Title of article :
Comparative assessment of coal fired IGCC systems with CO2 capture using physical absorption, membrane reactors and chemical looping
Author/Authors :
Rezvani، نويسنده , , Sina and Huang، نويسنده , , Ye and McIlveen-Wright، نويسنده , , David J. Hewitt، نويسنده , , Neil and Mondol، نويسنده , , Jayanta Deb Mondol، نويسنده ,
Issue Information :
روزنامه با شماره پیاپی سال 2009
Pages :
10
From page :
2463
To page :
2472
Abstract :
The integrated gasification combined cycle (IGCC) as an efficient power generation technology with lowest specific carbon dioxide emissions among coal power plants is a very good candidate for CO2 capture resulting in low energy penalties and minimised CO2 avoidance costs. In this paper, the techno-economic characteristics of four different capture technologies, which are built upon a conventional reference case, are studied using the chemical process simulation package “ECLIPSE”. The technology options considered are: physical absorption, water gas shift reactor membranes and two chemical looping combustion cycles (CLC), which employ single and double stage reactors. The latter system was devised to achieve a more balanced distribution of temperatures across the reactors and to counteract hot spots which lead to the agglomeration and the sintering of oxygen carriers. Despite the lowest efficiency loss among the studied systems, the economic performance of the double stage CLC was outperformed by systems employing physical absorption and water gas shift reactor membranes. Slightly higher efficiencies and lower costs were associated with systems with integrated air separation units. The estimation of the overall capital costs was carried out using a bottom-up approach. Finally, the CO2 avoidance costs of individual technologies were calculated based on the techno-economic data.
Keywords :
Physical absorption , Chemical looping , IGCC , Water gas shift membrane reactor , Ion transport membrane
Journal title :
Fuel
Serial Year :
2009
Journal title :
Fuel
Record number :
1465294
Link To Document :
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