Moving beyond 90% Carbon Capture by Highly Selective Membrane Processes

被引:10
作者
Han, Yang [1 ]
Ho, W. S. Winston [1 ,2 ]
机构
[1] Ohio State Univ, William G Lowrie Dept Chem & Biomol Engn, 151 West Woodruff Ave, Columbus, OH 43210 USA
[2] Ohio State Univ, Dept Mat Sci & Engn, 2041 Coll Rd, Columbus, OH 43210 USA
关键词
carbon capture; deep CCS; facilitated transport membrane; flue gas; membrane separation; FACILITATED TRANSPORT MEMBRANES; CO2; CAPTURE; COMPOSITE MEMBRANES; GAS PERMEATION; FLUE-GAS; PERFORMANCE; SEPARATION; PURIFICATION; DIOXIDE; VACUUM;
D O I
10.3390/membranes12040399
中图分类号
Q5 [生物化学]; Q7 [分子生物学];
学科分类号
071010 ; 081704 ;
摘要
A membrane-based system with a retentate recycle process in tandem with an enriching cascade was studied for >90% carbon capture from coal flue gas. A highly CO2-selective facilitated transport membrane (FTM) was utilized particularly to enhance the CO2 separation efficiency from the CO2-lean gases for a high capture degree. A techno-economic analysis showed that the retentate recycle process was advantageous for <= 90% capture owing to the reduced parasitic energy consumption and membrane area. At >90% capture, the enriching cascade outperformed the retentate recycle process since a higher feed-to-permeate pressure ratio could be applied. An overall 99% capture degree could be achieved by combining the two processes, which yielded a low capture cost of USD47.2/tonne, whereas that would be USD 42.0/tonne for 90% capture. This FTM-based approach for deep carbon capture and storage can direct air capture for the mitigation of carbon emissions in the energy sector.
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页数:13
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