Advanced CO2 Capture process using MEA scrubbing: Configuration of a Split Flow and Phase Separation Heat Exchanger

被引:40
作者
Jung, Jaeheum [1 ]
Jeong, Yeong Su [1 ]
Lim, Youngsub [1 ]
Lee, Chi Seob [2 ]
Han, Chonghun [1 ]
机构
[1] Seoul Natl Univ, Sch Chem & Biol Engn, Seoul 151742, South Korea
[2] KEPCO Engn & Construct Co, Yongin, South Korea
来源
GHGT-11 | 2013年 / 37卷
关键词
CO2; capture; post combustion CO2 capture; advanced stripper configuration; cold solvent split; rich vapor compression; POWER-PLANT;
D O I
10.1016/j.egypro.2013.06.054
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
CO2 capture process using aqueous Monoethanolamine (MEA) scrubbing is a well-proven and commercially-ready technology for reducing CO2 emission to the atmosphere. Although the MEA scrubbing is the one of the most suitable technologies for post-combustion CO2 capture, the MEA process has a critical problem which is high consumption of reboiler heat energy for solvent regeneration. In order to reduce the reboiler heat requirement, this paper suggests an advanced configuration of MEA process which consists of split flow and a phase separation heat exchanger. The split flow permits to reduce the reflux ratio in the stripper and the phase separation heat exchanger permits to alleviate preheating duty loss. As a result, the regeneration energy of the advanced process is reduced by 2.840.Ilton CO2, which is lower than one of the reference process by 27%. (C) 2013 The Authors. Published by Elsevier Ltd.
引用
收藏
页码:1778 / 1784
页数:7
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