Carbon Dioxide Absorption into Aqueous Blends of Methyldiethanolamine (MDEA) and Alkyl Amines Containing Multiple Amino Groups
Song Yi Choi, Sung Chan Nam, Yeo Il Yoon, Ki Tae Park, So-Jin Park
Abstract
Song Yi Choi, Sung Chan Nam, Yeo Il Yoon, Ki Tae Park, So-Jin Park
Abstract
Alkyl amines, which have multiple amino groups, are used as activators to improve the CO 2 absorption performances of aqueous methyldiethanolamine (MDEA) solutions. The aqueous MDEA blends consisted of 20% (w/w) of MDEA and 10% (w/w) of activators, which are 3-methylamino propylamine (MAPA), diethylenetriamine (DETA), triethylene tetramine (TETA), and tetraethylenepentamine (TEPA). Aqueous solutions of monoethanolamine (MEA; 30% (w/w)) and MDEA (30% (w/w)) are used as reference absorbents for comparison. The CO 2 absorption performances of aqueous MDEA blends were investigated by measurements of absorption capacities, absorption rates, and heats of absorption. The MDEA blends have higher CO 2 absorption capacities than MEA and MDEA. MDEA/TEPA shows the highest CO 2 loading amount of 0.753 mol-CO 2 ·mol-absorbent –1 at 313 K. In addition, the MDEA blends show high cyclic capacities (0.241–0.330 mol-CO 2 ·mol-absorbent –1 ), the values of which are about 3 times higher than that of MEA. All MDEA blends show higher absorption fluxes than MDEA. The MDEA/MAPA showed the highest overall mass transfer coefficient of 3.351 × 10 3 mol·m –2 ·s –1 ·kPa –1, 8 times higher than that of MDEA (0.451 × 10 3 mol·m –2 ·s –1 ·kPa –1 ) and even higher than that of MEA (3.014 × 10 3 mol·m –2 ·s –1 ·kPa –1 ). The heats of absorption of the MDEA blends (57.21–59.53 kJ·mol-CO 2 –1 ) are about 30% higher than that of MDEA and about 30% lower than that of MEA.
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Alkyl amines, which have multiple amino groups, are used as activators to improve the CO 2 absorption performances of aqueous methyldiethanolamine (MDEA) solutions. The aqueous MDEA blends consisted of 20% (w/w) of MDEA and 10% (w/w) of activators, which are 3-methylamino propylamine (MAPA), diethylenetriamine (DETA), triethylene tetramine (TETA), and tetraethylenepentamine (TEPA). Aqueous solutions of monoethanolamine (MEA; 30% (w/w)) and MDEA (30% (w/w)) are used as reference absorbents for comparison. The CO 2 absorption performances of aqueous MDEA blends were investigated by measurements of absorption capacities, absorption rates, and heats of absorption. The MDEA blends have higher CO 2 absorption capacities than MEA and MDEA. MDEA/TEPA shows the highest CO 2 loading amount of 0.753 mol-CO 2 ·mol-absorbent –1 at 313 K. In addition, the MDEA blends show high cyclic capacities (0.241–0.330 mol-CO 2 ·mol-absorbent –1 ), the values of which are about 3 times higher than that of MEA. All MDEA blends show higher absorption fluxes than MDEA. The MDEA/MAPA showed the highest overall mass transfer coefficient of 3.351 × 10 3 mol·m –2 ·s –1 ·kPa –1, 8 times higher than that of MDEA (0.451 × 10 3 mol·m –2 ·s –1 ·kPa –1 ) and even higher than that of MEA (3.014 × 10 3 mol·m –2 ·s –1 ·kPa –1 ). The heats of absorption of the MDEA blends (57.21–59.53 kJ·mol-CO 2 –1 ) are about 30% higher than that of MDEA and about 30% lower than that of MEA.
Key concepts: Aqueous solution, Absorption (acoustics), Chemistry, Alkyl, Propylamine, Diethylenetriamine, Triethylenetetramine, Sorption