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The aim of the present work was to characterize and study the mass transfer process of the CO2 absorption into single and blended alkanolamines in a packed column under atmospheric pressure. For this purpose, two systems were built, one of the columns is a laboratory structure packed column and the other is a pilot random packed column. The absorption of CO2 into NaOH was performed to determine the effective mass-transfer area and the overall mass-transfer coefficient. The absorption performance was evaluated in terms of the overall mass-transfer coefficient for the absorption of CO2 in air into single and blended alkanolamines: MEA 25% wt, and MEA-MDEA mixtures, MEA-MDEA (25% /5% wt), MEA-MDEA (20% /10% wt) and MEA-MDEA (15% /15% wt). The CO2 absorption performance of MEA-MDEA mixture has a high correlation with the proportion MEA-MDEA. Experimental series were designed employing a process simulator for the hydrodynamic checking and determination of gas and liq flow rates. Comparison of the experimental data and simulation results was made for the absorption into MEA.

Estudo do processo de absorção de CO2 em soluções de aminas empregando-se coluna recheada.