Method for bioleaching a metal present in a material
a metal and metal technology, applied in the field of methods, can solve the problems of reducing the profitability of these processes, reducing the reliability of microbial organisms, and inhibiting the growth and/or activity of microorganisms,
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example 1
Recovery of Copper from Brake Pad Dust
[0100]The waste treated is brake pad dust; this pulverulent material results from the automobile industry, and in particular from the steps of polishing, reaming and finishing treatment of the parts in question. The composition of the materials can vary according to the evolution of motor vehicle braking technologies and the batches of materials under consideration. The residue exploited in the context of this example has the following elemental composition as % by weight: Cu 15%, Fe 10%, Zn 2%, Mg 4.5%, Al 5%, but also Sb 0.4%, As 0.2%, Pb 0.5%, and other elements in trace amounts or in insignificant amount. The process is applicable to all types of waste described in this patent.
[0101]The bacteria exploited in this example are part of the class of iron(II)-oxidizing acidophilic bacteria: Acidiferrobacter thiooxydans (DSM 2392), Acidithiobacillus ferrooxidans (DSM 11477), Leptospirillum ferrooxidans (DSM 2391). These acidophilic bacteria have a...
example 2
Recovery of Non-Ferrous Metals, and of Noble Metals of Interest, by Bioleaching Ground Mobile Telephone Materials
[0106]This second example consists of the use of embedded acidophilic bacteria in order to leach heavy metals such as copper combined, in the structure of the waste, with noble metals such as gold. This makes it possible to bioleach the copper but also a fraction of the gold by acidolysis. This example is illustrated by the treatment of a material resulting from the grinding of mobile telephones (grinding of whole mobile telephones, of random brands and models, to an average particle size of 1 mm), with an initial concentration of Au of 221 mg / kg and of Cu of 69 g / kg. For this type of waste, it is not necessary to perform a separation or a preconditioning; however, an acidification of the waste is carried out. The addition of iron in FeSO4.7H2O form is essential given the absence of iron intrinsic to the waste. The process will therefore be carried out in two steps: oxida...
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