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May 19, 2026Sustainable Chemistry for Climate Action1 citationsOpen Access

Chitosan-Gallic Acid Tailored Thin-Film Nanocomposite Membrane with ZIF-8 Metal–Organic Frameworks toward Improved CO2/CH4 and CO2/N2 Separation Performance

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RKRoghaye KhazaiiRAReza AbediniAKAtousa Rezaei Khenari

Key Points

  • The aim is to improve the separation performance of CO2/CH4 and CO2/N2 using ZIF-8 incorporated membranes.
  • Prepared ZIF-8-incorporated TFN membranes via one-pot in situ synthesis
  • Varied ZIF-8 content (5-15 wt%) and applied pressure (2-10 bar)
  • Analyzed structural, morphological, and gas separation performance of membranes.
  • 10 wt% ZIF-8 achieved a 25% increase in CO2 permeance (from 487.2 to 647.1 GPU) at 35°C and 10 bar
  • CO2/CH4 selectivity improved from 17.5 to 21.0 (16.5% improvement)
  • CO2/N2 selectivity increased from 23.8 to 26.4, indicating effective molecular sieve behavior.

Abstract

• One-pot in situ synthesis ensured uniform ZIF-8 distribution in CS–GA TFN membranes. • ZIF-8 boosted CO 2 permeance while preserving high CO 2 /CH 4 and CO 2 /N 2 selectivity. • Optimal separation performance achieved at 10 wt% ZIF-8 and 10 bar pressure. • Enhanced CO 2 transport attributed to ZIF-8 microporosity and CO 2 affinity. In the present work, ZIF-8-incoporated TFN membranes were prepared via a facile one-pot in situ synthesis approach, enabling uniform incorporation of ZIF-8 nanoparticles within a Chitosan-Gallic acid (CS-GA) selective layer. Structural and morphological analyses confirmed effective integration and uniform distribution of ZIF-8 throughout the polymer matrix, while preserving the thermal stability of the membranes following the introduction of ZIF-8 nanoparticles. The gas separation behavior of the TFN membranes was systematically investigated by varying the ZIF-8 content (5-15 wt%) and the applied operating pressure (2-10 bar). Compared to the pure CS-GA membrane, incorporation of ZIF-8 significantly enhanced CO 2 transport without compromising selectivity. The membrane loaded with 10 wt% ZIF-8 demonstrated the optimal balance between permeance and selectivity, achieving a 25% increase in CO 2 permeance (from 487.2 to 647.1 GPU) at 35°C and 10 bar. At this loading, CH 4 and N 2 permeances remained relatively low (30.8 and 24.5 GPU, respectively), indicating effective molecular sieving behavior. Consequently, the CO 2 /CH 4 selectivity increased from 17.5 to 21.0 (16.5% improvement), while the CO 2 /N 2 selectivity improved by nearly 10%, rising from 23.8 to 26.4 compared to the unmodified membrane. These enhancements are attributed to the combined effects of increased CO 2 uptake due to specific interactions with the ZIF‑8 framework and facilitated molecular pathways introduced by the ZIF‑8 porous structure, which together promote preferential CO 2 transport relative to CH 4 and N 2 .

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Cite This Study

Khazaii et al. (2026) studied this question.

synapsesocial.com/papers/6a0bfdc7166b51b53d37913bhttps://doi.org/10.1016/j.scca.2026.100211
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