Abstract The effect of the side chain structure and the number of hydroxyl groups in primary, secondary and tertiary amines on CO 2 absorption and desorption kinetics, equilibrium loading, heat… Click to show full abstract
Abstract The effect of the side chain structure and the number of hydroxyl groups in primary, secondary and tertiary amines on CO 2 absorption and desorption kinetics, equilibrium loading, heat duty, cyclic capacity, heat of absorption and pKa were studied and used to develop rational criteria for selecting components to formulate an optimum amine blend. Based on the criteria, amines that had a combination of high absorption parameter and high desorption parameter were selected. Their mixing ratios and concentrations were varied to obtain the best overall performance. The results of this study showed that, in comparison with their straight-chain analogues, steric hindrance present in branched-chain alkanolamines resulted in much faster desorption rate, higher solubility CO 2 and cyclic capacity, and much lower heat duty for solvent regeneration, but just a slight decrease in CO 2 absorption rate. The developed criteria resulted in formulating an excellent bi-solvent aqueous amine blend (comprising 2 M BEA + 2 M AMP), which was shown to have an outstanding desorption characteristics/heat duty as well as very good absorption characteristics. In addition, this work developed a new non-trial-and-error procedure to determine the heat of CO 2 absorption based on Gibbs-Helmholtz equation. Furthermore, this work showed that the CO 2 absorption rate and the heat of CO 2 absorption may not necessarily be proportional to the heat of absorption and heat duty, respectively. Both these relations were shown to be strong functions of the amine structure.
               
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