Separation Of Zn, Co, And Ni Using Solvent Extraction Techniques (cefb7300-f881-4c58-b053-3847da285be7)

Society for Mining, Metallurgy & Exploration
E. H. Cho
Organization:
Society for Mining, Metallurgy & Exploration
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8
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366 KB
Publication Date:
Jan 1, 1993

Abstract

An acid mine drainage sludge sample containing 3.6% Mn, 0.18% Ni, 0.15% Co and 0.39% Zn was obtained from the central part of West Virginia and leached with sulfuric acid at pH 3 and at room temperature. Air was bubbled through the leach solution to precipitate the iron content from the solution at pH 4.5. The leach solution contained 258ppm Zn, 105ppm Ni, 90ppm Co and 2050ppm Mn. Three distinctive solvent extraction studies were performed to selectively extract these metal ions in a sequential operation with DEHPA, Cyanex 272, and then Lix 84. The AIO ratio was 1 and the extractants were diluted 10 times with kerosene. A study of solvent extraction with DEHPA showed that Zn could be extracted without Ni or Co up to pH 2.75. A pH of 2.75 is considered to be the optimum pH to maximize the selective separation of Zn from Mn. The separation factor of Co over manganese suggests that the two metal ions be extracted together by Cyanex 272. The separation factor of Co over Ni indicates that these two metal ions can be separated most effectively around pH 5.3. Also, Ni can be effectively extracted by Lix 84 above pH 5.5.
Citation

APA: E. H. Cho  (1993)  Separation Of Zn, Co, And Ni Using Solvent Extraction Techniques (cefb7300-f881-4c58-b053-3847da285be7)

MLA: E. H. Cho Separation Of Zn, Co, And Ni Using Solvent Extraction Techniques (cefb7300-f881-4c58-b053-3847da285be7). Society for Mining, Metallurgy & Exploration, 1993.

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