共 24 条
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.
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页码:20 / 26
页数:7
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