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• W2481036011 abstract "• A CFD absorber model linking flow hydrodynamics with CO 2 absorption was proposed. • Good correspondence between the model and a reference lab installation was found. • A parametric study of the absorber was performed, showing its performance. • Capture efficiency is slightly influenced by varying CO 2 content in flue gases. The paper deals with the numerical modeling of CO 2 removal from flue gases by amine solvent in an absorber column, i.e. the first stage of a post-combustion capture installation. 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. A Computational Fluid Dynamics (CFD) model simulates a small laboratory test rig which has provided the reference data for model validation. A 30% aqueous monoethanolamine (MEA) solution was employed as a chemical solvent. A 2-fluid Eulerian model has been employed to resolve the flow in a random packed bed. 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. It was found that the removal efficiency is weakly dependent on CO 2 content in exhaust gases as long as the amine solution loading is kept at a sufficiently high level." @default.
• W2481036011 created "2016-08-23" @default.
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• W2481036011 date "2016-12-01" @default.
• W2481036011 modified "2023-09-29" @default.
• W2481036011 title "Amine based CO2 capture – CFD simulation of absorber performance" @default.
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• W2481036011 doi "https://doi.org/10.1016/j.apm.2016.07.003" @default.
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