Kinetic study on promoted potassium carbonate solutions for CO2 capture from flue gas

被引:29
|
作者
Behr, P. [1 ]
Maun, A. [1 ]
Deutgen, K. [1 ]
Tunnat, A. [1 ]
Oeljeklaus, G. [1 ]
Goerner, K. [1 ]
机构
[1] Univ Duisburg Essen, Chair Environm Proc Engn & Plant Design, D-45141 Essen, Germany
关键词
Post-combustion CO2 capture; MEA; Potassium carbonate; Piperazine; Absorption; Desorption; Rates; Capacity;
D O I
10.1016/j.egypro.2011.01.027
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
Two different reactors were used to gather information about the kinetics of promoted potassium carbonate solutions for CO2 capture from flue gas. A bubble reactor was used to enable the fast evaluation of a wide rang of different solutions under a defined variation of experimental parameters as temperature and gas flow rate. Apart from the documentation of the CO2 absorption rate the bubble reactor also provided the possibility of a simultaneous documentation of the pH-value of the evaluated solution during the absorption process. These experiments underlined that the pH-value can be used as an indicator for the loading of a known solution during a absorption process. Secondly a wetted wall column reactor was used to obtain kinetic data of gas molecules on a clearly defined liquid surface. A variation of the experimental parameters as pressure, temperature and composition of the phases enables a process-steering in and out of chemical equilibrium. (C) 2011 Published by Elsevier Ltd.
引用
收藏
页码:85 / 92
页数:8
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