Abstract
This article is devoted to the study of granular flow regimes undergoing shear in a parallel-plate configuration with particular interest in granule dispersion. Both experimental and numerical investigations are carried out. Experimental investigations are conducted in a shear cell consisting of two parallel discs that contain the granular media. One disc is fixed, whereas the other rotates to shear the media. A normal force is imposed, and the gap is measured. Numerical investigations are based on simulations that use discrete element method (DEM), which allows local investigation of the flow across the gap. This article focuses on the effect of a mixture of size to the flow regime observed when shear velocity increases. The imposed loads on the granular media are weak, and thus, it is expected that the granular regime will pass from a quasi-static regime to a kinetic one. It is found that the granule mixture has a major influence on the normal displacement (lift) between the discs, whereas the effect on the measured friction coefficient is less pronounced. Numerical investigations are in agreement with experimental measurements, provided that the important parameters such as the local contact condition,
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