Abstract
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.
| Original language | English |
|---|---|
| Pages | 6941-6947 |
| Number of pages | 7 |
| State | Published - 2004 |
| Externally published | Yes |
| Event | 2004 AIChE Annual Meeting - Austin, TX, United States Duration: 7 Nov 2004 → 12 Nov 2004 |
Conference
| Conference | 2004 AIChE Annual Meeting |
|---|---|
| Country/Territory | United States |
| City | Austin, TX |
| Period | 7/11/04 → 12/11/04 |
Keywords
- CO recovery process
- Cost estimation
- Simulation