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.
引用
收藏
页数:15
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