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摘要:
The equilibrium of extraction of V(IV) in the V(IV)- SO42- (H+, Na+)-Cyanex 301 (HA)-kerosene system has been studied. Significant extraction occurs above pH 1 within 10 min. CD (extraction ratio at constant pH(eq) and [HA](o,eq)) value is slightly decreased with increasing [V(IV)](ini). CD is found to be directly proportional to [H+]-n (n ≤ 2), [HA] 2 and (1+1.58 [SO42-]). The process is endothermic (DH = 16 kJ/mol). Apparent Kexvalues at 303 K are 10-1.419 and 10-0.94 in 0.10 and 1.50 mol/L SO42- medium, respectively. The loading capacity is calculated to be7.87 gV(IV) per100 g Cyanex 301. Kerosene appears as the best diluent. Stripping to the extents of 100%, 94% and 97.7% are possible in single stage by 1 mol/L H2SO4, HCl and HNO3, respectively. Separations of V(IV) from Cu(II) (at pH 0), Zn(II) (at pH 0.5) and Fe(III) (at pH 1.0) by Cyanex 301 are possible.
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篇名 Liquid-Liquid Extraction of V(IV) from Sulphate Medium by Cyanex 301 Dissolved in Kerosene
来源期刊 有色冶金(英文) 学科 化学
关键词 Extraction EQUILIBRIUM Vanadium(IV) CYANEX 301 KEROSENE Sulphate
年,卷(期) 2013,(1) 所属期刊栏目
研究方向 页码范围 21-29
页数 9页 分类号 O6
字数 语种
DOI
五维指标
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研究主题发展历程
节点文献
Extraction
EQUILIBRIUM
Vanadium(IV)
CYANEX
301
KEROSENE
Sulphate
研究起点
研究来源
研究分支
研究去脉
引文网络交叉学科
相关学者/机构
期刊影响力
有色冶金(英文)
季刊
2168-2054
武汉市江夏区汤逊湖北路38号光谷总部空间
出版文献量(篇)
48
总下载数(次)
0
总被引数(次)
0
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