In this study, the regeneration procedure
of CO2-laden
amine-based solid sorbents in the regenerator fluidized bed was investigated.
The Eulerian–Eulerian two fluid model is used to conduct two-dimensional
Computational Fluid Dynamics (CFD) simulation of the regeneration
section of a circulating fluidized bed carbon capture unit, based
on the National Energy Technology Laboratory (NETL) setup. A two-dimensional
reactive CFD model was used to simulate the extent of CO2 desorption from carbonated amine-based solid sorbents. The carbonated
solid sorbents were up to 73% regenerated in this regeneration system.
The effect of the regenerator’s different configuration on
the carbon dioxide concentration at exiting gas flow was investigated.
Results showed that extension of the fluidized bed height and providing
heat to the system through heating coils could increase the carbon
dioxide concentration in the exiting gas flow up to 40%. Our reacting
CFD numerical model also compared well with the experimental data
on the regeneration efficiency and the pressure profile of the regenerator.