Enhancing the separation performance of vanadium from a black shale leaching solution by supported liquid membrane using trialkylamine

被引:13
作者
Liu, Hong [1 ]
Zhang, Yi-min [1 ,2 ]
Huang, Jing [1 ]
Liu, Tao [1 ]
Xue, Nan-nan [1 ]
Luo, Da-shuang [1 ]
机构
[1] Wuhan Univ Sci & Technol, Sch Resources & Environm Engn, Hubei Collaborat Innovat Ctr High Efficient Utili, Hubei Prov Engn Technol Res Ctr High Efficient Cl, Wuhan 430081, Hubei, Peoples R China
[2] Wuhan Univ Technol, Sch Resources & Environm Engn, Wuhan 430070, Hubei, Peoples R China
基金
中国国家自然科学基金;
关键词
Vanadium separation; Flat sheet supported liquid membrane; Trialkylamine; Black shale; PHENYL PHOSPHORIC-ACID; FACILITATED TRANSPORT; STONE COAL; SELECTIVE SEPARATION; EXTRACTION; RECOVERY; MIXTURE; D2EHPA; VISCOSITIES; DENSITIES;
D O I
10.1016/j.cherd.2018.05.039
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
To enhance the separation efficiency of vanadium from impurities, the highly selective separation of vanadium from multiple impurities and the transport mechanism of vanadium from a black shale leaching-solution, by a supported liquid membrane (SLM) using trialkylamine (N235) as the carrier, were investigated. The effects of parameters such as feed-solution pH, carrier concentration, stripping-solution species, and diluent nature were studied. The separation performance of the SLM system for vanadium from the main impurities in the black shale acid leaching-solution-Fe, Al, P, Si, K, and Mg-was also discussed. The diffusion parameters and facilitated transport mechanism were evaluated using a first order kinetic model. By enhancing the mass transfer of vanadium and the competitive extraction between vanadium and the impurity ions, the performance of the SLM system for the separation of vanadium from the highly impure black shale leaching-solution was significantly improved. These results show that highly selective separation of vanadium from impurities can be achieved using the N235-SLM system, indicating promising prospects for application in the vanadium industry. (C) 2018 Published by Elsevier B.V. on behalf of Institution of Chemical Engineers.
引用
收藏
页码:262 / 270
页数:9
相关论文
共 37 条
[31]   Transport of cobalt(II) through a hollow fiber supported liquid membrane containing di-(2-ethylhexyl) phosphoric acid (D2EHPA) as the carrier [J].
Vernekar, Prasad V. ;
Jagdale, Yogesh D. ;
Patwardhan, Ashwin W. ;
Patwardhan, Anand V. ;
Ansari, Seraj A. ;
Mohapatra, Prasanta K. ;
Manchanda, Vijay K. .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 2013, 91 (01) :141-157
[32]   High-efficient and selective extraction of vanadium (V) with N235-P507 synergistic extraction system [J].
Xiong, Pu ;
Zhang, Yimin ;
Huang, Jing ;
Bao, Shenxu ;
Yang, Xiao ;
Shen, Chun .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 2017, 120 :284-290
[33]   Facilitated transport of phenol through supported liquid membrane containing bis(2-ethylhexyl) sulfoxide (BESO) as the carrier [J].
Yang, Xiangjun ;
Duan, Hengpan ;
Shi, Deqiang ;
Yang, Ruisi ;
Wang, Shixiong ;
Guo, Hong .
CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2015, 93 :79-86
[34]   Separation and recovery of vanadium from a sulfuric-acid leaching solution of stone coal by solvent extraction using trialkylamine [J].
Yang, Xiao ;
Zhang, Yimin ;
Bao, Shenxu ;
Shen, Chun .
SEPARATION AND PURIFICATION TECHNOLOGY, 2016, 164 :49-55
[35]   Intensification of Europium extraction through a supported liquid membrane using mixture of D2EHPA and Cyanex272 as carrier [J].
Zaheri, Parisa ;
Abolghasemi, Hossein ;
Maraghe, Mohammad Ghannadi ;
Mohammadi, Toraj .
CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2015, 92 :18-24
[36]   Chelating extraction of vanadium(V) from low pH sulfuric acid solution by Mextral 973H [J].
Zhang, Ying ;
Zhang, Ting-An ;
Dreisinger, David ;
Zhou, Weihua ;
Xie, Feng ;
Lv, Guozhi ;
Zhang, Weiguang .
SEPARATION AND PURIFICATION TECHNOLOGY, 2018, 190 :123-135
[37]   Thermodynamics of vanadium-sulfur-water systems at 298 K [J].
Zhou, Xuejiao ;
Wei, Chang ;
Li, Minting ;
Qiu, Shuang ;
Li, Xingbin .
HYDROMETALLURGY, 2011, 106 (1-2) :104-112