Commercially available zinc and copper concentrates usually contain a significant amount of valuable metals such as lead, silver or indium, which accumulate in the solid waste from both hydrometallurgical and pyrometallurgical production processes.
Recovering these metals from the mentioned processes gives the possibility of offering waste to be an additional source of revenue for refineries, based either on the production of metal ingots or the sale of concentrates with a high market value. Moreover, it provides the possibility of reducing the volume of waste generated.
The Proprietary Technology Development Division (DDTP) has developed a lead and silver recovery process based on hot brine leaching followed by precipitation of the valuable metalsThe process can be applied to different sorts of metallurgical waste (oxides, sulphides, jarositic waste, and more), with certain variations to its basic structure depending on the type of waste to treat and the metals being targeted..
Performed in chloride medium (hot brine), in order to allow lead, silver and other metals pass into solution. The leaching conditions and the use of additives may vary depending on the nature of the material. ,
Performed by adding carbonate to give a first solid containing all the lead and silver from the previous solution.
The solid is treated to remove any contaminants and yielding a high grade lead-silver concentrate and a purity that allows to feed it directly to a melting furnace , being free of chlorides and sulfates.
It allows the regeneration of the reaction medium, closing the hot brine circuit and thus consumptions and effluent generation minimization. It is essentially a matter of removing dissolved sulfates from previous stages, as liquid or solid sodium sulfate purge.
The following figure shows a schematic of the process ECOLEADTM by identifying the key stages:
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