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 |
| Publication status | Published - 2004 Dec 1 |
| Event | 2004 AIChE Annual Meeting - Austin, TX, United States Duration: 2004 Nov 7 → 2004 Nov 12 |
Other
| Other | 2004 AIChE Annual Meeting |
|---|---|
| Country | United States |
| City | Austin, TX |
| Period | 04/11/7 → 04/11/12 |
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All Science Journal Classification (ASJC) codes
- Engineering(all)
Cite this
Kim, J., Kim, D., & Moon, I. I. (2004). Development and cost estimation of green gas reduction process for power plant. 6941-6947. Paper presented at 2004 AIChE Annual Meeting, Austin, TX, United States.