DocumentCode :
2104311
Title :
The Investigation on the Carbonation of CaO in FBC
Author :
Wang, Chunbo ; Lu, Guang ; Song, Chunchang
Author_Institution :
Sch. of Energy & Power Eng., North China Electr. Power Univ., Baoding, China
fYear :
2010
fDate :
28-31 March 2010
Firstpage :
1
Lastpage :
4
Abstract :
Limestone is usually be used as a sorbent for capture of sulphur dioxide, but, almost half of CaO will not reacted with SO2 in FBC. So, when the fly ash that contains CaO cools to bellow the calcination temperature, carbonation of CaO in fly ash that deposited on cool surfaces may occur. In this study, CaO was carbonated in a TGA under conditions expected in FBC. The temperature range investigated was 300, 350, 500 and 700°C with CO2 concentration set at 16%. The influence of H2O on the carbonation of CaO also be considered for the first time. And, the rate and the extent of the carbonation reaction were determined. H2O concentrations played important role in determining the reaction rate and extent of carbonation. The presence of H2O in the gas phase always resulted in higher CaO conversion ratio than that obtainable without H2O. Especially when T<350 there was no carbonation of CaO happened but the carbonation reaction was very obviously when reacted gases contains 10% H2O.
Keywords :
adsorption; calcium compounds; combustion; fluidised beds; power plants; CaO; carbonation; carbonation reaction; fluidized bed combustion; gas phase; limestone; power plant; sorbent; temperature 300 degC to 700 degC; Boilers; Calcination; Carbon capture and storage; Combustion; Flue gases; Fly ash; Heat transfer; Power generation; Temperature; Water;
fLanguage :
English
Publisher :
ieee
Conference_Titel :
Power and Energy Engineering Conference (APPEEC), 2010 Asia-Pacific
Conference_Location :
Chengdu
Print_ISBN :
978-1-4244-4812-8
Electronic_ISBN :
978-1-4244-4813-5
Type :
conf
DOI :
10.1109/APPEEC.2010.5448868
Filename :
5448868
Link To Document :
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