Absorption of carbon dioxide in aqueous MDEA solution coupling dust suppression under atomization

被引:1
作者
Liu, HongJing [1 ]
Bei, PengZhi [1 ]
Yao, Hui [1 ]
Li, Bo [1 ]
Guo, LiYing [1 ]
机构
[1] Shenyang Univ Technol, Sch Petrochem Engn, 30 Guanghua Rd, Liaoyang 111003, Liaoning, Peoples R China
基金
中国国家自然科学基金;
关键词
CO2; capture; aqueous MDEA solution; dust suppression; atomization; power plant flue gas; CO2; CAPTURE; ENHANCEMENT FACTOR; GAS-ABSORPTION; KINETICS; PARTICLES; MECHANISM; RECOVERY; POWER; HEAT; MEA;
D O I
10.1080/01496395.2018.1556694
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
Large amounts of CO2 and dust particles coming from power plant flue need to be captured and removed before flue is discharged into the air. In present work, absorption of carbon dioxide in aqueous N-methylidiethanolamine (MDEA) solution coupling dust suppression has been studied in an atomization absorption column, with MDEA concentrations ranging from 0.1 to 0.5mol/L, and with atomization frequencies ranging from 50 to 80?HZ. The obtained experimental results show that absorption rate of CO2 in aqueous MDEA solution can be enhanced when the absorption process couples a dust suppression one under the condition of atomization. The reason for it is attributed to the adsorption of droplets on the solid particles which restrains the amount of entrainment and makes more droplets contact with gas so as to increase effective mass transfer area, thus resulting in the increase of CO2 absorption rate. The range of obtained enhancement factor is from 1.1 to 1.7. Mass transfer enhancement factor increases with the increase of MDEA concentration and atomization frequency at a certain range. Effective mass transfer areas and entrainment ratios suppressed have been calculated based on theoretic research. The results calculated agree with our experimental phenomena, and support the enhancement mass transfer mechanism proposed.
引用
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页码:3027 / 3036
页数:10
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