Ultrathin porous cation exchange membranes for high‐performance diffusion dialysis alkali recovery

Abstract Salt‐laden waste alkali streams pose significant environmental and economic challenges and demand efficient recovery. As an energy‐efficient route for alkali recovery, diffusion dialysis (DD) is limited by the poor hydroxide permeability () of conventional dense cation exchange membranes (CEMs). Herein, porous CEMs were fabricated via non‐solvent induced phase separation of a blend of chloromethylated polyethersulfone and sulfonated polyethersulfone, followed by crosslinking with polyethylenimine and post‐sulfonation with 1,3‐propane sultone. Through optimization of polymer composition, crosslinking degree, and sulfonation level, we engineered membranes with tailored microstructure and transport properties. The optimized membrane demonstrates a record‐high of 23.8 × 10 −3 m/h in NaOH/Na 2 WO 4 systems, while maintaining OH − /WO 4 2− selectivity () of 21.2; the permeability exceeds commercial benchmarks and reported values. This breakthrough establishes a practical and scalable approach for sustainable alkali recovery from high‐salinity industrial waste streams.

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Publication Details

Journal
AIChE Journal
Published
2025-11-17
DOI
https://doi.org/10.1002/aic.70152
Primary Topic
Membrane-based Ion Separation Techniques
Type
article
Field-Weighted Citation Impact
0.00

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article

Ultrathin porous cation exchange membranes for high‐performance diffusion dialysis alkali recovery

Xiaoda Wang, Wen‐Bin Jian, Xiaocheng Lin, Lan Yang et al.
AIChE Journal
Membrane-based Ion Separation Techniques
article

Ultrathin porous cation exchange membranes for high‐performance diffusion dialysis alkali recovery

Xiaoda Wang, Wen‐Bin Jian, Xiaocheng Lin, Lan Yang, Xiang’an Yue, Yafei Cheng, C. Y. Jiang
article en

Abstract

Abstract Salt‐laden waste alkali streams pose significant environmental and economic challenges and demand efficient recovery. As an energy‐efficient route for alkali recovery, diffusion dialysis (DD) is limited by the poor hydroxide permeability () of conventional dense cation exchange membranes (CEMs). Herein, porous CEMs were fabricated via non‐solvent induced phase separation of a blend of chloromethylated polyethersulfone and sulfonated polyethersulfone, followed by crosslinking with polyethylenimine and post‐sulfonation with 1,3‐propane sultone. Through optimization of polymer composition, crosslinking degree, and sulfonation level, we engineered membranes with tailored microstructure and transport properties. The optimized membrane demonstrates a record‐high of 23.8 × 10 −3 m/h in NaOH/Na 2 WO 4 systems, while maintaining OH − /WO 4 2− selectivity () of 21.2; the permeability exceeds commercial benchmarks and reported values. This breakthrough establishes a practical and scalable approach for sustainable alkali recovery from high‐salinity industrial waste streams.

AIChE JournalVol. 72(2)
University of Science and Technology of China (CN), Fuzhou University (CN)
National Natural Science Foundation of China, Natural Science Foundation of Fujian Province, National Key Research and Development Program of China
Openalex Percentile: Top 66%
Membrane-based Ion Separation Techniques
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