Effect of sulfation on CO2 capture of CaO-based sorbents during calcium looping cycle

被引:51
|
作者
Luo, Cong [1 ,2 ]
Zheng, Ying [1 ]
Guo, Jia [2 ]
Feng, Bo [3 ]
机构
[1] Huazhong Univ Sci & Technol, State Key Lab Coal Combust, Wuhan 430074, Hubei, Peoples R China
[2] Univ Queensland, Sch Mech & Min Engn, St Lucia, Qld 4072, Australia
[3] Wuhan Inst Technol, Minist Educ, Key Lab Green Chem Proc, Wuhan 430073, Hubei, Peoples R China
基金
中国国家自然科学基金;
关键词
Calcium looping cycle; CaO-based sorbent; CO2; capture; SO2; Sulfation; FLUIDIZED-BED; PERFORMANCE; LIMESTONE; CARBONATION; OXIDE; REACTIVATION; CONVERSION;
D O I
10.1016/j.fuel.2013.09.063
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
Calcium looping cycle is considered as one of the most promising post combustion CO2 capture technologies that can curb CO2 emissions from power plants fired with fossil fuel. However the presence of SO2 and steam in the flue gas leads to the sulfation of CaO-based sorbents, and thus reduces the sorbents' capacity for CO2 capture. In this study, the effect of sorbent sulfation during both carbonation and calcination stage on the cyclic CO2 capture performance was investigated. The results showed that the reaction time, SO2 concentrations and steam greatly influenced the capacity of CaO-based sorbent. The sulfation degree of the sorbent decreased with the reduction of carbonation and calcination time per cycle. High SO2 concentration present with steam led to a rapid loss in capacity of the sorbent within a few cycles. Furthermore, the synthetic sorbent derived from a sol-gel process had much higher cyclic CO2 capture capacities than natural limestone sorbent whether in conditions without SO2 or with SO2 and steam. Microscopic images showed that after multiple cycles in the presence of SO2 and steam, the porous structure of the synthetic sorbent could be retained while limestone experienced serious pore blockage and agglomeration of grains. (C) 2013 Elsevier Ltd. All rights reserved.
引用
收藏
页码:124 / 130
页数:7
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