CO 2 capture solvent selection by combined absorption–desorption analysis

Abstract

A method was developed for selection of promising solvents based on CO 2 absorption experiments at 40 °C and 9.5 kPa CO 2 partial pressure followed by desorption of the same solvents at 80 °C down to 1.0 kPa CO 2 partial pressure. Experiments conducted on 13 solvent systems under atmospheric conditions revealed the solvents absorption and desorption characteristics and these were compared with 1.0 M, 2.5 M, 5.0 M and 10.0 M MEA. Results showed that absorption or stripping data alone were not sufficient in making robust solvent selection decisions, and that combined data analysis was necessary. 1.0 M tetraethylenepentamine (TEPA) and 5.0 M MEA showed the best performance in terms of absorption rate. 1.5 M Bis-(3-dimethylaminopropyl) amine (TMBPA) was easy to desorb, has high absorption capacity; and when promoted it showed the best performance in terms of CO 2 carrying capacity. At the test conditions, 1.5 M TMBPA promoted with 1.0 M PZ showed the best potential for efficient CO 2 removal at reduced cost of all systems tested. Its cyclic capacity in mol CO 2/mol amine was found to be 70% higher than that of 5 M MEA.