2017 Annual Meeting
(510a) A Multi-Phase Continuum Approach to Modeling the Performance of a Fluidized Bed Nuclear Reactor
Authors
Fluidized beds are currently used extensively in the petrochemical and pharmaceutical industries and there is extensive chemical engineering modeling work on the steady state and time-dependent hydrodynamics of gas- and liquid-fluidized beds with one particle species (see Jackson, 2000). However, models incorporating particle size and density distributions have been examined to a much lesser extent. This work considers a multiphase approach which makes use of volume-averaged mass and momentum balances for the fluid and particle phases independently and generalizes the monocomponent equations proposed by Anderson & Jackson (1967). The model consists of a multi-solid mixture of fluidized particles consisting of N particle species that mimics the particle size and/or density distribution of the TRISO fuel particles. The linear stability of the fluidized reactor core will be examined using hydrodynamic stability theory and a multi-fluid continuum approach to determine if and when the fluidized reactor core becomes hydrodynamically unstable. A reactor model, consisting of the proposed multi-phase continuum model along with a thermal hydraulics model and a neutron kinetics model, can be combined to investigate the dynamic stability of the reactor and the relationship between the expanded reactor core height, core neutronics, reactivity and coolant mass flowrate.