In the final phase of particle drying in a spouted bed,
the drying
rate is governed by intraparticle heat and mass diffusion. Coupled
computational fluid dynamics and the discrete element method (CFD-DEM)
have proven to be suitable tools for modeling gas–solid in
a spouted bed. However, existing CFD-DEM models are primarily employed
to calculate the interphase heat and mass transfer rates based on
an assumption of uniform intraparticle temperature and moisture distributions.
Alternatively, some models take into account only the evaporation
on the surface of the particles. As a result, these models may not
reasonably represent the final phase of particle drying. This study
introduces a novel CFD-DEM model for spouted bed drying that incorporates
intraparticle heat and mass diffusion. The model combines the CFD-DEM
governing equations with two one-dimensional intraparticle heat and
mass diffusion equations. Benchmark cases using a spouted bed are
presented to demonstrate the feasibility of the proposed model. The
results indicate that the CFD-DEM model effectively reproduces the
rational heat and mass transfer laws of the spouted bed particle drying
process characterized by an overall decline in transfer rates. Furthermore,
the model provides valuable insights into the temperature and moisture
distributions within the particles. The proposed model exhibits great
potential for extension to real-world industrial applications, encompassing
complex heat and mass diffusion phenomena as well as coupling characteristics.