The CO2 reduction process for three absorbents, such as (MEA (monoethanolamine), M-H amine solution, and T-D amine solution), were simulated in the same operating conditions. The simulation results included CO 2 recovery rate and CO2 mole fraction in CO2 rich gas of each absorbent. While the MEA and the M-H solution showed almost perfect CO2 recovery rate, CO2 recovery rate of the T-D solution was only 90%. It was also shown that whn the reboiler duty is changed 623MJ/h into 600MJ/h, about 2% in CO2 recovery rate of the M-H solution is increased and the energy consumption is decreased simultaneously.
|Number of pages||7|
|Publication status||Published - 2004|
|Event||2004 AIChE Annual Meeting - Austin, TX, United States|
Duration: 2004 Nov 7 → 2004 Nov 12
|Other||2004 AIChE Annual Meeting|
|Period||04/11/7 → 04/11/12|
All Science Journal Classification (ASJC) codes