In this Letter, the 2-dimensional dense flow of polygonal particles on an incline with a flat frictional inferior boundary is analyzed by means of contact dynamics discrete element simulations, in order to develop boundary conditions for continuum models of dense granular flows. We show the evidence that the global slip phenomenon deviates significantly from simple sliding: a finite slip velocity is generally found for shear forces lower than the sliding threshold for particle-wall contacts. We determined simple scaling laws for the dependence of the slip velocity on shear rate, normal and shear stresses, and material parameters. The importance of a correct determination of the slip at the base of the incline, which is crucial for the calculation of flow rates, is discussed in relation to natural flows.PACS numbers: 47.57. Gc, 83.80.Fg Despite the large number of studies devoted to understanding the rheology of dense granular flows, the boundary behavior -i.e. the interaction of an ensemble of flowing particles with a wall -is still poorly understood. The issue is relevant for nearly all the situations in which granular materials are processed (silo or chute flows, sampling, die filling and compression) or are observed in nature (avalanches, landslides). A complete understanding of the boundary behavior requires us to study the relationships among the amount of wall slip, stresses and deformation rates in the material, possibly arriving at a quantitative average characterization to be used for characterization and for continuum modeling. This was extensively done with respect to rapid, dilute granular flows [1][2][3], but the results from those analyses cannot be applied to dense, slow flows of granular materials since the phenomenology is largely different. Longlasting contacts, dynamics of force chain networks, and dissipation mainly due to friction are the most significant distinctions between dense and collisional flow regimes. From the practical point of view, in the dense flow of granular materials in silos and hoppers, wall friction is usually described by means of the effective wall friction coefficient µ w = σT σN , which is a bulk, not a particle property, where σ T is the shear stress and σ N is the normal stress in the direction perpendicular to the wall. Such a coefficient, often presented as the angle of wall friction (defined as tan −1 µ w ), is not necessarily a constant property of the couple of particle and wall materials [4,5]. In presence of shear, in a recent work we argued [5] that shear-induced fluctuations of the force network could determine a dependence of the effective wall friction coefficient on flow properties, such as slip velocity, shear rate and stresses. The main point of the theory is that the stronger the phenomenon of force chains breaking and forming in the material, the larger will be the deviation from the condition of steady sliding for the particles at a boundary, implying generally that µ w < µ pw , where µ pw is the particle-wall friction coefficient, and suggesting...