Separation and recovery of vanadium from leached solution of spent residuehydrodesulfurization (RHDS) catalyst using solvent extraction

被引:38
|
作者
Kim, Hong-In [1 ]
Lee, Ki-Woong [1 ]
Mishra, Debaraj [1 ]
Yi, Kang-Myong [1 ]
Hong, Jeong-Hee [2 ]
Jun, Min-Kee [3 ]
Park, Hea-Kyung [3 ]
机构
[1] Sungeel Hitech Ltd, Ctr Res & Dev, Inchon 404250, South Korea
[2] KC Cottrell Co Ltd, Ctr Res & Dev, Seoul 121898, South Korea
[3] Hanseo Univ, Res Inst Catalyst Technol, Seosan 356706, Chungnam, South Korea
关键词
Leached solution; Organic acid; Oxalic acid; Solvent extraction; Stripping; SELECTIVE RECOVERY; MOLYBDENUM; METALS;
D O I
10.1016/j.jiec.2014.02.017
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
Leached solution, generated by oxalic acid washing of spent residue hydrodesulfurization (RHDS) catalyst, was used for separation and recovery of vanadium. First of all, solvent extraction, using mixture of 20% (v/v) Alamine-336 and 5% (v/v) tri-butyl phosphate (TBP) as a phase modifier, was conducted to extract molybdenum completely at pH 0.50. Then molybdenum-free solution was used for vanadium extraction at pH 1.25 with 20% Alamine-336 and 5% TBP. Stripping of vanadium from loaded organic solution was performed with 1.5 M H2SO4 at O/A phase ratio of 5:1 where more than 99% of vanadium was stripped in two stages. The stripped vanadium solution was further processed by precipitating with ammonium hydroxide to recover ammonium-meta-vanadate which was calcined to obtain vanadium pentoxide. Finally a conceptual process was established for recovery of high purity vanadium pentoxide from oxalic acid leached solution of spent residue hydrodesulfurization (RHDS) catalyst. (C) 2014 Published by Elsevier B.V. on behalf of The Korean Society of Industrial and Engineering Chemistry.
引用
收藏
页码:4457 / 4462
页数:6
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