Selective gold extraction from copper anode slime with an alcohol
a technology of copper anode slime and alcohol, applied in the direction of improving process efficiency, etc., can solve the problems of high solubility in the aqueous phase, complicated slime processing, and serious drawbacks
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example 1
Selectivity of Reagent for Au over Po-210
[0111]The leach liquor produced from the oxidative chlorination of decopperised slimes as described above was used for the following tests. The leach liquor was diluted to ˜160 mg / L Au in a series of solutions with varying hydrochloric acid concentrations (1-8 M HCl). The solutions were then contacted in separate tests with the same volume of organic solution. Two types of organic solutions were tested:[0112]i) 50% by volume of isodecanol (Exxal®10) in Escaid 500 (a low aromatic content hydrocarbon diluent)[0113]ii) 50% by volume of 2-ethyl hexanol in Escaid 500
The percentage extraction of Au and Po-210 as a function of HCl concentration is presented in Table 3 and it can be seen that provided the HCl concentration is controlled between 3-5 M, high Au extraction is achieved with high rejection of Po-210 to the residue.
TABLE 3Typical composition of anode slimes2-ethyl Hexanolisodecanol% Extraction% ExtractionHCl (M)Au210PoHCl (M)Au210Po1.0161....
example 2
Au Recovery and Purification with Solvent Extraction
[0114]Leach liquor obtained from oxidative chlorination of decopperised anode slimes containing 4.1% Au to cation ratio in solution was treated as follows. The leach liquor was contacted in a batch counter-current mode with an organic solution containing 50 vol. % isodecanol in Escaid 300 diluent in 4 extraction stages. Five cycles were carried out in order to ensure that that equilibrium had been reached. An A:O ratio (i.e. leach liquor to organic solution) of 4.5 was used. The feed to the solvent extraction process contained 6.5 g / L Au and the loaded organic obtained contained 30.3 g / L Au. Gold extraction of >96% was obtained. The loaded organic analysis is presented in Table 4, is and indicates an upgrade of Au relative to the major impurities, Se, Te, As and Sb from 4.1% to 82%. The loaded solvent was submitted to a further 7 stages of counter-current scrubbing with an hydrochloric acid solution, resulting in a further upgrade ...
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