Article ID Journal Published Year Pages File Type
1514985 Energy Procedia 2011 8 Pages PDF
Abstract

CO2 solubility in an aqueous tertiary amine solution was measured, and thermodynamic models Kent-Eisenberg and Clegg-Pitzer were used to correlate CO2 solubility. Process simulation was also carried out with these models, and simulation results are compared with pilot plant measurement data. The results show that the mixed amine solution of the tertiary amine with MEA could save regeneration energy about 20% compared with 30% MEA aqueous solution.

Related Topics
Physical Sciences and Engineering Energy Energy (General)