Ionic liquids for post-combustion CO2 absorption

被引:171
作者
Wappel, D. [1 ]
Gronald, G. [2 ]
Kalb, R. [3 ]
Draxler, J. [1 ]
机构
[1] Univ Leoben, Inst Proc Technol & Ind Environm Protect, A-8700 Leoben, Austria
[2] AE&E Austria GmbH & Co KG, A-8074 Raaba Graz, Austria
[3] Proion Prod Ion Subst GmbH, A-8074 Grambach, Austria
关键词
CO2; absorption; Ionic liquids; Vapour-liquid equilibrium; Post-combustion capture; CARBON-DIOXIDE; 30-MASS-PERCENT MONOETHANOLAMINE; SOLUBILITY; METHYLDIETHANOLAMINE; ENTHALPY; CAPTURE; MEA;
D O I
10.1016/j.ijggc.2009.11.012
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The present work is a study to evaluate ionic liquids as a potential solvent for post-combustion CO2 capture. In order to enhance the absorption performance of a CO2 capture unit, different ionic liquids have been designed and tested. The main goal was to get a comparison between a reference liquid and selected ionic liquids. As the reference, a solution of 30 w% monoethanolamine (MEA) and water was used. A large range of different pure and diluted ionic liquids was tested with a special screening process to gain general information about the CO2 absorption performance. Based on these results, a 60 w% ionic liquid solution in water was selected and the vapour-liquid equilibrium was measured experimentally between 40 degrees C and 110 degrees C. From these curves the enthalpy of absorption for capturing CO2 into the ionic liquid was determined. With these important parameters one is able to calculate the total energy demand for stripping of CO2 from the loaded solvent for comparison of the ionic liquid based solvent with the reference MEA solvent. The energy demand of this 60 w% ionic liquid is slightly lower than that of the reference solution, resulting in possible energy savings between 12 and 16%. (C) 2009 Elsevier Ltd. All rights reserved.
引用
收藏
页码:486 / 494
页数:9
相关论文
共 31 条
[1]   CO2 capture from power plants -: Part II.: A parametric study of the economical performance based on mono-ethanolamine [J].
Abu-Zahra, Mohammad R. M. ;
Niederer, John P. M. ;
Feron, Paul H. M. ;
Versteeg, Geert F. .
INTERNATIONAL JOURNAL OF GREENHOUSE GAS CONTROL, 2007, 1 (02) :135-142
[2]  
ANDERSON JL, 2007, CHERMRAWN 17 C GREEN
[3]  
[Anonymous], 1985, IND SOLVENTS HDB
[4]  
Anthony J. L., 2004, International Journal of Environmental Technology and Management, V4, P105
[5]   Solution thermodynamics of imidazolium-based ionic liquids and water [J].
Anthony, JL ;
Maginn, EJ ;
Brennecke, JF .
JOURNAL OF PHYSICAL CHEMISTRY B, 2001, 105 (44) :10942-10949
[6]  
Anthony JL, 2005, J PHYS CHEM B, V109, P6366, DOI 10.1021/jp0464041
[7]   MODEL OF VAPOR-LIQUID-EQUILIBRIA FOR AQUEOUS ACID GAS-ALKANOLAMINE SYSTEMS .2. REPRESENTATION OF H2S AND CO2 SOLUBILITY IN AQUEOUS MDEA AND CO2 SOLUBILITY IN AQUEOUS MIXTURES OF MDEA WITH MEA OR DEA [J].
AUSTGEN, DM ;
ROCHELLE, GT ;
CHEN, CC .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1991, 30 (03) :543-555
[8]   CO2 capture by a task-specific ionic liquid [J].
Bates, ED ;
Mayton, RD ;
Ntai, I ;
Davis, JH .
JOURNAL OF THE AMERICAN CHEMICAL SOCIETY, 2002, 124 (06) :926-927
[9]   THERMODYNAMIC PROPERTIES OF STRONG ELECTROLYTES IN AQUEOUS-SOLUTIONS [J].
BROMLEY, LA .
AICHE JOURNAL, 1973, 19 (02) :313-320
[10]  
BURNS B, 1995, OFFICIAL METHODS ANA