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Dual-strategy fabrication of thin-film Pebax membranes for CO2 separation: Hydrophilic gutter layer design and solvent-induced swelling

Identifikátory výsledku

  • Kód výsledku v IS VaVaI

    <a href="https://www.isvavai.cz/riv?ss=detail&h=RIV%2F60461373%3A22340%2F25%3A43932786" target="_blank" >RIV/60461373:22340/25:43932786 - isvavai.cz</a>

  • Výsledek na webu

    <a href="https://www.sciencedirect.com/science/article/pii/S1385894725081744" target="_blank" >https://www.sciencedirect.com/science/article/pii/S1385894725081744</a>

  • DOI - Digital Object Identifier

    <a href="http://dx.doi.org/10.1016/j.cej.2025.167335" target="_blank" >10.1016/j.cej.2025.167335</a>

Alternativní jazyky

  • Jazyk výsledku

    angličtina

  • Název v původním jazyce

    Dual-strategy fabrication of thin-film Pebax membranes for CO2 separation: Hydrophilic gutter layer design and solvent-induced swelling

  • Popis výsledku v původním jazyce

    Fabricating polyether block amide thin-film composite (TFC) membranes for CO2 separation remains challenging due to their high viscosity, microphase separation, and strong hydrophilicity. This study introduces a dual-strategy approach for the scalable fabrication of defect-free Pebax-1657 TFC membranes: (i) hydrophilic modification of the polydimethylsiloxane (PDMS) gutter layer via polyethylene glycol (PEG) through a two-step hydrosilylation, and (ii) solvent vapor-induced swelling of both the gutter and selective layers. PEG incorporation into PDMS and the resulting increase in hydrophilicity were confirmed by 1H NMR, XPS, and contact angle measurements, while swelling solvents were optimized through systematic analysis. The PEG-grafted PDMS (PDMS-PEG) gutter layer improves interfacial compatibility and coating uniformity. Swelling with hexane and ethanol vapor increases free volume and suppresses defect formation. This strategy enabled reproducible fabrication of large-area (14 x 10 cm2) Pebax-poly(poly(ethylene glycol) methyl ether acrylate) (Pebax-PPEG-MEA) membranes. The optimized membrane exhibited a CO2 permeance of 272 gas permeation units (GPU), with CO2/O2 and CO2/N2 selectivities of 14.0 and 32.0, respectively. Under mixed-gas conditions, the membrane maintained stable performance up to 20 atm, with long-term operational stability confirmed. This work demonstrates that integrating interfacial engineering with swelling control is critical for achieving high-performance gas separation membranes. The proposed approach offers a scalable and reproducible route for producing next-generation TFC membranes for energy-efficient CO2 capture applications.

  • Název v anglickém jazyce

    Dual-strategy fabrication of thin-film Pebax membranes for CO2 separation: Hydrophilic gutter layer design and solvent-induced swelling

  • Popis výsledku anglicky

    Fabricating polyether block amide thin-film composite (TFC) membranes for CO2 separation remains challenging due to their high viscosity, microphase separation, and strong hydrophilicity. This study introduces a dual-strategy approach for the scalable fabrication of defect-free Pebax-1657 TFC membranes: (i) hydrophilic modification of the polydimethylsiloxane (PDMS) gutter layer via polyethylene glycol (PEG) through a two-step hydrosilylation, and (ii) solvent vapor-induced swelling of both the gutter and selective layers. PEG incorporation into PDMS and the resulting increase in hydrophilicity were confirmed by 1H NMR, XPS, and contact angle measurements, while swelling solvents were optimized through systematic analysis. The PEG-grafted PDMS (PDMS-PEG) gutter layer improves interfacial compatibility and coating uniformity. Swelling with hexane and ethanol vapor increases free volume and suppresses defect formation. This strategy enabled reproducible fabrication of large-area (14 x 10 cm2) Pebax-poly(poly(ethylene glycol) methyl ether acrylate) (Pebax-PPEG-MEA) membranes. The optimized membrane exhibited a CO2 permeance of 272 gas permeation units (GPU), with CO2/O2 and CO2/N2 selectivities of 14.0 and 32.0, respectively. Under mixed-gas conditions, the membrane maintained stable performance up to 20 atm, with long-term operational stability confirmed. This work demonstrates that integrating interfacial engineering with swelling control is critical for achieving high-performance gas separation membranes. The proposed approach offers a scalable and reproducible route for producing next-generation TFC membranes for energy-efficient CO2 capture applications.

Klasifikace

  • Druh

    J<sub>imp</sub> - Článek v periodiku v databázi Web of Science

  • CEP obor

  • OECD FORD obor

    20402 - Chemical process engineering

Návaznosti výsledku

  • Projekt

  • Návaznosti

    I - Institucionalni podpora na dlouhodoby koncepcni rozvoj vyzkumne organizace

Ostatní

  • Rok uplatnění

    2025

  • Kód důvěrnosti údajů

    S - Úplné a pravdivé údaje o projektu nepodléhají ochraně podle zvláštních právních předpisů

Údaje specifické pro druh výsledku

  • Název periodika

    Chemical Engineering Journal

  • ISSN

    1385-8947

  • e-ISSN

    1873-3212

  • Svazek periodika

    522

  • Číslo periodika v rámci svazku

    October 2025

  • Stát vydavatele periodika

    CH - Švýcarská konfederace

  • Počet stran výsledku

    10

  • Strana od-do

    167335

  • Kód UT WoS článku

    001584443900004

  • EID výsledku v databázi Scopus

    2-s2.0-105014033741