离子液体调控耐酸纳滤膜结构与性能的微观机制
批准号:
22108282
项目类别:
青年科学基金项目(C类)
资助金额:
30.0 万元
负责人:
单玲珑
依托单位:
学科分类:
分离工程
结题年份:
2024
批准年份:
2021
项目状态:
已结题
项目参与者:
单玲珑
中文摘要
针对稀土萃取分离所采用的酸性萃取剂皂化工艺需要消耗大量酸碱,成本高且会产生大量氨氮废水的问题,本研究创新性地提出采用纳滤膜技术将萃余相中H+进行分离而实现的无皂化绿色萃取分离新工艺,并基于此开展新型耐酸、高通量、高REn+/H+选择性纳滤膜的研究。拟通过功能化离子液体实现纳滤膜表界面性质、膜孔道结构和耐酸性的精细调控,首先从分子层面设计并合成具有特定官能团(反应基团、耐酸基团、荷正电基团等)的功能化离子液体膜材料作为界面聚合水相单体,筛选与之匹配的油相单体反应成膜,并对膜性能、表界面性质、膜结构等进行分析表征。揭示离子液体支链种类、阴阳离子结构、氢键-静电耦合作用等对其从水相到油相的扩散行为影响规律,探究扩散行为对膜结构构筑的控制机理,深入阐明离子液体微结构对膜表界面性质和耐酸性质的微观调控机制,建立完善的耐酸高通量纳滤膜制备方法。
英文摘要
The acid extractant saponification process in rare earth extraction separation consumed a lot of acid and alkali, has a high cost and produced a lot of ammonia nitrogen wastewater. In this study, a new unsaponified rare earth green extraction separation process was proposed innovatively by using nanofiltration membrane technology to separate H+ in the raffinate phase, and carried out the research of novel acid-resistant, high-flux, high REn+/H+ selectivity nanofiltration membrane based on this. In order to realize the fine control of the surface-interface properties, pore structure and acid resistance of nanofiltration membrane, functional ionic liquid membrane materials with specific functional groups (reaction group, acid resistance group, positively charged group, etc.) were designed and synthesized at the molecular level as interfacial polymerization monomer in aqueous phase, then select the matched oil phase monomer to form the membrane, the surface-interface properties and membrane structure were analyzed and characterized. The effects of branched chain types, cation anion structure, hydrogen bond-electrostatic coupling on the diffusion behavior of ionic liquids from aqueous phase to oil phase were revealed, and the regulation mechanism of diffusion behavior on the precise construction of membrane structure was explored. The micro regulation mechanism of ionic liquid microstructure on the surface interface properties and acid resistance properties of membrane was deeply elucidated, finally established an acid resistant high flux nanofiltration membrane preparation method.
稀土具有优异的物理化学性能,已经被广泛应用于石油、化工、冶金、磁性材料等众多领域。稀土分离的关键在于萃取,萃取过程采用的酸性萃取剂(如P507、P204等)皂化工艺需要消耗大量酸碱,每生产1吨稀土产品需要消耗约10吨浓盐酸和3吨烧碱,占直接成本的50%-70%,同时会产生大量氨氮废水。本研究创新性地提出采用纳滤膜技术将萃余相中H+进行分离而实现的无皂化绿色萃取分离新工艺,并基于此开展新型耐酸、高通量、高REn+/H+选择性纳滤膜的研究。通过模拟计算揭示了离子液体支链种类、阴阳离子结构、氢键-静电耦合作用等对其从水相到油相的扩散行为影响规律,探究离子液体微结构对膜表界面性质和膜结构的微观调控机制。设计制备了两种耐酸纳滤膜,一种为基于三嗪环的离子液体型耐酸纳滤膜(AEMIC-PEI-CC),三嗪环中N原子上共有三对未配位的电子对,形成的共轭结构,可降低分子总能量并增加了化学稳定性。相对于未采用离子液体调控的膜,AEMIC-PEI-CC纳滤膜的通量从58.2提高到79.1 L m-2h-1bar-1, H+/Y3+选择性为39.0,膜通量是商业纳滤膜的5-30倍左右。其可在pH=1的HCl-YCl3溶液中稳定运行30天。此外还开发了基于聚磺酰胺的耐酸纳滤膜(PEI-BTSC/PES膜)。对膜表面形貌、厚度、离子液体在膜中排布结构、膜表界面亲疏水性、表面能等进行系统分析。该膜对稀土离子截留率为95.5%,通量为57.0 L h-1 m-2 bar-1。BTSC单体独特的共振结构、反馈π键和大位阻增强了膜的耐酸性,使PEI-BTSC/PES膜在72天的强酸浸泡测试后仍保持94%的YCl3截留率。进一步,与稀土友力公司合作,实现了纳滤膜和萃取工艺集成优化,酸去除率>85%,负载有机相可直接用于后续萃取,稀土离子截留率>94.6%,长时间运行稳定超过1000小时,酸度恢复的萃余液可进行回用,成功开发了无皂化稀土萃取工艺。
纳滤膜中水分子的有序排列及传输行为研究
-
批准号:22578459
-
项目类别:面上项目
-
资助金额:50.00万元
-
批准年份:2025
-
负责人:单玲珑
-
依托单位:
国内基金
海外基金