Comparison of rotating packed bed and packed bed absorber in pilot plant and model simulation for CO2 capture

被引:33
作者
Chamchan, Nipon [1 ]
Chang, Jia-Yu [1 ]
Hsu, Hsiao-Ching [1 ]
Kang, Jia-Lin [1 ]
Wong, David Shan Hill [1 ]
Jang, Shi-Shang [1 ]
Shen, Jui-Fu [2 ]
机构
[1] Natl Tsing Hua Univ, Dept Chem Engn, Hsinchu 30013, Taiwan
[2] China Steel Corp, New Mat Res & Dev Dept, Kaohsiung, Taiwan
关键词
Rotating packed bed; Packed bed; Pilot plant; Carbon dioxide capture; Chemical absorption; Simulation; MASS-TRANSFER; CARBON-DIOXIDE; POWER-PLANTS; ABSORPTION; LIQUID; MONOETHANOLAMINE; PREDICTION; COLUMN; GAS; MEA;
D O I
10.1016/j.jtice.2016.08.046
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
In this study, both packed-bed (PB) and rotating PB (RPB) absorbers with a packed-bed stripper were used in a pilot plant for the removal of carbon dioxide (CO2) with 30 wt% monoethanolamine (MEA) as the solvent. The flue gas feed is the combustion product of the blast furnace gas from a steel mill containing approximately 30% of CO2. Both PB and RPB exhibit the same performance for the capture of CO2 with the same amount of energy consumption, but the RPB has a volume of approximately one-third that of PB absorber. The results obtained from experiments using similar to 20 wt% MEA showed good agreement with those obtained from simulation using an Aspen rate-based model for PB and an Aspen custom modeler for RPB. These results demonstrated the feasibility of using a RPB for decreasing the size of absorber under relevant process conditions for capturing CO2. (C) 2016 Taiwan Institute of Chemical Engineers. Published by Elsevier B.V. All rights reserved.
引用
收藏
页码:20 / 26
页数:7
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