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 |
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Pages | 6941-6947 |
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
Other | 2004 AIChE Annual Meeting |
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Country/Territory | United States |
City | Austin, TX |
Period | 04/11/7 → 04/11/12 |
All Science Journal Classification (ASJC) codes
- Engineering(all)