SCI和EI收录∣中国化工学会会刊

Chinese Journal of Chemical Engineering ›› 2025, Vol. 88 ›› Issue (12): 239-255.DOI: 10.1016/j.cjche.2025.06.039

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Thermodynamic mechanism of structural evolution for polyacrylonitrile membranes prepared via non-solvent induced phase separation

Chunqi Wang1,2,3, Zhongyu Fu1,2,3, Wei Liu1,2,3, Shuang Liu1,2,3, Shiling Jia1,2,3, Qingxin Meng1,2,3, Huixuan Zhang1,2,3   

  1. 1. School of Chemical Engineering, Changchun University of Technology, Changchun 130012, China;
    2. Engineering Research Center of Synthetic Resin and Special Fiber, Ministry of Education, Changchun University of Technology, Changchun 130012, China;
    3. Carbon Fiber Industry Innovation Center of Jilin Province, Changchun University of Technology, Changchun 130012, China
  • Received:2025-03-02 Revised:2025-05-08 Accepted:2025-06-11 Online:2025-11-08 Published:2026-02-09
  • Contact: Zhongyu Fu,E-mail:fuzhongyu@ccut.edu.cn;Huixuan Zhang,E-mail:zhanghx@ccut.edu.cn
  • Supported by:
    We would like to express our great thanks to Jilin Province National Development and Reform Commission(2024C019-1); Changbaishan Laboratory Science and Technology Innovation Project (CBS2025004, CBS2025004-01); Jilin Province Carbon Fiber Industry Innovation Center (2022C002) for the financial support.

Thermodynamic mechanism of structural evolution for polyacrylonitrile membranes prepared via non-solvent induced phase separation

Chunqi Wang1,2,3, Zhongyu Fu1,2,3, Wei Liu1,2,3, Shuang Liu1,2,3, Shiling Jia1,2,3, Qingxin Meng1,2,3, Huixuan Zhang1,2,3   

  1. 1. School of Chemical Engineering, Changchun University of Technology, Changchun 130012, China;
    2. Engineering Research Center of Synthetic Resin and Special Fiber, Ministry of Education, Changchun University of Technology, Changchun 130012, China;
    3. Carbon Fiber Industry Innovation Center of Jilin Province, Changchun University of Technology, Changchun 130012, China
  • 通讯作者: Zhongyu Fu,E-mail:fuzhongyu@ccut.edu.cn;Huixuan Zhang,E-mail:zhanghx@ccut.edu.cn
  • 基金资助:
    We would like to express our great thanks to Jilin Province National Development and Reform Commission(2024C019-1); Changbaishan Laboratory Science and Technology Innovation Project (CBS2025004, CBS2025004-01); Jilin Province Carbon Fiber Industry Innovation Center (2022C002) for the financial support.

Abstract: Non-solvent induced phase separation (NIPS) is one of the most used methods for the preparation of PAN membranes. Predicting the pattern of change in membrane structures remains a key issue. A binodal line procedure about PAN/solvent/non-solvent was established for it by Flory-Huggins theory. Calculation of non-solvent-polymer interaction parameter (χ13) by the osmotic pressure method combined with the Rudin model and the equilibrium dissolution method. Solvent-polymer interaction parameter (χ23) by viscosity method. Then, the solvent-nonsolvent interaction parameter (g12) equation is obtained by combining the modified Flory-Huggins free energy. Finally, the accuracy of the model was verified by cloud points experiments and membrane structures. It was found that when mixed non-solvents were used, the binodal line moved to 100% of the added component. Changes in membrane structure coincide with changes in phase diagrams when changing solvent and non-solvent species and temperature. Based on the combination of experiment and theory we obtained the maximum water flux of membranes was increased to 2217.47 L·m-2·h-1·bar-1 with the addition of additives PEG and SiO2 with DMF/PAN/H2O system. The average permeate flux over 0.75 h reached 387.12 L·m-2·h-1·bar-1 (1 bar = 0.1 MPa) with 82% flux recovery. The hexadecane oil-in-water emulsion have confirmed that the membranes showed prominently high retention rate achieved 99% for oil.

Key words: Polyacrylonitrile membrane, Phase separation, Thermodynamic

摘要: Non-solvent induced phase separation (NIPS) is one of the most used methods for the preparation of PAN membranes. Predicting the pattern of change in membrane structures remains a key issue. A binodal line procedure about PAN/solvent/non-solvent was established for it by Flory-Huggins theory. Calculation of non-solvent-polymer interaction parameter (χ13) by the osmotic pressure method combined with the Rudin model and the equilibrium dissolution method. Solvent-polymer interaction parameter (χ23) by viscosity method. Then, the solvent-nonsolvent interaction parameter (g12) equation is obtained by combining the modified Flory-Huggins free energy. Finally, the accuracy of the model was verified by cloud points experiments and membrane structures. It was found that when mixed non-solvents were used, the binodal line moved to 100% of the added component. Changes in membrane structure coincide with changes in phase diagrams when changing solvent and non-solvent species and temperature. Based on the combination of experiment and theory we obtained the maximum water flux of membranes was increased to 2217.47 L·m-2·h-1·bar-1 with the addition of additives PEG and SiO2 with DMF/PAN/H2O system. The average permeate flux over 0.75 h reached 387.12 L·m-2·h-1·bar-1 (1 bar = 0.1 MPa) with 82% flux recovery. The hexadecane oil-in-water emulsion have confirmed that the membranes showed prominently high retention rate achieved 99% for oil.

关键词: Polyacrylonitrile membrane, Phase separation, Thermodynamic