CIESC Journal ›› 2025, Vol. 76 ›› Issue (5): 2377-2386.DOI: 10.11949/0438-1157.20241174
• Separation engineering • Previous Articles Next Articles
Xinchen XIANG1(
), Dan LU1,2, Ying ZHAO1, Zhikan YAO1,2, Ruiqiang KOU3, Danjun ZHENG1, Zhijun ZHOU1,4, Lin ZHANG1,2(
)
Received:2024-10-23
Revised:2024-12-20
Online:2025-06-13
Published:2025-05-25
Contact:
Lin ZHANG
向昕辰1(
), 鲁丹1,2, 赵影1, 姚之侃1,2, 寇瑞强3, 郑丹军1, 周志军1,4, 张林1,2(
)
通讯作者:
张林
作者简介:向昕辰(2000—),男,硕士研究生,willshake@zju.edu.cn
基金资助:CLC Number:
Xinchen XIANG, Dan LU, Ying ZHAO, Zhikan YAO, Ruiqiang KOU, Danjun ZHENG, Zhijun ZHOU, Lin ZHANG. Preparation of highly positively charged NF membranes with surface quaternization modification and Li+/Mg2+ separation performance[J]. CIESC Journal, 2025, 76(5): 2377-2386.
向昕辰, 鲁丹, 赵影, 姚之侃, 寇瑞强, 郑丹军, 周志军, 张林. 聚酰胺纳滤膜表面季铵化提高荷正电性及其锂镁分离性能[J]. 化工学报, 2025, 76(5): 2377-2386.
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Fig.3 PEI grafting concentration optimization: (a) the effect of PEI concentration on the content of surface amine groups; (b) rejection performance of modified membranes with different PEI concentrations for MgCl2 solution at pH 6.8
Fig.4 Optimization of N-alkylation reaction conditions: (a) optimization of sodium hydroxide concentration; (b) optimization of iodomethane concentration
Fig.8 Single salt separation performance of membranes: (a) MgCl2 solution at pH 6.8; (b) MgCl2 solution at pH 9.7; (c) LiCl solution at pH 6.8; (d) LiCl solution at pH 9.7
Fig.9 Mixed salt (Li+∶Mg2+ = 1∶10) separation performance of membrane: (a) Mg2+ rejection at different pH; (b) Li+ rejection at different pH; (c) separation factor at different pH
| 膜类型 | 压力/bar | 混盐浓度/(mg·L-1) | 镁锂比 | pH | 分离因子 | 文献 |
|---|---|---|---|---|---|---|
| N-alkyl@PEI/PA | 6 | 10 | 1000 | 6.8 | 35.7 | 本文 |
| NF90 | 16 | 20 | 2000 | 6.0 | 2.1 | [ |
| DK | 16 | 24 | 4940 | 7.0 | 3.2 | [ |
| TFC-MeOH | 6 | 24 | 1000 | 7.6 | 5.77 | [ |
| TFC-1 | 6 | 24 | 1000 | 7.6 | 9.36 | [ |
| TFC-2 | 6 | 24 | 1000 | 7.6 | 9.8 | [ |
| TFC-3 | 6 | 24 | 1000 | 7.6 | 11.38 | [ |
| TFC-4 | 6 | 24 | 1000 | 7.6 | 11.15 | [ |
| PEI-g-PA | 4 | 73 | 2000 | 7.0 | 23.9 | [ |
| PES/(CNC-COOH)/PEI/TMC | 4 | 20 | 2000 | 7.0 | 12.2 | [ |
| MCPM-2.0 | 2 | 1.54 | 1000 | 7.0 | 18 | [ |
| PEI/TMC-PDA-gC3N4 (M4) | 4 | 20 | 2000 | 7.3 | 13.39 | [ |
| PEI/TMC-PDA-gC3N4 (M5) | 4 | 48 | 2000 | 7.3 | 10.77 | [ |
| NF-IL-2 | 6 | 20 | 2000 | 7.9 | 8.12 | [ |
| PBI_12-25K | 6 | 10 | 2000 | 7.9 | 15.15 | [ |
Table 1 Comparison of experimental Li+/Mg2+ separation factors with data in literature
| 膜类型 | 压力/bar | 混盐浓度/(mg·L-1) | 镁锂比 | pH | 分离因子 | 文献 |
|---|---|---|---|---|---|---|
| N-alkyl@PEI/PA | 6 | 10 | 1000 | 6.8 | 35.7 | 本文 |
| NF90 | 16 | 20 | 2000 | 6.0 | 2.1 | [ |
| DK | 16 | 24 | 4940 | 7.0 | 3.2 | [ |
| TFC-MeOH | 6 | 24 | 1000 | 7.6 | 5.77 | [ |
| TFC-1 | 6 | 24 | 1000 | 7.6 | 9.36 | [ |
| TFC-2 | 6 | 24 | 1000 | 7.6 | 9.8 | [ |
| TFC-3 | 6 | 24 | 1000 | 7.6 | 11.38 | [ |
| TFC-4 | 6 | 24 | 1000 | 7.6 | 11.15 | [ |
| PEI-g-PA | 4 | 73 | 2000 | 7.0 | 23.9 | [ |
| PES/(CNC-COOH)/PEI/TMC | 4 | 20 | 2000 | 7.0 | 12.2 | [ |
| MCPM-2.0 | 2 | 1.54 | 1000 | 7.0 | 18 | [ |
| PEI/TMC-PDA-gC3N4 (M4) | 4 | 20 | 2000 | 7.3 | 13.39 | [ |
| PEI/TMC-PDA-gC3N4 (M5) | 4 | 48 | 2000 | 7.3 | 10.77 | [ |
| NF-IL-2 | 6 | 20 | 2000 | 7.9 | 8.12 | [ |
| PBI_12-25K | 6 | 10 | 2000 | 7.9 | 15.15 | [ |
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