USING AN INTERDIGITAL MICROMIXER FOR SEPARATION OF In3+ FROM ZINC HYDROMETALLURGICAL PROCESS WITH D2EHPA AS AN EXTRACTANT

被引:1
作者
Li, C. [1 ,2 ,4 ]
Jiang, F. [1 ,2 ,3 ]
Ju, S. [1 ,3 ,4 ]
Peng, J. [1 ,2 ,3 ]
Wei, Y. [1 ,2 ,3 ]
Zhang, L. [1 ,2 ,3 ]
机构
[1] Yunnan Prov Key Lab Intensificat Met, Kunming 650093, Yunnan, Peoples R China
[2] Natl Local Joint Lab Engn Applicat Microwave Ener, Kunming 650093, Yunnan, Peoples R China
[3] Kunming Univ Sci & Technol, Key Lab Unconvent Met, Minist Educ, Kunming 650093, Yunnan, Peoples R China
[4] Kunming Univ Sci & Technol, Fac Met & Energy Engn, Kunming 650093, Yunnan, Peoples R China
基金
中国国家自然科学基金;
关键词
Interdigital micromixer; Solvent extraction; Mass transfer coefficient; Indium; Stripping; LIQUID-LIQUID-EXTRACTION; SOLVENT-EXTRACTION; MASS-TRANSFER; INDIUM; MICROCHANNELS; DISPERSION; RECOVERY;
D O I
10.1515/amm-2017-0128
中图分类号
TF [冶金工业];
学科分类号
0806 ;
摘要
Experiments were performed in an interdigital micromixer with 30 microchannels (40 mu m width of each channel) to separate In3+, Fe3+ and Zn2+ from sulfate solutions using Di-(2-ethylhexyl) phosphoric acid (D2EHPA) as the extractant. The effects of pH, extractant concentration and flow rate on the extraction efficiency and flow rate on mass transfer coefficient of In3+, Fe3+ and Zn2+ were investigated. At a phase flow rate of 7.0 mL/min and initial solution pH of 0.423, the extraction efficiency of In3+, Fe3+ and Zn2+ was 99.29%, 3.43% and 2.54%, respectively and mass transfer coefficient of In3+, Fe3+ and Zn2+ was 144.307 s(-1),1.018 s(-1) and 0.750 s(-1). Then, the loaded organic phase was stripped in an interdigital micromixer. At a phase flow rate of 9.0 mL/min and HCl concentration of 160 g/L, stripping efficiency of In3+ was 98.92% and mass transfer coefficient of In3+ was 169.808 s(-1), while concentration of Fe3+ and Zn2+ was lower than 0.005 g/L with good separation of In3+ from Fe3+ and Zn2+.
引用
收藏
页码:873 / 878
页数:6
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