Effects of SO2 on CO2 capture using chilled ammonia solvent

被引:3
|
作者
Li, Jingde [1 ]
Cheng, Kuang [1 ]
Croiset, Eric [1 ]
Anderson, William A. [1 ]
Li, Qinghai [2 ]
Tan, Zhongchao [1 ,3 ]
机构
[1] Univ Waterloo, Dept Chem Engn, Waterloo, ON N2L 3G1, Canada
[2] Tsinghua Univ, Key Lab Thermal Sci & Power Engn, Minist Educ, Dept Thermal Engn, Beijing 100084, Peoples R China
[3] Univ Waterloo, Dept Mech & Mech Engn, Waterloo, ON N2L 3G1, Canada
基金
对外科技合作项目(国际科技项目);
关键词
CO2; capture; SO2; effect; Chilled aqueous ammonia; Mass transfer coefficient; CARBON-DIOXIDE; AQUEOUS AMMONIA; SIMULTANEOUS ABSORPTION; HEAT REQUIREMENT; SULFUR-DIOXIDE; GASES; KINETICS; REGENERATION;
D O I
10.1016/j.ijggc.2017.06.013
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The impact of SO2 on CO2 capture using chilled aqueous ammonia was investigated in the present study. Experimental observations showed that the mass transfer of CO2 in aqueous ammonia decreased with the increasing concentration of SO2 in the gas phase. A mathematic model based on reaction plane three-film theory was developed and validated to predict the effects of SO2 on CO2 absorption in aqueous ammonia. To make the model more easily used, a simple equation that correlates the concentrations of CO2 and SO2 in chilled aqueous ammonia was proposed based on the numerical results. Although the correlation equation was developed at 0 degrees C, its prediction for CO2 mass transfer coefficients fit well with experimental data in the temperature range of 0-60 degrees C.
引用
收藏
页码:442 / 448
页数:7
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