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<dc:dc xmlns:dc="http://purl.org/dc/elements/1.1/" xmlns:invenio="http://invenio-software.org/elements/1.0" xmlns:xsi="http://www.w3.org/2001/XMLSchema-instance" xsi:schemaLocation="http://www.openarchives.org/OAI/2.0/oai_dc/ http://www.openarchives.org/OAI/2.0/oai_dc.xsd"><dc:identifier>doi:10.1021/acsami.3c16093</dc:identifier><dc:language>eng</dc:language><dc:creator>Martínez-Izquierdo, Lidia</dc:creator><dc:creator>García-Comas, Cristina</dc:creator><dc:creator>Dai, Shan</dc:creator><dc:creator>Navarro, Marta</dc:creator><dc:creator>Tissot, Antoine</dc:creator><dc:creator>Serre, Christian</dc:creator><dc:creator>Téllez, Carlos</dc:creator><dc:creator>Coronas, Joaquín</dc:creator><dc:title>Ultrasmall Functionalized UiO-66 Nanoparticle/Polymer Pebax 1657 Thin-Film Nanocomposite Membranes for Optimal CO2 Separation</dc:title><dc:identifier>ART-2024-137347</dc:identifier><dc:description>Ultrasmall 4 to 6 nm nanoparticles of the metal–organic framework (MOF) UiO-66 (University of Oslo-66) were successfully prepared and embedded into the polymer Pebax 1657 to fabricate thin-film nanocomposite (TFN) membranes for CO2/N2 and CO2/CH4 separations. Furthermore, it has been demonstrated that ligand functionalization with amino (−NH2) and nitro (−NO2) groups significantly enhances the gas separation performance of the membranes. For CO2/N2 separation, 7.5 wt % UiO-66-NH2 nanoparticles provided a 53% improvement in CO2 permeance over the pristine membrane (from 181 to 277 GPU). Regarding the CO2/N2 selectivity, the membranes prepared with 5 wt % UiO-66-NO2 nanoparticles provided an increment of 17% over the membrane without the MOF (from 43.5 to 51.0). However, the CO2 permeance of this membrane dropped to 155 GPU. The addition of 10 wt % ZIF-94 particles with an average particle size of ∼45 nm into the 5 wt % UiO-66-NO2 membrane allowed to increase the CO2 permeance to 192 GPU while maintaining the CO2/N2 selectivity at ca. 51 due to the synergistic interaction between the MOFs and the polymer matrix provided by the hydrophilic nature of ZIF-94. In the case of CO2/CH4 separation, the 7.5 wt % UiO-66-NH2 membrane exhibited the best performance with an increase of the CO2 permeance from 201 to 245 GPU.</dc:description><dc:date>2024</dc:date><dc:source>http://zaguan.unizar.es/record/132200</dc:source><dc:doi>10.1021/acsami.3c16093</dc:doi><dc:identifier>http://zaguan.unizar.es/record/132200</dc:identifier><dc:identifier>oai:zaguan.unizar.es:132200</dc:identifier><dc:relation>info:eu-repo/grantAgreement/ES/DGA/T68-23R</dc:relation><dc:relation>info:eu-repo/grantAgreement/ES/MCIN-AEI/PID2019-104009RB-I00-AEI-10.13039-501100011033</dc:relation><dc:relation>info:eu-repo/grantAgreement/EUR/MICINN/TED2021-130621B-C41</dc:relation><dc:identifier.citation>ACS applied materials &amp; interfaces 16, 3 (2024), 4024-4034</dc:identifier.citation><dc:rights>by</dc:rights><dc:rights>https://creativecommons.org/licenses/by/4.0/deed.es</dc:rights><dc:rights>info:eu-repo/semantics/openAccess</dc:rights></dc:dc>

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