Elastic Granular Flows
Large scale landslide simulations provided the surprising result that the effective friction coefficient (the ratio of shear to normal forces at the base of the slide) increased with the shear rate. This might possibly explain the effect of slide volume on the runout of large landslides, but it also indicates that landslides operated in an entirely new and unexplored flow regime.Previously, granular flows had been divided into (1) the slow, quasistatic regime, in which the effective friction coefficient is taken to be a material property and thus constant, and (2) the fast, rapid-flow regime, where the particles interact collisionally, but which scales in such a way that the effective friction coefficient is independent of the shear rate. Both indicate that the effective friction coefficient is independent of the shear rate. Consequently the landslides operated in a separate intermediate regime.This talk will discuss detailed computer simulation studies into this intermediate regime and into the transitions between regimes. In this way, it is possible to draw the entire flowmap connecting the quasistatic and rapid-flow regimes. The key was to include the elastic properties of the solid material in the set of rheological parameters; in effect this put solid properties into the rheology of granular solids, properties that were unnecessary in previous theories as a result of the plasticity and kinetic theory formalisms on which quasistatic and rapid-flow theories are respectively based. Granular flows are then divided into two broad categories, the Elastic Regimes, in which the particles are locked in force chains and interact elastically over long duration contact with their neighbors and the Inertial regimes, where the particles have broken free of the force chains. The Elastic regimes can be further subdivided into the Elastic-Quasistatic regime (the old quasistatic regime) and the Elastic-Inertial regime. The Elastic-Inertial regime is the new regime observed in the landslide simulations, in which the inertially induced stresses are significant compared to the elastically induced stresses. The Inertial regime can also be sub-divided into an Inertial-Non-Collisional where the stresses scale inertially, but the particles interact through long duration contacts, and the Inertial-Collisional or the old rapid-flow regime.Finally, it will be shown that Stress-Controlled flows are rheologically different from Controlled-Volume flows. Physically, there is a range of dense concentrations (solid volume fractions between 0.5 and 0.6) in which it is possible to form force chains and thus to demonstrate elastically. But there are conditions under which force chains do not form at the same average concentrations. (In other words it is possible for the material to exhibit two different states at the same concentration.) By forcing the material to support an applied loads across force chains, Stress-Controlled flows generally behave elastically through this range of concentrations under the same conditions where Controlled-Volume flows behave inertially.
©2011 Walter de Gruyter GmbH & Co. KG, Berlin/Boston
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- Combined Mechanistic and Empirical Modelling
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- A Mechanistic Model for the Water Gas Shift Reaction Over Commercial Catalysts Containing CuO/ZnO
- Catalytic Pyrolysis of Difluorochloromethane to Produce Tetrafluoroethylene
- Radial Profiles of Particle Velocity in a Large Scale CFB Downer
- Nonlinear Dynamic Analysis of the Local Heat Transfer Rate in Three-Phase Reactors
- Conversion of Synthesis Gas into Light Hydrocarbons. Modelling of the Catalytic Reaction Network
- Influence of the Preparation Method and Metal Precursor Compound on Alumina-Supported Pd Catalysts
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- A Hybrid Methodology For On-Line Process Monitoring
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- Conference Presentation
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- Elastic Granular Flows
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- Review
- Industrial Applications of Reactive Distillation: Recent Trends
- Phase Mixing Modeling in Multiphase Reactors Containing Gas Bubble: a Review.
- Article
- Numerical Aspects of Bubble Column Simulations
- Reactor Operating Strategy and Secondary Nucleation in Emulsion Polymerization
- Combined Mechanistic and Empirical Modelling
- The Catalytic Evaluation of Structured Zeolite Catalysts
- A Mechanistic Model for the Water Gas Shift Reaction Over Commercial Catalysts Containing CuO/ZnO
- Catalytic Pyrolysis of Difluorochloromethane to Produce Tetrafluoroethylene
- Radial Profiles of Particle Velocity in a Large Scale CFB Downer
- Nonlinear Dynamic Analysis of the Local Heat Transfer Rate in Three-Phase Reactors
- Conversion of Synthesis Gas into Light Hydrocarbons. Modelling of the Catalytic Reaction Network
- Influence of the Preparation Method and Metal Precursor Compound on Alumina-Supported Pd Catalysts
- A 3D Model of Combustion in Large-Scale Circulating Fluidized Bed Boilers
- Gas and Solid Mixing in High-Density CFB Risers
- A Local Model for Gas-Liquid Mass Transfer in a Gas-Liquid-Solid Circulating Fluidized Bed
- A Hybrid Methodology For On-Line Process Monitoring
- A Laboratory Steam-Cracking Reactor to Characterize Raw Materials
- Modeling, Simulation and Optimal Control of Ethylene Polymerization in Non-Isothermal, High-Pressure Tubular Reactors
- A Parametric Study of the Oxygen Elimination Process in a Packed Bed
- Flow Generated by Radial Flow Impellers: PIV Measurements and CFD Simulations
- Enhanced Reactor Performance with Pressure and Vacuum Swing Reaction
- Characterization and Selection of Materials for Air Biofiltration in Fluidized Beds
- Control and Optimization of a Three Phase Industrial Hydrogenation Reactor
- Horizontal Penetration of Gas-Liquid Spray Jets in Gas-Solid Fluidized Beds
- Optimization of Flow Shear Stress Through a Network of Capillary Fibers With the Use of CFD
- Oxygen Distribution in Packed Bed Membrane Reactors For Partial Oxidation Systems and its Effect On Product Selectivity
- Wastewater Minimisation Using a Heuristic Procedure
- Characterization of Fluidization Quality in Fluidized Beds of Wet Particles
- Numerical and Experimental Investigations into The Effect of Gap Between Baffle and Wall on Mixing in an Oscillatory Baffled Column
- Alternative Designs for Fixed Bed Catalytic Reactors
- Hydrodynamic and Mass Transfer Parameters in Agitated Reactors Part I: Critical Mixing Speed, Induced Gas Flow Rate, and Wavy Surface in SARs and GIRs
- Application of CFD Modelling Technique in Engineering Calculations of Three-Phase Flow Hydrodynamics in a Jet-Loop Reactor
- 3-D Modeling of Liquid Injection into Fluidized Beds
- Conference Presentation
- Granular Flows and Gas Fluidization
- Elastic Granular Flows
- Multi-fluid CFD modelling of fluidised bed reactors
- Chemical Reaction Engineering, the Environment, Pollution Prevention and Sustainable Development
- Gas-Liquid-Solid Fluidization: Perspectives
- Short Communication or Note
- Catalytic Drying of Digested Sludge
- Enhancement of the Distribution of a Liquid Sprayed Into a Fluidized Bed