Kinetics of reaction between carbon dioxide and sterically hindered amines for carbon dioxide recovery from power plant flue gases

被引:79
|
作者
Mimura, T
Suda, T
Iwaki, I
Honda, A
Kumazawa, H
机构
[1] Kansai Elect Power Co, Environm Res Ctr, Amagasaki, Hyogo 661, Japan
[2] Kansai Elect Power Co, Gen Off Nucl & Fossil Power Prod, Osaka 530, Japan
[3] Mitsubishi Heavy Ind Ltd, Hiroshima Res & Dev Ctr, Hirosima 733, Japan
[4] Kansai Tech Co, Merchandise Dev Grp, Oil Div, Osaka 552, Japan
[5] Toyama Univ, Dept Chem & Biochem Engn, Toyama 930, Japan
关键词
absorption; carbon dioxide; sterically hindered amine; chemical absorption method; chemical kinetics;
D O I
10.1080/00986449808912745
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The kinetics of the reaction of CO2 with secondary an alkanolamine linked with alkyl group, methylaminoethanol (MAE), ethylaminoethanol (EAE) and n-butylaminoethanol (BAE), for CO2 recovery from power plant flue gases was investigated using a stirred tank absorber with a plane unbroken gas-liquid interface at 298 K. To evaluate the reaction rate constant from the CO2 absorption rate data under the fast-reaction regime, a combined parameter containing the solubility and diffusivity for N2O in aqueous solutions of sterically hindered amines; MAE, EAE and BAE, was measured using a wetter-wall column apparatus at the same temperature. For further practical evaluation of the reaction rate, apparent rate constants for EAE under the process condition of CO2 removal from power plants were investigated.
引用
收藏
页码:245 / 260
页数:16
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