Method of recovery copper, nickel and noble metal in waste water and slag by combined technology of wet method and fire method
A combined process and precious metal technology, applied in the field of recycling copper, nickel and precious metals, can solve the problems of high cost, declining economic benefits, rising prices, etc., and achieve the effect of strong adaptability of raw materials and high comprehensive utilization rate of metals
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Embodiment 1
[0044] Raw material (neutralized slag containing nickel-copper wastewater) composition:
[0045] Ni8.20%, Cu6.33%, Fe3.50%, CaO3.0%, Cr2.25%, MgO0.2%,
[0046] al 2 o 3 0.10%Zn0.11%Au3.5g / tAg60.5g / tPd2.5g / t.
[0047] According to the process steps, it is described as follows:
[0048] (1) Leaching
[0049] The neutralized slag in the above waste water is stirred and leached.
[0050] Leaching technical conditions: Leaching agent: 98% sulfuric acid; add intermittently.
[0051] Leaching method: stirring leaching; stirring speed 80 rpm;
[0052] The volume of compressed air blown in is 55 liters / minute;
[0053] Endpoint pH: 1.3;
[0054] Leaching time: 2.5 hours.
[0055] Copper and nickel are separated after leaching.
[0056] (2) Separation of copper and nickel:
[0057] Copper and nickel separation technical conditions: A sulfide copper removal
[0058] Sodium sulfide concentration 15%;
[0...
Embodiment 2
[0104] Raw material (neutralized slag containing nickel-copper wastewater) composition:
[0105] Ni6.20%, Cu7.33%, Fe5.50%, CaO4.0%, Cr1.25%, MgO0.18%, Al 2 o 3 0.11%Zn0.13%Au3.29g / tAg70.6g / tPd3.05g / t.
[0106] According to the process steps, it is described as follows:
[0107](1) Leaching: stirring and leaching the above-mentioned waste water neutralized slag. Adjust the technical conditions according to the raw material situation. In order to ensure a higher leaching rate of nickel and copper and a lower leaching rate of iron, chromium and aluminum, the reaction time should be increased and the pH value of the solution should be increased. That is, keep the pH value at 1.5 during the leaching process, and continue to stir after the leaching is completed, and the time is increased by 1.0 hours.
[0108] Leaching technical conditions: terminal pH: 1.5;
[0109] Leaching time: 3.5 hours.
[0110] Other conditions are with embodiment 1.
[01...
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