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

Jiyong Kim; Dongwoon Kim; I. I. Moon

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

Jiyong Kim, Dongwoon Kim, I. I. Moon

Department of Chemical and Biomolecular Engineering

Research output: Contribution to conference › Paper › peer-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 language	English
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
Country	United States
City	Austin, TX
Period	04/11/7 → 04/11/12

All Science Journal Classification (ASJC) codes

Engineering(all)

UN SDGs

This output contributes to the following Sustainable Development Goal(s)

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title = "Development and cost estimation of green gas reduction process for power plant",

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.",

author = "Jiyong Kim and Dongwoon Kim and Moon, {I. I.}",

year = "2004",

language = "English",

pages = "6941--6947",

note = "2004 AIChE Annual Meeting ; Conference date: 07-11-2004 Through 12-11-2004",

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TY - CONF

T1 - Development and cost estimation of green gas reduction process for power plant

AU - Kim, Jiyong

AU - Kim, Dongwoon

AU - Moon, I. I.

PY - 2004

Y1 - 2004

N2 - 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.

AB - 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.

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M3 - Paper

AN - SCOPUS:22544450785

SP - 6941

EP - 6947

T2 - 2004 AIChE Annual Meeting

Y2 - 7 November 2004 through 12 November 2004

ER -

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

Abstract

Other

All Science Journal Classification (ASJC) codes

UN SDGs

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Cite this