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SAMSI Workshop on Fluctuations and continuum Equations for Granular flow , April 16-17, 2004. Granular flow in silos - observations and comments. Jørgen Nielsen Danish Building and Urban Research Jn@dbur.dk. Silo versus hydrostatic pressure. Focus on understanding phenomena.
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SAMSI Workshop onFluctuations and continuum Equations for Granular flow, April 16-17, 2004 Granular flow in silos - observations and comments Jørgen Nielsen Danish Building and Urban Research Jn@dbur.dk
Focus on understanding phenomena • Observations from silo tests • Comments related to • Physical and mathematical modelling – Continuum / discrete particles • Phenomena observed in silos • Stochastic approach
Physical modelling versus mathematical modelling • Mathematical modelling is needed to generalise our understanding of physical phenomena and to predict behaviour under specified circumstances • Physical modelling is wanted for controlled experiments in order to systematically observe and explore phenomena as a basis for mathematical modelling - and to verify such models
A good scientific physical model is more than just a small scale structure The creation of a model law calls for some considerations: • Which phenomena to cover? • Discrete particles or continuum approach? • Which mathematical model to be based on? – Must be precisely formulated, but you may not be able to solve the equations Leads to the model law: Model Requirements and a Scaling Law Ref: J. Nielsen ”Model laws for granular media and powders with special view to silo models”, Archives of Mechanics, 29, 4, pp 547-560, Warzawa, 1977
Model requirements Kx (scaled particles) Kg = 1/ Kx (centrifuge) …….. Scaling law K = 1 K = 1 Kt = Kx (Forces of inertia) Kt = 1 (Time dep. Konst. rel.) Kt = 1 (Pore flow) Model law – discrete, particles
Outcomes of filling from the stacking process • Density • Pore pressure • Homogeneity • Anisotropy - and thus strength, stiffness and rupture mode of the ensiled solids
Relative standard deviation Test Diameter of particle Pressure cell diameter Surface area of pressure cell From contact forces to pressure
Circumferential distribution of maximum discharge pressures – Wheat, eccentric inlet and outlet
Circumferential distribution of maximum discharge pressures – Barley, eccentric inlet and outlet
Rotational symmetrical pressure distribution – almost(Jørgen Munch-Andersen)
On the search of a suitable model for the stress-strain relationship in granular materials
The modelling challenges P.S. Time dependent material behaviour may cause scale errors
A ”friendly” silo problem - may be characterised by: • A non-cohesive powder • Aerated filling • Low wall friction • Mass flow
A ”bad” silo problem - may be characterised by: • Coarse-grained sticky particles • Eccentric filling • High wall friction • Pipe flow expanding upwards until the full cross section has become involved
Items for a stochastic/statistic treatment • Redistribution of pressure due to imperfections of wall geometry • The value of material parameters for the (future) stored material • The wall friction coefficient • The formation of unsymmetrical flow patterns in symmetrical silos – and their load implications • Wall pressure fluctuations - load redistributions • The formation of rupture planes in dense materials