2003Solvent Extraction and Ion ExchangeRequires access

Scrubbing of Cadmium and Nickel from Cyanex 272 Loaded with Cobalt

Carlos A. Nogueira, Paula C. Oliveira, Fátima Pedrosa

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Abstract

Abstract A process for the scrubbing of cadmium and nickel from Cyanex 272 loaded with cobalt was studied and is presented in this paper, as a part of a global solvent extraction process proposed for the recycling of spent Ni‐Cd batteries. After cadmium recovery in a first extraction circuit, the resulting solution containing about 80 g/L Ni, 1 g/L Co, and a residual Cd concentration of 0.10 g/L is processed in the second circuit where cobalt is extracted by 0.5 M Cyanex 272. The resulting organic phase containing about 7 g/L Co is contaminated with about 2 g/L Ni and 0.5 g/L Cd. The removal of nickel was successfully attained by scrubbing with cobalt sulphate solutions containing more than 8.7 g/L Co, at organic/aqueous (O/A) = 4 (95–98% efficiency in a single stage), while cadmium removal by this process was inefficient. The scrubbing of cadmium was achieved with high efficiency using aqueous complexing agents, namely 1 M sodium thiosulphate or 3 M ammonium chloride (scrubbing efficiencies of 97% and 80...

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Abstract A process for the scrubbing of cadmium and nickel from Cyanex 272 loaded with cobalt was studied and is presented in this paper, as a part of a global solvent extraction process proposed for the recycling of spent Ni‐Cd batteries. After cadmium recovery in a first extraction circuit, the resulting solution containing about 80 g/L Ni, 1 g/L Co, and a residual Cd concentration of 0.10 g/L is processed in the second circuit where cobalt is extracted by 0.5 M Cyanex 272. The resulting organic phase containing about 7 g/L Co is contaminated with about 2 g/L Ni and 0.5 g/L Cd. The removal of nickel was successfully attained by scrubbing with cobalt sulphate solutions containing more than 8.7 g/L Co, at organic/aqueous (O/A) = 4 (95–98% efficiency in a single stage), while cadmium removal by this process was inefficient. The scrubbing of cadmium was achieved with high efficiency using aqueous complexing agents, namely 1 M sodium thiosulphate or 3 M ammonium chloride (scrubbing efficiencies of 97% and 80...

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Available abstract

Abstract A process for the scrubbing of cadmium and nickel from Cyanex 272 loaded with cobalt was studied and is presented in this paper, as a part of a global solvent extraction process proposed for the recycling of spent Ni‐Cd batteries. After cadmium recovery in a first extraction circuit, the resulting solution containing about 80 g/L Ni, 1 g/L Co, and a residual Cd concentration of 0.10 g/L is processed in the second circuit where cobalt is extracted by 0.5 M Cyanex 272. The resulting organic phase containing about 7 g/L Co is contaminated with about 2 g/L Ni and 0.5 g/L Cd. The removal of nickel was successfully attained by scrubbing with cobalt sulphate solutions containing more than 8.7 g/L Co, at organic/aqueous (O/A) = 4 (95–98% efficiency in a single stage), while cadmium removal by this process was inefficient. The scrubbing of cadmium was achieved with high efficiency using aqueous complexing agents, namely 1 M sodium thiosulphate or 3 M ammonium chloride (scrubbing efficiencies of 97% and 80...

Key concepts: Cobalt, Chemistry, Nickel, Cadmium, Data scrubbing, Nuclear chemistry, Metallurgy, Radiochemistry

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