Development and cost estimation of green gas reduction process for power plant

Jiyong Kim, Dongwoon Kim, I. I. Moon

Research output: Contribution to conferencePaper

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 languageEnglish
Pages6941-6947
Number of pages7
Publication statusPublished - 2004
Event2004 AIChE Annual Meeting - Austin, TX, United States
Duration: 2004 Nov 72004 Nov 12

Other

Other2004 AIChE Annual Meeting
CountryUnited States
CityAustin, TX
Period04/11/704/11/12

All Science Journal Classification (ASJC) codes

  • Engineering(all)

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    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.