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HYDROMETALLURGICAL TREATMENT OF E-SCRAP

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HYDROMETALLURGICAL TREATMENT OF E-SCRAP ( hydrometallurgical-treatment-e-scrap )

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glycol ether) and OREPREPĀ® F549 (glycol), were tested. Moreover, Ammonium lignin sulfonate, starch, and Na2S were investigated as the depressants. Fig. 5.8 indicates that the metal distribution is fairly sensitive to pH in the extremely acidic solution; however, beyond pH 7, as pH continues to increase, the metal distribution in the sink appears to be constant. The reason that the metallic elements could be mostly recovered in the acidic solution is that nothing could float because of the depressing effect at the lower pH. It is observed that there is no selectivity with Frother 70 alone. It is necessary to note that at the low pH, the sum of the float and the sink is significantly lower than the original feed mass, probably due to the reaction between the active metals (such as zinc and iron) and acids that are utilized to adjust the solution pH. A series of tests was conducted to investigate the effect of the addition of Na2S, given that Na2S is considered a depressant to depress gold in copper-gold processing plants. 100.00 90.00 80.00 70.00 60.00 50.00 40.00 30.00 20.00 10.00 0.00 0 1000 2000 3000 4000 Magnetic field (gauss) Fe Cu Ni Au Ag Figure 5.7 Metals retained in the non-magnetic fraction as a function of magnetic field The microflotation tests as a function of Na2S concentration were performed at pH 10. Fig. 5.9 presents that at the 10-1 M Na2S concentration, approximately 60% of the copper and silver 59 Metal in non-magnetic fraction (%)

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