Method for preparing nickel-zinc ferrite through pressure acid leaching of sulfide ore
A technology of nickel-zinc ferrite and sulfide ore, applied in chemical instruments and methods, inorganic chemistry, nickel compounds, etc., can solve the problems of difficult mixing of materials, large powder particles, high production costs, etc., and achieve good airtightness , Reduce the iron removal process, the effect of low cost
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Embodiment 1
[0049] According to the nickel zinc ferrite formula Ni 0.6 Zn 0.4 Fe 2 o 4 Weigh a certain proportion of nickel sulfide concentrate (Ni content 6.56%, Fe content 26.19%) and zinc sulfide concentrate (Zn content 50.08%, Fe content 6.77%), add the two minerals and a certain amount of sulfuric acid solution Into the autoclave, feed oxygen, and control the conditions of pressurized acid leaching: liquid-solid ratio 6:1, initial sulfuric acid concentration 180g / L, time 1.5h, temperature controlled at 160°C, pressure 0.8MPa, stirring rate 600r / min. The leaching rates of nickel, zinc and iron were 95.54%, 99.42% and 82.05%, respectively.
[0050] The leached pulp is filtered, the filter residue is washed and stockpiled, the washing water is returned to the oxygen pressure acid leaching process, the ferric iron in the solution is reduced with the raw material sulfide ore as the reducing agent, and the reduced filter residue is returned to the pressure leaching process for leachin...
Embodiment 2
[0052] According to the nickel zinc ferrite formula Ni 0.6 Zn 0.4 Fe 2 o 4 Weigh a certain proportion of nickel sulfide concentrate (Ni content 6.56%, Fe content 26.19%) and zinc sulfide concentrate (Zn content 50.08%, Fe content 6.77%), add the two minerals and a certain amount of sulfuric acid solution Into the autoclave, feed oxygen, and control the conditions of pressurized acid leaching: liquid-solid ratio 5:1, initial sulfuric acid concentration 220g / L, time 2h, temperature controlled at 200°C, pressure 1.2MPa, stirring rate 600r / min. The leaching rates of nickel, zinc and iron were 98.78%, 99.61% and 81.67%, respectively.
[0053] The leached pulp is filtered, the filter residue is washed and stockpiled, the washing water is returned to the oxygen pressure acid leaching process, the ferric iron in the solution is reduced with the raw material sulfide ore as the reducing agent, and the reduced filter residue is returned to the pressure leaching process for leaching....
Embodiment 3
[0055] According to the nickel zinc ferrite formula Ni 0.35 Zn 0.65 Fe 2 o 4 Weigh a certain proportion of nickel sulfide concentrate (Ni content 6.56%, Fe content 26.19%) and zinc sulfide concentrate (Zn content 50.08%, Fe content 6.77%), add the two minerals and a certain amount of sulfuric acid solution Into the autoclave, feed oxygen, and control the conditions of pressurized acid leaching: liquid-solid ratio 6:1, initial sulfuric acid concentration 200g / L, time 1.5h, temperature controlled at 160°C, pressure 1.0MPa, stirring rate 600r / min. The leaching rates of nickel, zinc and iron were 97.73%, 99.78% and 83.16%, respectively.
[0056] The leached pulp is filtered, the filter residue is washed and stockpiled, the washing water is returned to the oxygen pressure acid leaching process, the ferric iron in the solution is reduced with the raw material sulfide ore as the reducing agent, and the reduced filter residue is returned to the pressure leaching process for leach...
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