Modeling and Simulation of CO2 Capture Process for Coal-based Power Plant using Amine Solvent in South Korea

被引:23
作者
Lim, Youngsub [1 ]
Kim, Jeongnam [1 ]
Jung, Jaeheum [1 ]
Lee, Chi Seob [2 ]
Han, Chonghun [1 ]
机构
[1] Seoul Natl Univ, 1 Gwanak Ro, Seoul 151742, South Korea
[2] KEPCO Engn & Construct Co, Yongin, South Korea
来源
GHGT-11 | 2013年 / 37卷
关键词
carbon capture; rate-based model; coal-based power plant; EXPERIMENTAL VALIDATION; POSTCOMBUSTION CAPTURE; ABSORPTION;
D O I
10.1016/j.egypro.2013.06.065
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
The interest in carbon capture technology is continuously rising since worldwide climate-change problems have intensified the concern regarding efficient removal of carbon dioxide Amine-based capture technology is a conventional technology to remove carbon dioxide in natural gas processing, and also can be used for carbon dioxide removal from flue gas in coal-based power plants. In particular, monoethanolamine is a conventional commercial absorbent to remove carbon dioxide and considered as a standard amine absorbent. Due to the high non-ideality of amine, rate-based models have been suggested to describe absorption and desorption of amine absorbent. However, most suggested models were validated against large-scale pilot plant results, and there were few models to consider both absorber and stripper with rate-based model. In this study, we applied two rate-based models introduced by previous literature to the actual pilot plant operation data in 0.1MW-scale Boryeong pilot plant. South Korea and developed a modified model with increased accuracy. The developed model showed good agreements with pilot plant results for both absorber and stripper. However, under low liquid-to-vapor ratio operation with high rich loading value, all model showed worse estimations. (C) 2013 The Authors. Published by Elsevier Ltd.
引用
收藏
页码:1855 / 1862
页数:8
相关论文
共 15 条
[1]  
Aboudheir A., 2002, THESIS
[2]  
[Anonymous], THESIS
[3]  
AspenPlus, 2011, RAT BAS MOD CO2 CAPT
[4]   MODEL OF VAPOR LIQUID EQUILIBRIA FOR AQUEOUS ACID GAS ALKANOLAMINE SYSTEMS USING THE ELECTROLYTE NRTL EQUATION [J].
AUSTGEN, DM ;
ROCHELLE, GT ;
PENG, X ;
CHEN, CC .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1989, 28 (07) :1060-1073
[5]  
Dugas R, 2006, THESIS
[6]   New Mass-Transfer Correlations for Packed Towers [J].
Hanley, Brian ;
Chen, Chau-Chyun .
AICHE JOURNAL, 2012, 58 (01) :132-152
[7]  
Hilliard M.D., 2008, PREDICTIVE THERMODYN
[8]   On the modelling and simulation of sour gas absorption by aqueous amine solutions [J].
Kucka, L ;
Müller, I ;
Kenig, EY ;
Górak, A .
CHEMICAL ENGINEERING SCIENCE, 2003, 58 (16) :3571-3578
[9]   Kinetics of the gas-liquid reaction between carbon dioxide and hydroxide ions [J].
Kucka, L ;
Kenig, EY ;
Górak, A .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2002, 41 (24) :5952-5957
[10]  
Onda K., 1968, Journal of Chemical Engineering of Japan, V1, P56, DOI DOI 10.1252/JCEJ.1.56