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A numerical model for catalyst-aided carbon dioxide (CO2) desorption from CO2-loaded aqueous amines solution has been developed. The model includes a hot water-heater and considers phase separation at the top of the desorption column. The model was validated with experimental data obtained from an integrated CO2 capture pilot plant which used 5M monoethanolamine (MEA) solution with two industrial...
A mathematical model for low temperature catalyst-aided CO2 desorption from loaded amines has been developed and validated against experimental data obtained from an integrated pilot plant utilizing blended 5M/2M MEA-MDEA using two industrial catalysts, namely, HZSM-5 and γ-Al2O3. The rigorous model considers the presence of electrolytes and both the physical and chemical contribution of the catalyst...
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