Chemical Industry and Engineering Progress ›› 2022, Vol. 41 ›› Issue (10): 5567-5577.DOI: 10.16085/j.issn.1000-6613.2021-2597
• Resources and environmental engineering • Previous Articles Next Articles
ZHANG Yi(), LIU Donghao, DING Yigang
Received:
2021-12-21
Revised:
2022-02-15
Online:
2022-10-21
Published:
2022-10-20
Contact:
ZHANG Yi
通讯作者:
张逸
作者简介:
张逸(1986—),男,副教授,硕士生导师,研究方向为稀土金属的分离。E-mail:zhangyi_1208@whu.edu.cn。
基金资助:
CLC Number:
ZHANG Yi, LIU Donghao, DING Yigang. Research progress of membrane technology for the separation of rare earth elements[J]. Chemical Industry and Engineering Progress, 2022, 41(10): 5567-5577.
张逸, 刘东昊, 丁一刚. 膜技术分离稀土金属元素的研究进展[J]. 化工进展, 2022, 41(10): 5567-5577.
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URL: https://hgjz.cip.com.cn/EN/10.16085/j.issn.1000-6613.2021-2597
膜骨架 | 载体 | 稀土金属 | 主要研究结果 | 文献 |
---|---|---|---|---|
PVDF | P227 | Lu | 载体质量分数40%、稀土浓度1mmol·L-1时,萃取率91% | [ |
PVDF | P227 | Lu/Sm/La | pH=1.5时,对Lu、Sm、La回收率为82%、40%、4% | [ |
EVOH | Cyanex272 | Lu | 处理能力较大,但载体质量分数25%时分离选择性3.78 | [ |
PAN | Calix8 | La | 静电纺丝法制备,吸附容量达155.10mg·g-1 | [ |
PVC | P204 | La/Gd/Y | 载体质量分数45%、pH=1.5时,萃取率接近100% | [ |
CTA | D2EHAF | Sc | 可选择性分离混合液中Sc,重复用5次萃取率基本不变 | [ |
CA | CMPO | Ce | 稀土浓度200mg·L-1时,萃取率大于90% | [ |
CA | TODGA | Ce | 稀土浓度200mg·L-1时,扩散系数为6.65×10-12m2·s-1 | [ |
PVDF | [A336][P507] | Lu/Yb | 载体质量分数37.5%时,对Yb的选择性高于Lu | [ |
PVDF | [A336][P227] | Y | 载体质量分数37.5%、稀土浓度1.1mmol·L-1时,可重复用8次 | [ |
PVDF | Cyphos 104 | Lu/Yb | 载体质量分数25%、稀土浓度20mmol·L-1时,分离选择性1.37 | [ |
膜骨架 | 载体 | 稀土金属 | 主要研究结果 | 文献 |
---|---|---|---|---|
PVDF | P227 | Lu | 载体质量分数40%、稀土浓度1mmol·L-1时,萃取率91% | [ |
PVDF | P227 | Lu/Sm/La | pH=1.5时,对Lu、Sm、La回收率为82%、40%、4% | [ |
EVOH | Cyanex272 | Lu | 处理能力较大,但载体质量分数25%时分离选择性3.78 | [ |
PAN | Calix8 | La | 静电纺丝法制备,吸附容量达155.10mg·g-1 | [ |
PVC | P204 | La/Gd/Y | 载体质量分数45%、pH=1.5时,萃取率接近100% | [ |
CTA | D2EHAF | Sc | 可选择性分离混合液中Sc,重复用5次萃取率基本不变 | [ |
CA | CMPO | Ce | 稀土浓度200mg·L-1时,萃取率大于90% | [ |
CA | TODGA | Ce | 稀土浓度200mg·L-1时,扩散系数为6.65×10-12m2·s-1 | [ |
PVDF | [A336][P507] | Lu/Yb | 载体质量分数37.5%时,对Yb的选择性高于Lu | [ |
PVDF | [A336][P227] | Y | 载体质量分数37.5%、稀土浓度1.1mmol·L-1时,可重复用8次 | [ |
PVDF | Cyphos 104 | Lu/Yb | 载体质量分数25%、稀土浓度20mmol·L-1时,分离选择性1.37 | [ |
类型 | 载体 | 稀土金属 | 主要研究结果 | 文献 |
---|---|---|---|---|
ELM | 苯胺 | RE | 表面活性剂T154、有机相磺化煤油时,可从磷矿浸取液中萃取出93%的混合RE | [ |
ELM | Cyanex272 | Dy | 表面活性剂Span80/85、有机相煤油时,萃取率99.6% | [ |
EPLM | P507 | Y/La/Sm/Al | 金属总浓度1.22g·L-1、电压4.5~5kV时,回收率分别为97.7%、90.3%、19.7、95.1% | [ |
EPLM | PMBP | Sc | 稀土浓度10mg·L-1、电压5kV时,萃取率96.9% | [ |
BOLM | N1923 | RE/Al | 稀土浓度116.68mg·L-1、Al浓度27.7mg·L-1时,RE/Al选择性为44.89,稀土回收率为84.4% | [ |
BOLM | P507 | RE | 稀土浓度116.68mg·L-1时,稀土回收率为90%以上 | [ |
FSLM | D2EHPA | Eu | PVDF为膜骨架、稀土浓度0.1mmol·L-1时,萃取率94.2% | [ |
FSLM | TODGA | RE | PVDF为膜骨架、稀土浓度72.4mg·L-1时,可从含有Ca/Mg/Fe/RE的磷矿模拟废液中萃取出96.3%的RE | [ |
HFSLM | PC-88A | Nd | 4mol·L-1硝酸时,萃取率95%,反萃率87% | [ |
HFSLM | D2EHPA | Nd/Pr/Dy | 2mol·L-1硝酸时,萃取率分别58.62%、85.59%、98.46% | [ |
HFLM | TODGA | Nd | 稀土浓度1g·L-1、3.5mol·L-1硝酸时,萃取率接近100% | [ |
HFLM | PC-88A | Dy | 0.3mol·L-1硝酸时,通过二级萃取可从含有20%Dy的FeNdB磁铁中回收高纯度Dy(>97%) | [ |
类型 | 载体 | 稀土金属 | 主要研究结果 | 文献 |
---|---|---|---|---|
ELM | 苯胺 | RE | 表面活性剂T154、有机相磺化煤油时,可从磷矿浸取液中萃取出93%的混合RE | [ |
ELM | Cyanex272 | Dy | 表面活性剂Span80/85、有机相煤油时,萃取率99.6% | [ |
EPLM | P507 | Y/La/Sm/Al | 金属总浓度1.22g·L-1、电压4.5~5kV时,回收率分别为97.7%、90.3%、19.7、95.1% | [ |
EPLM | PMBP | Sc | 稀土浓度10mg·L-1、电压5kV时,萃取率96.9% | [ |
BOLM | N1923 | RE/Al | 稀土浓度116.68mg·L-1、Al浓度27.7mg·L-1时,RE/Al选择性为44.89,稀土回收率为84.4% | [ |
BOLM | P507 | RE | 稀土浓度116.68mg·L-1时,稀土回收率为90%以上 | [ |
FSLM | D2EHPA | Eu | PVDF为膜骨架、稀土浓度0.1mmol·L-1时,萃取率94.2% | [ |
FSLM | TODGA | RE | PVDF为膜骨架、稀土浓度72.4mg·L-1时,可从含有Ca/Mg/Fe/RE的磷矿模拟废液中萃取出96.3%的RE | [ |
HFSLM | PC-88A | Nd | 4mol·L-1硝酸时,萃取率95%,反萃率87% | [ |
HFSLM | D2EHPA | Nd/Pr/Dy | 2mol·L-1硝酸时,萃取率分别58.62%、85.59%、98.46% | [ |
HFLM | TODGA | Nd | 稀土浓度1g·L-1、3.5mol·L-1硝酸时,萃取率接近100% | [ |
HFLM | PC-88A | Dy | 0.3mol·L-1硝酸时,通过二级萃取可从含有20%Dy的FeNdB磁铁中回收高纯度Dy(>97%) | [ |
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