Large‐Area Ultrathin Metal–Organic Framework Membranes Fabricated on Flexible Polymer Supports for Gas Separations

Author:

Liang Yueyao12,Zhang Zhengqing1,Chen Aibing3,Yu Caijiao1,Sun Yuxiu1ORCID,Du Juan3,Qiao Zhihua1ORCID,Wang Zhi4,Guiver Michael D.56ORCID,Zhong Chongli1ORCID

Affiliation:

1. State Key Laboratory of Separation Membranes and Membrane Processes Tiangong University Tianjin 300387 China

2. College of Textiles and Clothing Qingdao University Qingdao 266071 China

3. College of Chemical and Pharmaceutical Engineering Hebei University of Science and Technology 26 Yuxiang Road Shijiazhuang 050018 China

4. School of Chemical Engineering and Technology Tianjin University Tianjin 300072 China

5. State Key Laboratory of Engines, School of Mechanical Engineering Tianjin University Tianjin 300072 China

6. National Industry-Education Platform of Energy Storage Tianjin University Tianjin 300072 China

Abstract

AbstractUltrathin continuous metal–organic framework (MOF) membranes have the potential to achieve high gas permeance and selectivity simultaneously for otherwise difficult gas separations, but with few exceptions for zeolitic‐imidazolate frameworks (ZIF) membranes, current methods cannot conveniently realize practical large‐area fabrication. Here, we propose a ligand back diffusion‐assisted bipolymer‐directed metal ion distribution strategy for preparing large‐area ultrathin MOF membranes on flexible polymeric support layers. The bipolymer directs metal ions to form a cross‐linked two‐dimensional (2D) network with a uniform distribution of metal ions on support layers. Ligand back diffusion controls the feed of ligand molecules available for nuclei formation, resulting in the continuous growth of large‐area ultrathin MOF membranes. We report the practical fabrication of three representative defect‐free MOF membranes with areas larger than 2,400 cm2 and ultrathin selective layers (50–130 nm), including ZIFs and carboxylate‐linker MOFs. Among these, the ZIF‐8 membrane displays high gas permeance of 3,979 GPU for C3H6, with good mixed gas selectivity (43.88 for C3H6/C3H8). To illustrate its scale‐up practicality, MOF membranes were prepared and incorporated into spiral‐wound membrane modules with an active area of 4,800 cm2. The ZIF‐8 membrane module presents high gas permeance (3,930 GPU for C3H6) with acceptable ideal gas selectivity (37.45 for C3H6/C3H8).

Funder

Key Technologies Research and Development Program

National Natural Science Foundation of China

State Key Laboratory of Engines

Publisher

Wiley

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