Design of a bench scale unit for continuous CO2 capture via temperature swing adsorption-Fluid-dynamic feasibility study

- A multi-stage fluidized bed system for continuous CO2 separation is introduced.
- The fluid-dynamic feasibility of the system is studied in a cold flow model.
- The impact of the main operating parameters on the solids distribution is studied.
- The dense phase height of top stages is assessed for different solids flow rates.