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Electrophoretic Crystallization of Ultrathin High-performance Metal-organic Framework Membranes
Published on: August 16, 2018
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Ultrathin porous amine-based solid adsorbent incorporated zeolitic imidazolate framework-8 membrane for gas
Yu Qin1, Li Xu1, Liying Liu1
1Beijing Key Laboratory of Membrane Science and Technology, College of Chemical Engineering, Beijing University of Chemical Technology Beijing 100029 China dingzw@mail.buct.edu.cn +86-10-64436781.
RSC Advances
|April 28, 2022
Summary
This study introduces a novel gas separation membrane by integrating an amine-based solid adsorbent with a zeolitic imidazolate framework-8 (ZIF-8) membrane. This innovative approach enhances continuous gas separation performance for CO2/N2, CO2/CH4, and H2/CH4 mixtures.
Area of Science:
- Materials Science
- Chemical Engineering
- Separation Science
Background:
- Continuous gas separation is crucial for industrial processes.
- Traditional solid adsorbents often require regeneration, limiting continuous operation.
- Zeolitic imidazolate framework-8 (ZIF-8) membranes show promise for gas separation but can have defects.
Purpose of the Study:
- To develop a novel, continuously operable gas separation system.
- To enhance the fabrication and performance of ZIF-8 membranes.
- To leverage amine-based adsorbents for improved gas selectivity and membrane integrity.
Main Methods:
- Fabrication of an amine-based solid adsorbent using ZIF-8, 3-isocyanatopropyltrimethoxysilane (IPTMS), and N-[(3-trimethoxysilyl)propyl]diethylenetriamine (3N-APS).
- Incorporation of the amine-based adsorbent during the in-situ growth of ZIF-8 membranes on a macroporous substrate.
- Characterization of the resulting composite membrane's gas separation performance (CO2/N2, CO2/CH4, H2/CH4).
Main Results:
- The integrated ZIF-8 membrane exhibited excellent CO2/N2 and CO2/CH4 separation performance.
- An ultrathin (0.6 μm) ZIF-8 membrane achieved a high CO2 permeance (4.75 × 10^-6 mol m^-2 s^-1 Pa^-1) with selectivities of 4.67 for CO2/N2 and 6.02 for CO2/CH4.
- The membrane demonstrated superior H2/CH4 selectivity (31.2) and high H2 permeance (2.45 × 10^-5 mol m^-2 s^-1 Pa^-1).
Conclusions:
- Combining amine-based adsorbents with ZIF-8 membranes offers a viable strategy for continuous gas separation.
- The amino groups in the adsorbent facilitate ZIF-8 nucleation and growth, improving membrane quality.
- This novel composite membrane system shows significant potential for efficient industrial gas separations.

