Cyclic CO2 Capture Performance of Carbide Slag: Parametric Study

被引:0
作者
Zhang, Deng-Feng [1 ,2 ]
Zhao, Peng-Fei [1 ]
Li, Song-Geng [1 ]
Song, Wen-Li [1 ]
机构
[1] Chinese Acad Sci, Inst Proc Engn, State Key Lab Multi Phase Complex Syst, Beijing 100190, Peoples R China
[2] Grad Univ, Chinese Acad Sci, Beijing 100049, Peoples R China
来源
CLEANER COMBUSTION AND SUSTAINABLE WORLD | 2012年
基金
中国国家自然科学基金;
关键词
CO2; capture; carbonate looping; carbide slag; kinetics; CAO-BASED SORBENT; CAPACITY; REACTIVATION;
D O I
暂无
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 this work, CO2 capture performance of carbide slag has been investigated in a thermogravimetric analyzer (TGA). Effects of operation parameters including particle size, reaction temperature and reaction duration on CO2 capture capacity were studied. The experimental results indicate that the increase of particle size ranging from 80-180 gm has a positive effect on the CO2 capture capacity of carbide slag. The sorbent reactivity decreases with an increase of calcination temperature. The prolonged exposure to carbonation conditions has a beneficial effect on sorbent behavior as a function of the number of calcination/carbonation cycles; however, the duration in the calcination step has little effect. Based on the experimental results, the reaction rate constant of carbonation reaction is obtained from Jander equation. It is found that it decreases with the increasing cycles.
引用
收藏
页码:864 / 867
页数:4
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