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High-Throughput Screening of MOF Adsorbents and Membranes for H(2) Purification and CO(2) Capture
[Image: see text] Metal organic frameworks (MOFs) have emerged as great adsorbent and membrane candidates for separation of CO(2)/H(2) mixtures. The main challenge is the existence of thousands of MOFs, which requires computational screening methods to identify the best materials prior to experiment...
Autores principales: | , , |
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Formato: | Online Artículo Texto |
Lenguaje: | English |
Publicado: |
American
Chemical Society
2018
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Acceso en línea: | https://www.ncbi.nlm.nih.gov/pmc/articles/PMC6172601/ https://www.ncbi.nlm.nih.gov/pubmed/30193065 http://dx.doi.org/10.1021/acsami.8b12746 |
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author | Avci, Gokay Velioglu, Sadiye Keskin, Seda |
author_facet | Avci, Gokay Velioglu, Sadiye Keskin, Seda |
author_sort | Avci, Gokay |
collection | PubMed |
description | [Image: see text] Metal organic frameworks (MOFs) have emerged as great adsorbent and membrane candidates for separation of CO(2)/H(2) mixtures. The main challenge is the existence of thousands of MOFs, which requires computational screening methods to identify the best materials prior to experimental efforts. In this study, we performed high-throughput computational screening of MOFs to examine their adsorbent and membrane performances for CO(2)/H(2) separation. Grand canonical Monte Carlo (GCMC) and molecular dynamics (MD) simulations were used to compute various adsorbent and membrane performance metrics of 3857 MOFs. CO(2)/H(2) adsorption selectivities of MOFs at pressure swing adsorption (PSA) and vacuum swing adsorption (VSA) conditions were calculated to be in the range of 2.5–25 000 and 2.5–85 000, respectively, outperforming many zeolite adsorbents. Correlations between the ranking of MOF adsorbents at the PSA and VSA conditions were examined. H(2)/CO(2) selectivities and H(2) permeabilities of MOF membranes were computed as 2.1 × 10(–5)–6.3 and 230–1.7 × 10(6) Barrer, respectively. A high number of MOF membranes was identified to surpass the upper bound defined for polymers due to high gas permeabilities of MOFs. Structure–performance relations revealed that MOFs with narrow pore sizes and low porosities are the best adsorbent materials for separation of CO(2) from H(2), whereas MOFs with large pore sizes and high porosities are the best membrane materials for selective separation of H(2). Our results will guide the selection of MOF adsorbents and membranes for efficient H(2) purification and CO(2) capture processes. |
format | Online Article Text |
id | pubmed-6172601 |
institution | National Center for Biotechnology Information |
language | English |
publishDate | 2018 |
publisher | American
Chemical Society |
record_format | MEDLINE/PubMed |
spelling | pubmed-61726012018-10-11 High-Throughput Screening of MOF Adsorbents and Membranes for H(2) Purification and CO(2) Capture Avci, Gokay Velioglu, Sadiye Keskin, Seda ACS Appl Mater Interfaces [Image: see text] Metal organic frameworks (MOFs) have emerged as great adsorbent and membrane candidates for separation of CO(2)/H(2) mixtures. The main challenge is the existence of thousands of MOFs, which requires computational screening methods to identify the best materials prior to experimental efforts. In this study, we performed high-throughput computational screening of MOFs to examine their adsorbent and membrane performances for CO(2)/H(2) separation. Grand canonical Monte Carlo (GCMC) and molecular dynamics (MD) simulations were used to compute various adsorbent and membrane performance metrics of 3857 MOFs. CO(2)/H(2) adsorption selectivities of MOFs at pressure swing adsorption (PSA) and vacuum swing adsorption (VSA) conditions were calculated to be in the range of 2.5–25 000 and 2.5–85 000, respectively, outperforming many zeolite adsorbents. Correlations between the ranking of MOF adsorbents at the PSA and VSA conditions were examined. H(2)/CO(2) selectivities and H(2) permeabilities of MOF membranes were computed as 2.1 × 10(–5)–6.3 and 230–1.7 × 10(6) Barrer, respectively. A high number of MOF membranes was identified to surpass the upper bound defined for polymers due to high gas permeabilities of MOFs. Structure–performance relations revealed that MOFs with narrow pore sizes and low porosities are the best adsorbent materials for separation of CO(2) from H(2), whereas MOFs with large pore sizes and high porosities are the best membrane materials for selective separation of H(2). Our results will guide the selection of MOF adsorbents and membranes for efficient H(2) purification and CO(2) capture processes. American Chemical Society 2018-09-07 2018-10-03 /pmc/articles/PMC6172601/ /pubmed/30193065 http://dx.doi.org/10.1021/acsami.8b12746 Text en Copyright © 2018 American Chemical Society This is an open access article published under an ACS AuthorChoice License (http://pubs.acs.org/page/policy/authorchoice_termsofuse.html) , which permits copying and redistribution of the article or any adaptations for non-commercial purposes. |
spellingShingle | Avci, Gokay Velioglu, Sadiye Keskin, Seda High-Throughput Screening of MOF Adsorbents and Membranes for H(2) Purification and CO(2) Capture |
title | High-Throughput
Screening of MOF Adsorbents and Membranes
for H(2) Purification and CO(2) Capture |
title_full | High-Throughput
Screening of MOF Adsorbents and Membranes
for H(2) Purification and CO(2) Capture |
title_fullStr | High-Throughput
Screening of MOF Adsorbents and Membranes
for H(2) Purification and CO(2) Capture |
title_full_unstemmed | High-Throughput
Screening of MOF Adsorbents and Membranes
for H(2) Purification and CO(2) Capture |
title_short | High-Throughput
Screening of MOF Adsorbents and Membranes
for H(2) Purification and CO(2) Capture |
title_sort | high-throughput
screening of mof adsorbents and membranes
for h(2) purification and co(2) capture |
url | https://www.ncbi.nlm.nih.gov/pmc/articles/PMC6172601/ https://www.ncbi.nlm.nih.gov/pubmed/30193065 http://dx.doi.org/10.1021/acsami.8b12746 |
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