Pilot plant results for advanced CO2 capture process using amine scrubbing at the Jaworzno II Power Plant in Poland

被引:99
作者
Stec, Marcin [1 ]
Tatarczuk, Adam [1 ]
Wieclaw-Solny, Lucyna [1 ]
Krotki, Aleksander [1 ]
Sciazko, Marek [1 ]
Tokarski, Stanislaw [2 ]
机构
[1] Inst Chem Proc Coal, PL-41803 Zabrze, Poland
[2] TAURON Polska Energia SA, PL-40114 Katowice, Poland
关键词
Post combustion CO2 capture; Pilot plant; Coal-fired power plant; STRIPPER CONFIGURATIONS; ABSORPTION; PERFORMANCE; SOLUBILITY; SOLVENTS; MEA;
D O I
10.1016/j.fuel.2015.01.014
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 purpose of this study is to present the testing of a 30 wt% solution of ethanolamine (MEA) in an advanced CO2 capture pilot plant. The mobile pilot plant, designed, constructed and operated by the Institute for Chemical Processing of Coal (IChPW) in cooperation with industrial partners: TAURON Polska Energia and TAURON Wytwarzanie, was used to carry out trials at the Jaworzno II Power Plant in Poland. Thanks to flexible technological design, numerous process flows sheet modifications were tested. The use of split flow or inter-stage absorber cooling is demonstrated and compared to the standard amine process. Presented modifications resulted in an increase of CO2 recovery ranging from 3% to 8%, whilst reducing the reboiler heat duty by about 5%. The correlation of CO2 recovery, reboiler heat duty and process parameters (solvent loading, L/G ratio) has been established for numerous process flow sheet modifications. The tests provide valuable experimental evidence for modifications described in the literature, mainly through modelling and demonstrate that flow sheet modifications, despite the increase in plant complexity, are worth considering. (C) 2015 Elsevier Ltd. All rights reserved.
引用
收藏
页码:50 / 56
页数:7
相关论文
共 24 条
[1]  
Andrzej Wilk, 2012, INVESTIGATION EFFECT
[2]   Integration of CO2 capture unit using single- and blended-amines into supercritical coal-fired power plants:: Implications for emission and energy management [J].
Aroonwilas, Adisorn ;
Veawab, Amornuadee .
INTERNATIONAL JOURNAL OF GREENHOUSE GAS CONTROL, 2007, 1 (02) :143-150
[3]   Performance of MEA and amine-blends in the CSIRO PCC pilot plant at Loy Yang Power in Australia [J].
Artanto, Yuli ;
Jansen, James ;
Pearson, Pauline ;
Thong Do ;
Cottrell, Aaron ;
Meuleman, Erik ;
Feron, Paul .
FUEL, 2012, 101 :264-275
[4]   A survey of process flow sheet modifications for energy efficient CO2 capture from flue gases using chemical absorption [J].
Cousins, A. ;
Wardhaugh, L. T. ;
Feron, P. H. M. .
INTERNATIONAL JOURNAL OF GREENHOUSE GAS CONTROL, 2011, 5 (04) :605-619
[5]  
Hilliard M., 2008, A predictive thermodynamic model for an aqueous blend of potassium carbonate, piperazine, and monoethanolamine for carbon dioxide capture from flue gas
[6]   THE SOLUBILITY OF CO2 IN A 30-MASS-PERCENT MONOETHANOLAMINE SOLUTION [J].
JOU, FY ;
MATHER, AE ;
OTTO, FD .
CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1995, 73 (01) :140-147
[7]   Enthalpy of absorption of CO2 with alkanolamine solutions predicted from reaction equilibrium constants [J].
Kim, Inna ;
Hoff, Karl A. ;
Hessen, Erik T. ;
Haug-Warberg, Tore ;
Svendsen, Hallvard F. .
CHEMICAL ENGINEERING SCIENCE, 2009, 64 (09) :2027-2038
[8]   Effects of the temperature bulge in CO2 absorption from flue gas by aqueous monoethanolamine [J].
Kvamsdal, Hanne M. ;
Rochelle, Gary T. .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2008, 47 (03) :867-875
[9]   Screening of flowsheet modifications for an efficient monoethanolamine (MEA) based post-combustion CO2 capture [J].
Le Moullec, Y. ;
Kanniche, M. .
INTERNATIONAL JOURNAL OF GREENHOUSE GAS CONTROL, 2011, 5 (04) :727-740
[10]   The theory and practice of energy saving in the chemical industry: some methods for reducing thermodynamic irreversibility in chemical technology processes [J].
Leites, IL ;
Sama, DA ;
Lior, N .
ENERGY, 2003, 28 (01) :55-97