CIESC Journal ›› 2023, Vol. 74 ›› Issue (8): 3203-3215.DOI: 10.11949/0438-1157.20230541
• Reviews and monographs • Previous Articles Next Articles
Jiayi ZHANG1(), Jiali HE1, Jiangpeng XIE1, Jian WANG1, Yu ZHAO1,2, Dongqiang ZHANG1,2()
Received:
2023-06-05
Revised:
2023-08-02
Online:
2023-10-18
Published:
2023-08-25
Contact:
Dongqiang ZHANG
张佳怡1(), 何佳莉1, 谢江鹏1, 王健1, 赵鹬1,2, 张栋强1,2()
通讯作者:
张栋强
作者简介:
张佳怡(1998—),女,硕士研究生,212081702005@lut.edu.cn
基金资助:
CLC Number:
Jiayi ZHANG, Jiali HE, Jiangpeng XIE, Jian WANG, Yu ZHAO, Dongqiang ZHANG. Research progress of pervaporation technology for N-methylpyrrolidone recovery in lithium battery production[J]. CIESC Journal, 2023, 74(8): 3203-3215.
张佳怡, 何佳莉, 谢江鹏, 王健, 赵鹬, 张栋强. 渗透汽化技术用于锂电池生产中N-甲基吡咯烷酮回收的研究进展[J]. 化工学报, 2023, 74(8): 3203-3215.
膜类型 | 进料/% | 渗透液/% | 通量/(g/(m2·h)) | 选择性 | ||
---|---|---|---|---|---|---|
NMP | H2O | NMP | H2O | |||
15% PEBA-2533 | 97.12 | 2.88 | 37.22 | 63 | 41.50 | 56.96 |
15% PEBA-2533 + 10% zeolite | 97.12 | 2.88 | 36.47 | 64 | 45.14 | 58.84 |
15% PEBA-2533 + 20% zeolite | 97.12 | 2.88 | 33.28 | 67 | 48.64 | 67.71 |
15% PEBA-2533 + 30% zeolite | 97.12 | 2.88 | 38.18 | 62 | 50.48 | 54.68 |
15% PEBA-2533 + 2% TDI crosslinked for 2 h | 97.12 | 2.88 | 35.14 | 65 | 44.64 | 62.34 |
15% PEBA-2533 + 10% zeolite + 2% TDI crosslinked for 2 h | 97.12 | 2.88 | 35.9 | 64 | 49.47 | 60.3 |
15% PEBA-2533 + 20% zeolite + 2% TDI crosslinked for 2 h | 97.12 | 2.88 | 30.75 | 69 | 51.74 | 76.06 |
15% PEBA-2533 + 30% zeolite + 2% TDI crosslinked for 2 h | 97.12 | 2.88 | 21.69 | 78 | 54.94 | 121.95 |
Table 1 Effect of zeolite loading on membrane performance for NMP dehydration at constant temperature (30℃) and permeate pressure (133.3 Pa)[64]
膜类型 | 进料/% | 渗透液/% | 通量/(g/(m2·h)) | 选择性 | ||
---|---|---|---|---|---|---|
NMP | H2O | NMP | H2O | |||
15% PEBA-2533 | 97.12 | 2.88 | 37.22 | 63 | 41.50 | 56.96 |
15% PEBA-2533 + 10% zeolite | 97.12 | 2.88 | 36.47 | 64 | 45.14 | 58.84 |
15% PEBA-2533 + 20% zeolite | 97.12 | 2.88 | 33.28 | 67 | 48.64 | 67.71 |
15% PEBA-2533 + 30% zeolite | 97.12 | 2.88 | 38.18 | 62 | 50.48 | 54.68 |
15% PEBA-2533 + 2% TDI crosslinked for 2 h | 97.12 | 2.88 | 35.14 | 65 | 44.64 | 62.34 |
15% PEBA-2533 + 10% zeolite + 2% TDI crosslinked for 2 h | 97.12 | 2.88 | 35.9 | 64 | 49.47 | 60.3 |
15% PEBA-2533 + 20% zeolite + 2% TDI crosslinked for 2 h | 97.12 | 2.88 | 30.75 | 69 | 51.74 | 76.06 |
15% PEBA-2533 + 30% zeolite + 2% TDI crosslinked for 2 h | 97.12 | 2.88 | 21.69 | 78 | 54.94 | 121.95 |
膜类型 | 进料水含量/%(质量) | 温度/ ℃ | 通量/(kg/(m2·h)) | 分离因子 | 文献 |
---|---|---|---|---|---|
polyurethane urea | — | 45 | 0.013 | 3396 | [ |
BTESE | 8 | 130 | 3.2 | 1183 | [ |
high-silica CHA-type | 50 | 130 | 36 | 1100 | [ |
PAN hollow fiber | 30 | 70 | 1.5 | — | [ |
poly(ether-block-amide) 2533 + 4A zeolite + TDI | 3 | 30 | 1.2 | 180 | [ |
chitosan/poly(ether-block-amide) composite (TEOS crosslinked) | 1.3 | 30 | 0.02 | 1007 | [ |
polyvinyl alcohol (PVA)/CNT composite membranes | — | 80 | 0.06 | 3500 | [ |
NaA zeolite | 0.1 | 150 | 0.11 | 9997 | [ |
Table 2 Summary of membrane materials used for NMP recovery by pervaporation technology
膜类型 | 进料水含量/%(质量) | 温度/ ℃ | 通量/(kg/(m2·h)) | 分离因子 | 文献 |
---|---|---|---|---|---|
polyurethane urea | — | 45 | 0.013 | 3396 | [ |
BTESE | 8 | 130 | 3.2 | 1183 | [ |
high-silica CHA-type | 50 | 130 | 36 | 1100 | [ |
PAN hollow fiber | 30 | 70 | 1.5 | — | [ |
poly(ether-block-amide) 2533 + 4A zeolite + TDI | 3 | 30 | 1.2 | 180 | [ |
chitosan/poly(ether-block-amide) composite (TEOS crosslinked) | 1.3 | 30 | 0.02 | 1007 | [ |
polyvinyl alcohol (PVA)/CNT composite membranes | — | 80 | 0.06 | 3500 | [ |
NaA zeolite | 0.1 | 150 | 0.11 | 9997 | [ |
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