![]() The calculations were carried out for varying lean loading (0.375–0.425 mol CO 2/mol MEA), solvent to flue gases ratio (4.46–6.92 kg/kg) and CO 2 content (8–16%), with the results showing reasonable absorber behavior and satisfactory consistency with experimental data. A 2-fluid Eulerian model has been employed to resolve the flow in a random packed bed. A 30% aqueous monoethanolamine (MEA) solution was employed as a chemical solvent. A Computational Fluid Dynamics (CFD) model simulates a small laboratory test rig which has provided the reference data for model validation. The complex flow system including multi-phase gas-liquid countercurrent streams with chemical reaction and heat transfer is considered to resolve the CO 2 absorption. ![]() the first stage of a post-combustion capture installation. The paper deals with the numerical modeling of CO 2 removal from flue gases by amine solvent in an absorber column, i.e. ![]()
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