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  4. Overall process analysis and optimisation for CO₂ capture from coal fired power plants based on phase change solvents forming two liquid phases
 
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Overall process analysis and optimisation for CO₂ capture from coal fired power plants based on phase change solvents forming two liquid phases

Citation Link: https://doi.org/10.15480/882.2225
Publikationstyp
Conference Paper
Date Issued
2013-08-05
Sprache
English
Author(s)
Liebenthal, Ulrich  
Pinto, Diego D. D.  
Monteiro, Juliana G. M.-S.  
Svendsen, Hallvard F.  
Kather, Alfons  
Institut
Energietechnik M-5  
TORE-DOI
10.15480/882.2225
TORE-URI
http://hdl.handle.net/11420/2544
Journal
Energy procedia  
Start Page
1844
End Page
1854
Citation
Energy Procedia (37): 1844-1854 (2013)
Contribution to Conference
GHGT-11, 11th International Conference on Greenhouse Gas Control Technologies, 2012  
Publisher DOI
10.1016/j.egypro.2013.06.064
Scopus ID
2-s2.0-84883751360
Publisher
Elsevier
In this work the potential of a novel post-combustion CO₂ capture process is analysed with respect to the integrated overall process. As solvent a blend of two amines (DEEA/MAPA) which forms two liquid phases under CO₂ loading is used. The two phases have distinct physical characteristics. Only the heavy phase, rich in CO₂ loading, is led to the desorber. The novel solvent combination promises very low energy consumption compared to a 30 wt.-% MEA solution. The efficiency penalty, taking into account the integrated overall process, is very low too. Furthermore, different integration configurations in the overall process are investigated to show the effect in greenfield and retrofit power plant cases.
Subjects
post-cobustion
CO2 capture
integration
phase change solvents
DDC Class
600: Technik
620: Ingenieurwissenschaften
Lizenz
https://creativecommons.org/licenses/by-nc-nd/3.0/
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