应用化学 ›› 2020, Vol. 37 ›› Issue (7): 803-809.DOI: 10.11944/j.issn.1000-0518.2020.07.190356

• 研究论文 • 上一篇    下一篇

“抑制-萃取”法从含铁酸溶液中选择性提钒

阳征斐a, 陈友顺a, 张豪杰a, 刘志雄a, 颜文斌a,b,c, 李飞a,b,c,*   

  1. 吉首大学a化学化工学院;b锰-锌-钒产业技术协同创新中心;c矿物清洁生产与绿色功能材料开发湖南省重点实验室 湖南 吉首 416000
  • 出版日期:2020-07-01 发布日期:2020-07-07
  • 通讯作者: 李飞,副教授; E-mail:113501005@csu.edu.cn; 研究方向:湿法冶金及相似元素分离
  • 基金资助:
    湖南省教育厅优秀青年项目(18B320)、锰-锌-钒产业技术协同创新中心“2011计划”资助项目、吉首大学科研启动项目(jsdxrcyjkyxm201701)资助

Selective Extraction of Vanadium from the Fe-Bearing Acidic Solution by Method of “Depressing Extraction-Extraction”

YANG Zhengfeia, CHEN Youshuna, ZHANG Haojiea, LIU Zhixionga, YAN Wenbina,b,c, LI Feia,b,c,*   

  1. aSchool of Chemistry and Chemical Engineering; bThe Collaborative Innovation Center of Manganese-Zinc-Vanadium Industrial Technologythe 2011 Plan of Hunan Province; cKey Laboratory of Mineral Cleaner Production and Exploit of Green Functional Materials in Hunan Province,Jishou University,Jishou,Hunan 416000,China
  • Published:2020-07-01 Online:2020-07-07
  • Contact: LI Fei, associate professor; E-mail:113501005@csu.edu.cn; Research interests:hydrometallurgy and separation of similar elements
  • Supported by:
    Supported by the Foundation of Educational Commission of Hunan Province(No.18B320), the Foundation of the Collaborative Innovation Center of Manganese-Zinc-Vanadium Industrial Technology(the 2011 Plan of Hunan Province), the Research Startup Foundation of Jishou University(No.jsdxrcyjkyxm201701)

摘要: 酸法浸出石煤提钒因具有环保、金属收率高的特点而备受关注,但同时进入母液的铁(高含量的Fe3+)严重影响了钒的富集和产品生产。 对此,本文提出一种基于“抑制-萃取”效应的钒/铁分离混合萃取体系(P507(2-乙基己基磷酸-单2-乙基己基酯)+ N235(三辛/癸烷基叔胺)+磺化煤油),并详细研究了各因素对钒铁分离和钒富集的影响规律。 结果表明,P507是钒铁萃取的主体,N235不具萃Fe3+能力,是产生抑制铁萃取的关键因素,其浓度越高铁萃取率越低;对于酸度较高(pH≤0.4)的原料液钒/铁的分离效果仍较好,这表明了该“抑制-萃取”混合萃取体系对高酸度浸出液钒/铁分离的适用性。 采用氨水从负载有机相中反萃取钒铁,当氨水浓度为6 mol/L时钒的反萃率99%以上,25 ℃,V(有机相)∶V(水相)=2∶1时的反萃液中钒质量浓度14.73 g/L,铁质量浓度小于0.022 g/L,m(V)/m(Fe)=669.5。 该“抑制-萃取”法分离钒/铁操作简单、经济高效,极具工业化前景。

关键词: 溶剂萃取, 抑萃效应, 钒铁分离, 赝反萃, 钒酸铵

Abstract: The extraction of vanadium from stone coal by acid leaching has attracted much attention because of its characteristic of environment friendly and high metal yield. However, the process is seriously affected by concentrated Fe3+ in the vanadium mother solution. In this paper, a system (P507(2-ethylhexylphosphonic acid mono-(2-ethylhexyl) ester)+N235(Trioctyl/tridecylaklylamines)+sulfonated kerosene) based on the “depressing extraction-extraction” effect was proposed to separate V from Fe. The influence of various factors on the separation and enrichment of V over Fe was studied in details. Results show that P507 is responsible for extraction of Fe and V, while N235 suppresses the extraction of Fe3+. The higher the concentration of N235, the less Fe3+ is extracted. The separation efficiency of V over Fe is high in the raw solution at pH≤0.4, demonstrating the applicability of the designed “depressing extraction-extraction” mixed extractants toward concentrated acid leaching solution. When 6 mol/L ammonia is used, more than 99% of vanadium can be stripped. Under the condition of 25 ℃, V(organic phase)∶V(aqueous phase)=2∶1 the stripping pregnant solution is obtained, in which the mass concentration of vanadium is 14.73 g/L, the mass concentration of iron is less than 0.022 g/L, and the mass ratio of vanadium to iron is more than 669.5. It is evident that the “depressing extraction-extraction” is a method of easy operation, being economic and efficient, and great industrial prospect.

Key words: solvent extraction, depressing extraction, separation of vanadium over iron, pseudo-stripping, ammonium vanadate