Extraction of vanadium from chloride solution with high concentration of iron by solvent extraction using D2EHPA
Extraction of vanadium from chloride solution with high concentration of iron by solvent extraction using D2EHPA
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使用 D2EHPA 溶剂萃取从高浓度铁氯化物溶液中提取钒
DOI:
10.1016/j.seppur.2014.01.031
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发表时间:
2014
影响因子:
8.6
通讯作者:
Yu Ping
中科院分区:
文献类型:
--
作者:
Hu Guoping;Chen Desheng;Wang Lina;Liu JingChong;Zhao Hongxin;Liu Yahui;Qi Tao;Zhang Changqiao;Yu Ping
Vanadium (IV) bearing chloride solution with the Fe (II)/V (IV) mass ratio of 60 was prepared to simulate the acidic liquor by hydrochloric acid leaching of reduced vanadium-bearing titanomagnetite. Extractant of bis (2-ethylhexyl) phosphoric acid (D2EHPA) was used to extract vanadium from the solution. Under the optimal extraction conditions of equilibrium H+concentration of 0.27–0.42 mol/L, D2EHPA concentration (v/v, diluted in n-heptane) of 10%, extraction temperature of 20–25 °C, equilibrium time of 60 min, phase ratio (O/A) of 1:1, more than 99% of vanadium can be extracted. Loaded organic phase were stripped by dilute H2SO4solution under the optimal stripping conditions of H2SO4concentration of 20 wt.%, phase ratio (O/A) of 10:1, stripping time of 120 min, and 98% of vanadium can be stripped. The concentrations of V and Fe in the stripping solution were 13.0 g/L and 3.9 g/L, respectively. V2O5products with purity of 99.2% were obtained after oxidation, precipitation and calcination. The overall separation coefficient of V and Fe was 200. Experimental results indicated that V (IV) can be also separated from other metal ions such as Mg (II), Ni (II), Zn (II), Ca (II), Al (III) and Cu (II) in the chloride solution. A flow sheet on the recovery of vanadium from vanadium-bearing chloride solution containing high concentration of iron was proposed.