Simulating the Dynamics of Spouted‐Bed Nuclear Fuel Coaters

We describe simulation studies of the dynamics of spouted beds used for CVD coating of nuclear fuel particles. Our principal modeling tool is the Multiphase Flow with Interphase eXchanges (MFIX) code that was originally developed by the National Energy Technology Laboratory (NETL) for fossil energy process applications. In addition to standard MFIX features that allow coupling of transient hydrodynamics, heat and mass transfer, and chemical kinetics, we employ special post-processing tools to track particle mixing and circulation as functions of operating conditions and bed design. We describe in detail one major feature of the dynamics, which is the occurrence of very regular spontaneous pulsations of gas and particle flow in the spout. These pulsations appear to be critically linked to the entrainment and circulation of solids, and they produce readily accessible dynamic pressure variations that can be used for direct comparisons of model predictions with experiments. Spouted-bed dynamics are important from a CVD perspective because they directly determine the magnitude and variability of the concentration and species gradients in the zone where reactant gases first come into contact with hot particles. As this unsteady spouted-bed environment differs from other types of CVD reactors, the design and scale-up of such reactorsmore » is likely to involve unique modeling issues. Our primary goal here is to lay the groundwork for how computational simulation can be used to address these modeling issues in the specific context of nuclear fuel particle coating.« less

[1]  Francine Battaglia,et al.  Simulations of multiphase reactive flows in fluidized beds using in situ adaptive tabulation , 2004 .

[2]  T. Laurell,et al.  A new device for coating single particles under controlled conditions , 2005 .

[3]  Piotr Wnukowski,et al.  Modelling of the three-domain fluidized-bed particulate coating process , 1997 .

[4]  S. Savage,et al.  Analyses of slow high-concentration flows of granular materials , 1998, Journal of Fluid Mechanics.

[5]  Zhimao Yang,et al.  The coating process of silica film on TiH2 particles and gas release characteristic , 2005 .

[6]  M. Syamlal,et al.  Fluid dynamic simulation of O3 decomposition in a bubbling fluidized bed , 2003 .

[7]  David G. Schaeffer,et al.  Instability in the evolution equations describing incompressible granular flow , 1987 .

[8]  Fredrik Setterwall,et al.  The coating of particles in a fluidized bed (residence time distribution in a system of two coupled perfect mixers) , 1989 .

[9]  D. Gunn Transfer of heat or mass to particles in fixed and fluidised beds , 1978 .

[10]  G. Jellison,et al.  Optical Characterization of Tristructural Isotropic Fuel Particle Cross-Sections Using Generalized Ellipsometry , 2006 .

[11]  Cor M. van den Bleek,et al.  Response characteristics of probe-transducer systems for pressure measurements in gas-solid fluidized beds: how to prevent pitfalls in dynamic pressure measurements , 1999 .

[12]  D. Jeffrey,et al.  Kinetic theories for granular flow: inelastic particles in Couette flow and slightly inelastic particles in a general flowfield , 1984, Journal of Fluid Mechanics.

[13]  M. Syamlal,et al.  MFIX documentation theory guide , 1993 .

[14]  Yulong Ding,et al.  Positron emission particle tracking studies of a wurster process for coating applications , 2003 .