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Techno-economic analysis of MOF-based adsorption cycles for postcombustion CO2 capture from wet flue gas
被引:20
|作者:
Peh, Shing Bo
[1
]
Farooq, Shamsuzzaman
[1
]
Zhao, Dan
[1
]
机构:
[1] Natl Univ Singapore, Dept Chem & Biomol Engn, 4 Engn Dr 4, Singapore 117585, Singapore
关键词:
Gas separation;
Process simulation;
Metal-organic frameworks;
CO2;
capture;
Temperature swing adsorption;
PRESSURE SWING ADSORPTION;
CARBON CAPTURE;
POWER-PLANTS;
PART I;
OPTIMIZATION;
PERFORMANCE;
TECHNOLOGY;
SIMULATION;
DESIGN;
D O I:
10.1016/j.ces.2022.118390
中图分类号:
TQ [化学工业];
学科分类号:
0817 ;
摘要:
In this study, we present a scale-up design, scheduling, and costing of a single-stage MOF (Metal-Organic Framework)-based 5-step temperature swing adsorption (TSA) process, which was recently shown to be effective for carbon capture and concentration (CCC) from wet flue gas containing 5 to 15 mol% CO2 with-out any pre-drying (Peh et al., 2022). This TSA process is also compared with a two-stage process at two feed conditions. In the two-stage process, the wet flue gas is first dried in a TSA process, and then CCC from the dry flue gas is carried out in a MOF-based 6-step vacuum swing adsorption (VSA) process. The TSA-based pre-drying process is also analyzed in detail. The two-stage process has lower minimum capture costs at both feed conditions ($91 versus $104.1 per tonne of CO2 captured at 25 degrees C and $113.3 versus $146.9 per tonne of CO2 captured at 40 degrees C).(c) 2022 Elsevier Ltd. All rights reserved.
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