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

Jiyong Kim, Dongwoon Kim, I. I. Moon

Research output: Contribution to conferencePaperpeer-review

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
StatePublished - 2004
Externally publishedYes
Event2004 AIChE Annual Meeting - Austin, TX, United States
Duration: 7 Nov 200412 Nov 2004

Conference

Conference2004 AIChE Annual Meeting
Country/TerritoryUnited States
CityAustin, TX
Period7/11/0412/11/04

Keywords

  • CO recovery process
  • Cost estimation
  • Simulation

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