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Moving beyond 90% Carbon Capture by Highly Selective Membrane Processes

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 CO(2)-selective facilitated transport membrane (FTM) was utilized particularly to enhance the CO(2) separation efficiency from the CO(2)-le...

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Detalles Bibliográficos
Autores principales: Han, Yang, Ho, W. S. Winston
Formato: Online Artículo Texto
Lenguaje:English
Publicado: MDPI 2022
Materias:
Acceso en línea:https://www.ncbi.nlm.nih.gov/pmc/articles/PMC9031579/
https://www.ncbi.nlm.nih.gov/pubmed/35448369
http://dx.doi.org/10.3390/membranes12040399
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author Han, Yang
Ho, W. S. Winston
author_facet Han, Yang
Ho, W. S. Winston
author_sort Han, Yang
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description 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 CO(2)-selective facilitated transport membrane (FTM) was utilized particularly to enhance the CO(2) separation efficiency from the CO(2)-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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spelling pubmed-90315792022-04-23 Moving beyond 90% Carbon Capture by Highly Selective Membrane Processes Han, Yang Ho, W. S. Winston Membranes (Basel) Article 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 CO(2)-selective facilitated transport membrane (FTM) was utilized particularly to enhance the CO(2) separation efficiency from the CO(2)-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. MDPI 2022-04-01 /pmc/articles/PMC9031579/ /pubmed/35448369 http://dx.doi.org/10.3390/membranes12040399 Text en © 2022 by the authors. https://creativecommons.org/licenses/by/4.0/Licensee MDPI, Basel, Switzerland. This article is an open access article distributed under the terms and conditions of the Creative Commons Attribution (CC BY) license (https://creativecommons.org/licenses/by/4.0/).
spellingShingle Article
Han, Yang
Ho, W. S. Winston
Moving beyond 90% Carbon Capture by Highly Selective Membrane Processes
title Moving beyond 90% Carbon Capture by Highly Selective Membrane Processes
title_full Moving beyond 90% Carbon Capture by Highly Selective Membrane Processes
title_fullStr Moving beyond 90% Carbon Capture by Highly Selective Membrane Processes
title_full_unstemmed Moving beyond 90% Carbon Capture by Highly Selective Membrane Processes
title_short Moving beyond 90% Carbon Capture by Highly Selective Membrane Processes
title_sort moving beyond 90% carbon capture by highly selective membrane processes
topic Article
url https://www.ncbi.nlm.nih.gov/pmc/articles/PMC9031579/
https://www.ncbi.nlm.nih.gov/pubmed/35448369
http://dx.doi.org/10.3390/membranes12040399
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