CIESC Journal

• 分离工程 • 上一篇    下一篇

微乳液的增溶、相态及微乳液/中空纤维膜萃取钕

龚福忠;马培华;罗艳;刘力恒;张丽梅   

  1. 中国科学院青海盐湖研究所,青海 西宁 810008;中国科学院研究生院,北京 100049;广西大学化学化工学院,广西 南宁 530004

  • 出版日期:2006-03-25 发布日期:2006-03-25

SoSolubilization and phase behavior of nonionic water-in-oil microemulsion and its application to extraction of Nd3+ in hollow fiber modules

GONG Fuzhong;MA Peihua;LUO Yan;LIU Liheng;ZHANG Limei   

  • Online:2006-03-25 Published:2006-03-25

摘要: 通过考察非离子型微乳液体系(OP-4+OP-7)/ 苯甲醇/D2EHPA/煤油/盐酸中的混合表面活性剂OP-4[壬基酚聚氧乙烯(4)醚]和OP-7[壬基酚聚氧乙烯(7)醚]配比、盐酸浓度、温度和NaCl对盐酸增溶量的影响以及D2EHPA[二(2-乙基己基)磷酸]和盐酸浓度对体系相态的影响,制备了适合作为液膜分离介质的微乳液体系,同时提出了新的膜萃取过程:微乳液/中空纤维膜萃取,并用于稀土钕的萃取.结果表明,微乳液中盐酸的增溶量随混合表面活性剂HLB值以及盐酸浓度的增大而增大,随温度的升高、NaCl浓度的增大而减小;D2EHPA的加入有利于WinsorⅡ体系的形成;盐酸浓度小于6 mol•dm-3时也可形成WinsorⅡ体系,而盐酸浓度为7 mol•dm-3和8 mol•dm-3时则分别形成WinsorⅢ体系或WinsorⅠ体系;将W/O非离子型微乳液通过中空纤维膜从浓度为300 mg•dm-3的料液中萃取钕时,采用3个中空纤维膜器串连一次萃取即可使萃取率达95.3%,内相富集倍数18.1.该新膜萃取体系同时具有液膜与固膜萃取的优点,不需进行反萃操作.

Abstract: A nonionic microemulsion(ME) consisted of mixed surfactants named OP-4 [polyoxyethylene(4)nonylphenol] and OP-7[polyoxyethylene(7)nonylphenol], benzyl alcohol, D2EHPA[2-(2-ethylhexylphosphonic acid)], kerosene as well as HCl solution was prepared.The effects of mass ratio of OP-7 to OP-4,hydrochloric acid concentration,temperature,sodium chloride concentration on the solubilization of HCl solution and the effects of D2EHPA and HCl concentration on phase behaviors were invested.A new membrane-extraction process using the microemulsion as liquid membrane for neodymium extraction in hollow fiber membrane(HFM)was presented for the first time.The results showed out that the content of HCl solution in ME increased with increasing HLB values of mixed surfactants and hydrochloric acid concentrations.But the increase of temperature and NaCl concentration led to a decrease of the content of HCl solution in ME.It also revealed that the WinsorⅡsystem(equilibrium of W/O ME with excess aqueous solution) could form when HCl solution concentration was under 6 mol•dm-3. While the HCl solution concentration was 7 or 8 mol•dm-3, however, the Winsor Ⅲsystem(equilibrium of middle ME with both oil and aqueous solution) or the WinsorⅠsystem(equilibrium of O/W ME with excess oil)could form, respectively.As this new membrane-extraction technique was used for the extraction of Nd3+ from 300 mg•dm-3 feed solution, the extraction percentage reached as high as 95.3% and the concentration in receiving phase was 18.1 fold compared to their initial feed concentration after counter-current extraction with three-modules in tandem.This new membrane system has the advantages of both emulsion liquid membrane and solid membrane extraction.