The effect of different solvents on the formation of large‐area MOF membranes

Author:

Zhou Fan12,Chen Yanling3,Zhang Zhengqing12ORCID,Gu Zhenjie14,Sun Yuxiu12ORCID,Tong Minman5ORCID,Yang Qingyuan3ORCID,Dong Wenjun6,Pan Yichang7ORCID,Qiao Zhihua12ORCID,Zhong Chongli12ORCID

Affiliation:

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

2. School of Chemistry and Chemical Engineering Tiangong University Tianjin China

3. State Key Laboratory of Organic‐Inorganic Composites, College of Chemical Engineering Beijing University of Chemical Technology Beijing China

4. School of Physical Science and Technology Tiangong University Tianjin China

5. School of Chemistry and Materials Science Jiangsu Normal University Xuzhou China

6. Beijing Advanced Innovation Center for Materials Genome Engineering, Beijing Key Laboratory of Function Materials for Molecule & Structure Construction, School of Materials Science and Engineering University of Science and Technology Beijing Beijing China

7. College of Chemical Engineering, State Key Laboratory of Materials‐Oriented Chemical Engineering Nanjing Tech University Nanjing China

Abstract

AbstractMetal–organic framework (MOF) membranes are widely used in gas separation processes. However, the effect of solvents on the formation of large‐area MOF membranes, which directly influences separation performance, has rarely been investigated. In this study, three solvents (methanol, ethanol, and water) were selected to systematically investigate their effects on the zeolite imidazolium frameworks (ZIF) membrane formation via experimental validation and simulations. The results indicated that the solvent selection influenced crystallization rate, crystal size, and ZIF‐8 membrane formation ability. Particularly, when water was used as a solvent, slow nucleation and crystallization of the ZIF‐8 crystals were observed, resulting in a more complete crystal structure and a thinner ZIF‐8 membrane. Therefore, the ZIF‐8 membrane exhibited a gas permeance of 10,000 gas permeation unit and enhanced CO2/N2 selectivity. Furthermore, ZIF‐8 membrane with a surface area of 2400 cm2 and spiral‐wound membrane modules were developed, paving the way for large‐scale industrial production.

Funder

National Key Research and Development Program of China

National Natural Science Foundation of China

Publisher

Wiley

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