The effect of SO2 on CO2 absorption in an aqueous potassium carbonate solvent

被引:17
|
作者
Wappel, David [1 ]
Khan, Ash [1 ]
Shallcross, David [1 ]
Joswig, Sebastian [1 ]
Kentish, Sandra [1 ]
Stevens, Geoff [1 ]
机构
[1] Univ Melbourne, Dept Chem & Biomol Engn, CO2CRC, Melbourne, Vic 3010, Australia
来源
GREENHOUSE GAS CONTROL TECHNOLOGIES 9 | 2009年 / 1卷 / 01期
关键词
electrolytes; Vapor liquid equilibria; solvent absorption; carbon dioxide; potassium carbonate; SOx; LOW PARTIAL PRESSURES; ELECTROLYTE SYSTEMS; SOLUBILITY;
D O I
10.1016/j.egypro.2009.01.019
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
In solvent absorption systems for carbon dioxide capture, potassium carbonate shows particular promise as a solvent. One of the advantages of this solvent is that it is more manageable by way of separation and/or cost effectiveness in the presence of SO2. This paper examines the feasibility of using the same absorber system for simultaneous capture of both CO2 and SO2 from post combustion flue gases. Using a dynamic equilibrium apparatus, the changes in the vapour pressure were measured upon the introduction of sulphur dioxide to a CO2/N-2 mixed gas stream. It has been shown that there is a small change in the resultant vapour pressure. The overall affect of SO2 on the efficiency of CO2 capture is discussed. (C) 2009 CO2CRC Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:125 / 131
页数:7
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