Optimizing SSMMP-Based Fillers with −NH <sub>2</sub> Functionalization and PIM-1 Coating for High-Performance CO <sub>2</sub> /CH <sub>4</sub> and CO <sub>2</sub> /N <sub>2</sub> Separation in Mixed Matrix Membranes and Thin-Film Composite (TFC) Memb

Gas separation employing polymeric membranes is limited by the permeability-selectivity trade-off, which has driven the development, among numerous technologies, of mixed matrix membranes (MMMs) that combine highly permeable polymers with fillers capable of enhancing gas selectivity. The compatibility in the filler/polymer interface is therefore essential to design materials with superior separation performances. In this work, MMMs were produced with Pebax-2533, incorporating synthetic silico-metallic mineral particles (SSMMPs) and SSMMP-NH<sub>2</sub> fillers, both with and without PIM-1 surface coating, and were evaluated in the separation of CO<sub>2</sub>/CH<sub>4</sub> and CO<sub>2</sub>/N<sub>2</sub>. The membranes were prepared in two types: dense and thin-film composite (TFC). These MMMs were characterized through several techniques, and gas permeation assessments of the dense membranes were conducted at pressures ranging from 1 to 10 bar. The findings demonstrated enhanced thermal, mechanical, and gas separation properties following the addition of the fillers. Specifically, the sample containing 20 wt % SSMMP-NH<sub>2</sub>@PIM-1 achieved a permeability of 501.7 Barrer at 10 bar, representing a 129.8% increase relative to the pure membrane. Additionally, the TFC membrane was fabricated using a self-made porous polysulfone (PSF) support, which was subsequently coated with a selective layer and a protective layer of polydimethylsiloxane (PDMS), achieving a CO<sub>2</sub> permeance of 575 GPU and selectivities of 12 for CO<sub>2</sub>/CH<sub>4</sub> and 33 for CO<sub>2</sub>/N<sub>2</sub>. The results demonstrated the beneficial effects of functionalizing the amine groups (-NH<sub>2</sub>) in the fillers, particularly when employing the nonsolvent-induced surface deposition (NISD) technique to coat PIM-1 on the filler surface. The developed materials exhibit promising performance as visualized in the Robeson graph and TFCs target regions, suggesting that they could be suitable for industrial-scale CO<sub>2</sub> separation with additional development.

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Journal
ACS Omega
Published
2026-01-22
DOI
https://doi.org/10.1021/acsomega.5c11506
Primary Topic
Membrane Separation and Gas Transport
Type
article
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article

Optimizing SSMMP-Based Fillers with −NH 2 Functionalization and PIM-1 Coating for High-Performance CO 2 /CH 4 and CO 2 /N 2 Separation in Mixed Matrix Membranes and Thin-Film Composite (TFC) Memb

Leonardo Mello Garcia dos Santos, Sandra Einloft, Pierre Micoud, F. Martín et al.
ACS Omega
Membrane Separation and Gas Transport
article

Optimizing SSMMP-Based Fillers with −NH 2 Functionalization and PIM-1 Coating for High-Performance CO 2 /CH 4 and CO 2 /N 2 Separation in Mixed Matrix Membranes and Thin-Film Composite (TFC) Memb

Leonardo Mello Garcia dos Santos, Sandra Einloft, Pierre Micoud, F. Martín, Henrique Z. Ferrari, Franciele L. Bernard, C. Le Roux, Stéphane Mazières, Guilherme Dias
article en

Abstract

Gas separation employing polymeric membranes is limited by the permeability-selectivity trade-off, which has driven the development, among numerous technologies, of mixed matrix membranes (MMMs) that combine highly permeable polymers with fillers capable of enhancing gas selectivity. The compatibility in the filler/polymer interface is therefore essential to design materials with superior separation performances. In this work, MMMs were produced with Pebax-2533, incorporating synthetic silico-metallic mineral particles (SSMMPs) and SSMMP-NH<sub>2</sub> fillers, both with and without PIM-1 surface coating, and were evaluated in the separation of CO<sub>2</sub>/CH<sub>4</sub> and CO<sub>2</sub>/N<sub>2</sub>. The membranes were prepared in two types: dense and thin-film composite (TFC). These MMMs were characterized through several techniques, and gas permeation assessments of the dense membranes were conducted at pressures ranging from 1 to 10 bar. The findings demonstrated enhanced thermal, mechanical, and gas separation properties following the addition of the fillers. Specifically, the sample containing 20 wt % SSMMP-NH<sub>2</sub>@PIM-1 achieved a permeability of 501.7 Barrer at 10 bar, representing a 129.8% increase relative to the pure membrane. Additionally, the TFC membrane was fabricated using a self-made porous polysulfone (PSF) support, which was subsequently coated with a selective layer and a protective layer of polydimethylsiloxane (PDMS), achieving a CO<sub>2</sub> permeance of 575 GPU and selectivities of 12 for CO<sub>2</sub>/CH<sub>4</sub> and 33 for CO<sub>2</sub>/N<sub>2</sub>. The results demonstrated the beneficial effects of functionalizing the amine groups (-NH<sub>2</sub>) in the fillers, particularly when employing the nonsolvent-induced surface deposition (NISD) technique to coat PIM-1 on the filler surface. The developed materials exhibit promising performance as visualized in the Robeson graph and TFCs target regions, suggesting that they could be suitable for industrial-scale CO<sub>2</sub> separation with additional development.

ACS OmegaVol. 11(4)
Centre National de la Recherche Scientifique (FR), Université Fédérale de Toulouse Midi-Pyrénées (FR), Géosciences Environnement Toulouse (FR), Institut de Recherche pour le Développement (FR), Pontifícia Universidade Católica do Rio Grande do Sul (BR), University of Rio Grande and Rio Grande Community College (US), Pontifícia Universidade Católica de São Paulo (BR)
Openalex Percentile: Top 81%
Membrane Separation and Gas Transport
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