This preliminary program is subject to change.

Important Length Scales in Dense Gas-Particle Flows

Stefan Radl1, Chris Milioli2, Fernando Milioli2 and Sankaran Sundaresan3, (1)Institute for Process and Particle Engineering, Graz University of Technology, Graz, Austria, (2)Mechanical Engineering, University of Sao Paulo, São Carlos-SP, Brazil, (3)Department of Chemical and Biological Engineering, Princeton University, Princeton, NJ

There is a long history of studies on application of dimensional analysis to develop scaling relations that can be employed for scale-up and scale-down of gas-particle fluidized beds. It is now well established that two-fluid models (TFM), with constitutive models for the stresses deduced from the kinetic theory of granular materials, are able to capture the formation inhomogeneous structures over a wide range of time and length scales. As resolving all these structures in simulations of industrial scale devices is impractical, filtered models that average over small-scale structures are currently being developed. This has brought to the surface the issue of relevant length scales in gas-particle flows.

In this talk, we will review the various length scales that naturally enter in gas-particle fluidized beds and discuss how an understanding of these scales is being used to construct simplified filtered models. A dimensional analysis of these filtered models then suggests a simple set of dimensionless groups that are important to capture the dynamics of such devices when simulated on coarse computational grids. Finally, we present simulation results, using both a TFM and an Euler-Langrange model, which support our choice of dimensionless parameters.

 


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