驱动流动中颗粒相和液相的“差异排水”,建立了一个用于描述膜流中颗粒和液体分离的机制,以描述浓度波动的起始。该模型预测,悬浮液排水流动会导致负表面曲率区域下(\phi)波动的增长。