2014Industrial & Engineering Chemistry ResearchRequires access

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

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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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What this paper is about

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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Available 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.

Key concepts: Aqueous solution, Absorption (acoustics), Chemistry, Alkyl, Propylamine, Diethylenetriamine, Triethylenetetramine, Sorption

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Carbon Dioxide Absorption into Aqueous Blends of Methyldiethanolamine (MDEA) and Alkyl Amines Containing Multiple Amino Groups — Research Paper | ScholarLens