CIESC Journal ›› 2024, Vol. 75 ›› Issue (12): 4606-4616.DOI: 10.11949/0438-1157.20240495

• Separation engineering • Previous Articles     Next Articles

Electro-membrane extraction of Li() by Cyanex923/TBP/PHEN in collaboration with 2-thiophenecarbonyltrifluoroacetone

Xiaorong MENG1(), Chi SUN1, Yiwen LONG2   

  1. 1.School of Chemistry and Chemical Engineering, Xi'an University of Architecture and Technology, Xi'an 710055, Shaanxi, China
    2.Xi'an Runqin Water Limited Liability Company, Xi'an 710048, Shaanxi, China
  • Received:2024-05-06 Revised:2024-07-25 Online:2025-01-03 Published:2024-12-25
  • Contact: Xiaorong MENG

Cyanex923/TBP/PHEN协同2-噻吩甲酰三氟丙酮对Li()的电膜萃取研究

孟晓荣1(), 孙驰1, 龙伊文2   

  1. 1.西安建筑科技大学化学与化工学院,陕西 西安 710055
    2.西安润秦水务有限责任公司,陕西 西安 710048
  • 通讯作者: 孟晓荣
  • 作者简介:孟晓荣(1966—),女,博士,教授,mxr5@163.com
  • 基金资助:
    国家重点研发计划项目(2022YFC2904304-01);陕西省技术创新引导专项-重点研发计划三项改革项目(2023GXLH-060)

Abstract:

Lithium resource plays an important role in energy strategy. Membrane extraction technology is expected to solve the green sustainability problem of liquid lithium resource extraction. Binary composite extraction membranes PT-PIMs (PTC-PIM /PTT-PIM/PTP-PIM) with 2-thiophenoyltrifluoroacetone (TTA) synergistically solvated carriers [trialkylphosphine oxide mixture (Cyanex923)/tributyl phosphate (TBP)/phenanthroline (PHEN)] were prepared. The mass transfer behaviour of PT-PIMs-Li() system by electric field enhancement was investigated under optimized membrane phase conditions, and the stability and Li/Na/K selective separation performance of the kerosene-modified PK-PIMs-Li() system were evaluated. The results show that the membrane phase composition has a large effect on the mass transfer rate of Li(Ⅰ), the main extractant TTA plays a dominant role in Li(Ⅰ) mass transfer, and the mass transfer rate increases with the voltage. The permeability coefficient of PTC-PIM-Li(Ⅰ) system increases linearly with increasing voltage. The permeability coefficient of PTC-PIM-Li(Ⅰ) system is 33.20 μm·s-1 at 40 V. The permeation rate of Li(Ⅰ) in the PT-PIMs-Li(Ⅰ) system modified by kerosene decreased by <21% after four cycles; When the mass concentration ratio of Li(Ⅰ)∶Na(Ⅰ)∶K(Ⅰ) in liquid phase is 20∶20∶20, the separation factors SLi(Ⅰ)/Na(Ⅰ) and SLi(Ⅰ)/K(Ⅰ) of PT-PIMs system are 8.41, 4.88, 3.88 and 7.99, 4.64, 3.81, respectively, indicating the selective separation ability of Li. The combined permeability coefficient, stability and PK-PIMs-Li(Ⅰ) systems: PCK-PIM > PTK-PIM > PPK-PIM. This paper provides an important idea for sustainable extraction technology of lithium resources with green energy saving.

Key words: lithium, membrane, electro-membrane extraction, HTTA+synergist, stability, selectivity

摘要:

为强化2-噻吩甲酰三氟丙酮(HTTA)萃锂体系的性能,分别制备了以三烷基氧化膦、磷酸三丁酯、邻菲罗啉3种协萃剂配伍的聚氯乙烯基二元复合萃取膜(PT-PIMs),用于研究电场强化的膜萃取提锂技术。考察了膜相组成和操作电压对Li(Ⅰ)传质性能的影响规律,结合表面红外和扫描电镜对PT-PIMs的表征结果,初步探索了PTC-PIM-Li(Ⅰ)电膜萃取机制。研究表明:在PT-PIMs体系中,HTTA通过烯醇化结构与Li(Ⅰ)形成离子型配合物,在PT-PIMs中起主萃作用。3种协萃剂通过对HTTA的去质子化协同传质,并因协萃剂的碱性及塑化能力的不同而导致3种PT-PIMs对Li(Ⅰ)的传质能力不同。Li(Ⅰ)在膜界面的传质机制为“离子交换-中和”,外加电场通过强化TTA-Li(Ⅰ)配合物解离而促进传质,但同时会受限于PT-PIMs膜界面的化学反应速率。经煤油改性后的PT-PIMs-Li(Ⅰ)体系在四次循环后Li(Ⅰ)的渗透速率下降率<21%;在料液相 Li(Ⅰ)∶Na(Ⅰ)∶K(Ⅰ)质量浓度比为20∶20∶20时,PT-PIMs体系分离因子SLi(Ⅰ)/Na(Ⅰ)SLi(Ⅰ)/K(Ⅰ)分别为8.41、4.88、3.88和7.99、4.64、3.81,显示了Li选择性分离能力。

关键词: 锂, 膜, 电膜萃取, HTTA+协萃剂, 稳定性, 选择性

CLC Number: