Comparison of different CO2 recovery processes in their optimum operating conditions from a pulverized coal power plant

被引:2
作者
Molina, Carol Toro [1 ]
Bouallou, Chakib [1 ]
机构
[1] PSL Res Univ, MINES ParisTech, CES Ctr Efficacite Energet Syst, 60 Bd St Michel, F-75006 Paris, France
来源
13TH INTERNATIONAL CONFERENCE ON GREENHOUSE GAS CONTROL TECHNOLOGIES, GHGT-13 | 2017年 / 114卷
关键词
CO2; capture; ammonia; monoethanolamine; methyldiethanolamine; coal; power plant; PLUS TRIETHYLENE TETRAMINE; AQUEOUS-SOLUTIONS; CAPTURE; AMMONIA; MONOETHANOLAMINE; SOLVENT;
D O I
10.1016/j.egypro.2017.03.1257
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
To capture CO2, ammonia solution is a good chemical solvent compared to monoethanolamine (MEA) and methyldiethanolamine (MDEA) because its reactivity and its low enthalpy of solution. In the idea of having a relevant comparison, this study compares the different processes using these solvents in their optimal operating conditions. With respect to ammonia, the experimentally determined optimal conditions are: 3 wt%, 303 K, 1 atm. The purpose of this study is modelling CO2 capture from a pulverized coal (PC) fired power plant and estimated its efficiency when CO2 capture is integrated. A relevant comparison between ammonia solvent and conventional amines: MEA and MDEA are made. This study has allowed us to select the solvent that reduces the cost of CO2 capture in power plants. The net electrical power of the plant decreased with CO2 capture: from 555.6 MW without capture to 451.9 with NH3 capture, and 385.16 with MEA capture. (C) 2017 The Authors. Published by Elsevier Ltd.
引用
收藏
页码:1360 / 1365
页数:6
相关论文
共 12 条
[1]   CO2 Capture from Power Stations Running with Natural Gas (NGCC) and Pulverized Coal (PC): Assessment of a New Chemical Solvent Based on Aqueous Solutions of N-MethylDiEthanolAmine plus TriEthylene TetrAmine [J].
Amann, Jean-Marc G. ;
Bouallou, Chakib .
GREENHOUSE GAS CONTROL TECHNOLOGIES 9, 2009, 1 (01) :909-916
[2]   Kinetics of the Absorption of CO2 in Aqueous Solutions of N-Methyldiethanolamine plus Triethylene Tetramine [J].
Amann, Jean-Marc G. ;
Bouallou, Chakib .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2009, 48 (08) :3761-3770
[3]  
[Anonymous], 2004, INT J THERMODYN, DOI DOI 10.5541/IJ0T.139
[4]  
[Anonymous], 2011, International Energy Outlook 2011
[5]   Chilled ammonia process for CO2 capture [J].
Darde, Victor ;
Thomsen, Kaj ;
van Well, Willy J. M. ;
Stenby, Erling H. .
GREENHOUSE GAS CONTROL TECHNOLOGIES 9, 2009, 1 (01) :1035-1042
[6]  
Duncan J., 2003, P 20 ANN INT PITTSB
[7]   Comparison of Ammonia, MonoEthanolAmine, DiEthanolAmine and MethylDiEthanolAmine Solvents to Reduce CO2 Greenhouse Gas Emissions [J].
Gonzalez-Garza, Daniel ;
Rivera-Tinoco, Rodrigo ;
Bouallou, Chakib .
PRES'09: 12TH INTERNATIONAL CONFERENCE ON PROCESS INTEGRATION, MODELLING AND OPTIMISATION FOR ENERGY SAVING AND POLLUTION REDUCTION, PTS 1 AND 2, 2009, 18 :279-284
[8]   Greek Lignite-Fired Power Plants with CO2 Capture for the Electricity Generation Sector [J].
Kakaras, Emmanouil K. ;
Koumanakos, Antonios K. ;
Doukelis, Aggelos F. .
16TH INTERNATIONAL CONFERENCE ON PROCESS INTEGRATION, MODELLING AND OPTIMISATION FOR ENERGY SAVING AND POLLUTION REDUCTION (PRES'13), 2013, 35 :331-336
[9]   Pre-combustion, post-combustion and oxy-combustion in thermal power plant for CO2 capture [J].
Kanniche, Mohamed ;
Gros-Bonnivard, Rene ;
Jaud, Philippe ;
Valle-Marcos, Jose ;
Amann, Jean-Marc ;
Bouallou, Chakib .
APPLIED THERMAL ENGINEERING, 2010, 30 (01) :53-62
[10]   Description and evaluation of flowsheet modifications and their interaction for an efficient monoethanolamine based post-combustion CO2 capture [J].
Le Moullec, Yann ;
Kanniche, Mohamed .
PRES 2010: 13TH INTERNATIONAL CONFERENCE ON PROCESS INTEGRATION, MODELLING AND OPTIMISATION FOR ENERGY SAVING AND POLLUTION REDUCTION, 2010, 21 :175-180