2002
DOI: 10.1017/s0022112001006796
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Friction law for dense granular flows: application to the motion of a mass down a rough inclined plane

Abstract: The problem of the spreading of a granular mass released at the top of a rough inclined plane was investigated. We experimentally measure the evolution of the avalanche from the initiation up to the deposit using a Moir image processing technique. The results are quantitatively compared with the prediction of an hydrodynamic model based on depth averaged equations. In the model, the interaction between the flowing layer and the rough bottom is described by a non trivial friction force whose expression is deriv… Show more

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Cited by 398 publications
(650 citation statements)
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“…Let us assume that a i is greater than the residual friction angle /, which is consistent with the experimental observations of dry granular flows [30]. The normal stress P i is zero in the critical state of triggering the flow since the flow velocity is almost null at that time point.…”
Section: Introductionsupporting
confidence: 65%
“…Let us assume that a i is greater than the residual friction angle /, which is consistent with the experimental observations of dry granular flows [30]. The normal stress P i is zero in the critical state of triggering the flow since the flow velocity is almost null at that time point.…”
Section: Introductionsupporting
confidence: 65%
“…The depth-averaged equations, introduced by [49] and recently revisited [29,50] in the context of shallow granular flows down an inclined plane, allow us to estimate the effective friction coefficient µ * . The acceleration is balanced by the gravity parallel to the plane, the tangential stress between the fixed bottom and the flowing layer, and a pressure force related to the thickness gradient [29,49,50]. The momentum balance is reduced to the following equation in steady 2D flow conditions:…”
Section: Control Flows Without An Obstaclementioning
confidence: 99%
“…It can be calculated provided an assumption on the shape of the velocity profile: β = 4/3 for linear velocity profiles and β = 5/4 for Bagnold velocity profiles [51]. The k factor, in the thickness gradient term, is the ratio of the normal stress σ xx to the normal stress σ yy , classically introduced for dense granular flows [49,50].…”
Section: Control Flows Without An Obstaclementioning
confidence: 99%
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“…They found that the volume fraction Φ of the sample is also a function of I but varies only slightly in the dense regime. The inertial number, which is the square root of the Savage number 20 or of the Coulomb number 21 17,22 , it can be shown that the friction coefficient µ(I ) has the shape given in Fig. 1.…”
mentioning
confidence: 99%