4.6 Article

Refining of Precious Metal Bearing Materials from Secondary Sources-Methanesulfonic Acid Leaching of Raw Silver Granules as a Promising Approach towards a Green Way of Silver Refining

Journal

MATERIALS
Volume 14, Issue 20, Pages -

Publisher

MDPI
DOI: 10.3390/ma14206095

Keywords

hydrometallurgy; raw silver refining; leaching; methanesulfonic acid; hydrogen peroxide; green metallurgy

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The state-of-the-art technology Moebius-electrolysis for raw silver refining has drawbacks from both technological and ecological perspectives. The increasing concentrations of critical impurities in raw silver, such as palladium, pose challenges for future refining processes. Methanesulfonic acid (MSA) shows promise as a base chemical for a more environmentally friendly and efficient refining method, with leaching experiments showing high silver leaching yields at elevated temperatures and solid concentrations.
The state-of-the-art technology of raw silver refining in a silver nitrate-based electrorefining process (Moebius-electrolysis) is accompanied by several disadvantages, both from a technological and from an ecological point of view. In addition, increasing concentrations of critical impurities from secondary sources, like palladium, in raw silver are a further challenge for the future of silver refining. Thus, there is strong motivation for the development of an adequate, alternative process of raw silver refining to substitute the existing Moebius-electrolysis. Due to its less environmentally toxic character and the high aqueous solubility of its silver salt, methanesulfonic acid (MSA) is a possible base chemical for the design of an efficient refining method based on leaching of raw silver followed by electrowinning, with less ecological and technological complications. In this paper the results of some fundamental investigations on the leaching of raw silver granules, containing approx. 94% silver, with methanesulfonic acid and hydrogen peroxide as an oxidation agent are presented. Agitation leaching experiments were conducted on a laboratory scale and the effects of the solid concentration, the hydrogen peroxide dosage and the temperature as leaching parameters were studied. The obtained results indicate that silver leaching yields of more than 90% are achievable with leaching at elevated temperatures of 65 & DEG;C or 80 & DEG;C, solid concentrations of 500 g/L and at a stoichiometric H2O2:Ag-ratio of 3:1. Increased solid concentrations greater than 500 g/L and elevated temperatures of 65 & DEG;C or 80 & DEG;C additionally improved the selectivity of the process regarding the leaching of Pd.

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