Flue gas desulfurization by fine carbon-based sorbent

被引:0
|
作者
Peng, WW [1 ]
Wang, NJ [1 ]
Ji, XG [1 ]
Bu, XP [1 ]
Ying, YJ [1 ]
Bian, W [1 ]
Deng, YY [1 ]
机构
[1] China Coal Res Inst, Beijing Res Inst Coal Chem, Beijing 100013, Peoples R China
关键词
flue gas; desulfurization; carbon-based sorbent; regeneration; recovery;
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
This paper introduces the model of flue gas desulfurization by small size coal-based sorbent and results of fundamental support test studies. The SO2-removing efficiencies of more than 90% are achieved during multi-cycle tests in the downward entrained bed reactor. Sorbent regeneration by indirectly heating leads to tail gas consisting of 40-50% of SO2. The tail gas after cleanup is pressurized up to 2.0-3.0 MPa and cooled down to 0-20 degrees C resulting in gain of liquid sulfur dioxide at rate of 80-94%.
引用
收藏
页码:1385 / 1388
页数:4
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