One of the most pressing challenges facing the energy sector is the urgent need to reduce anthropogenic CO2 emissions while simultaneously meeting the increasing energy demands of a growing global population. Among the various strategies to mitigate point-source CO2 emissions, post-combustion carbon capture stands out as one of the most straightforward and widely applicable methods. This study focused on modeling a fixed bed reactor utilizing K2CO3-doped Li4SiO4 porous pellets as the adsorbent material. The pellets were tested in a lab-scale fixed bed reactor under conditions simulating the exhaust gases of power plants, specifically at a low CO2 concentration (4 vol%) and an adsorption temperature of 515 °C. A one-dimensional model was developed using COMSOL Multiphysics® to simulate the CO2 adsorption process within the pellet bed. The model incorporated modified shrinking core reaction kinetics, which accounted for the presence of a molten carbonate mixture and a nucleation phase to capture the adsorption process accurately. Simulation results showed good agreement with the experimental data, confirming the model’s ability to predict the adsorption performance under the specified conditions.
CO2 Capture in a Fixed Bed Reactor: Experimental and Simulation Study of Adsorption Process Using Li4SiO4-based Sorbents
Stefanelli EleonoraPrimo
;Francalanci FlavioSecondo
;Vitolo Sandra;Puccini Monica
Ultimo
2025-01-01
Abstract
One of the most pressing challenges facing the energy sector is the urgent need to reduce anthropogenic CO2 emissions while simultaneously meeting the increasing energy demands of a growing global population. Among the various strategies to mitigate point-source CO2 emissions, post-combustion carbon capture stands out as one of the most straightforward and widely applicable methods. This study focused on modeling a fixed bed reactor utilizing K2CO3-doped Li4SiO4 porous pellets as the adsorbent material. The pellets were tested in a lab-scale fixed bed reactor under conditions simulating the exhaust gases of power plants, specifically at a low CO2 concentration (4 vol%) and an adsorption temperature of 515 °C. A one-dimensional model was developed using COMSOL Multiphysics® to simulate the CO2 adsorption process within the pellet bed. The model incorporated modified shrinking core reaction kinetics, which accounted for the presence of a molten carbonate mixture and a nucleation phase to capture the adsorption process accurately. Simulation results showed good agreement with the experimental data, confirming the model’s ability to predict the adsorption performance under the specified conditions.I documenti in IRIS sono protetti da copyright e tutti i diritti sono riservati, salvo diversa indicazione.


