A method for efficiently recovering zinc from zinc leaching residues
A zinc leaching residue and high-efficiency technology, applied in the field of hydrometallurgy zinc, can solve problems such as low zinc leaching rate, and achieve the effects of improving separation performance, improving recovery rate and reducing production cost
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Embodiment 1
[0026] Step 1: Mix the zinc leaching slag and sulfuric acid evenly at a roasting temperature of 200°C, the amount of sulfuric acid is 60% of the mass of the zinc leaching slag, and roast in an atmosphere furnace with a preset temperature of 200°C under normal pressure 3h;
[0027] Step 2, after the roasting is completed, take out the calcined sand, cool and grind;
[0028] Step 3, at normal temperature and pressure, put the ground calcined sand into a container filled with tap water, then place the container in a parallel magnetic field with a magnetic induction intensity of 3T, stir and leaching at a stirring speed of 200r / min, and stir The direction should make the positive ions generate upward Lorentz force, the volume-to-mass ratio of liquid to solid during water leaching is 3:1; the leaching time is 1h;
[0029] Step 4: After the leaching is completed, solid-liquid separation is carried out.
[0030] At this time, the zinc leaching rate was 85.3%.
Embodiment 2
[0032] Step 1: Mix the zinc leaching slag and sulfuric acid evenly at a roasting temperature of 300°C, the amount of sulfuric acid is 80% of the mass of the zinc leaching slag, and roast in an atmosphere furnace with a preset temperature of 300°C under normal pressure 2.5 hours;
[0033] Step 2, after the roasting is completed, take out the calcined sand, cool and grind;
[0034] Step 3, at normal temperature and pressure, put the ground calcined sand into a container filled with tap water, then place the container in a parallel magnetic field with a magnetic induction intensity of 3T, stir and leaching at a stirring speed of 500r / min, and stir The direction should make the positive ions produce upward Lorentz force, the volume-to-mass ratio of liquid to solid during water leaching is 6:1; the leaching time is 1h;
[0035] Step 4: After the leaching is completed, solid-liquid separation is carried out.
[0036] At this time, the zinc leaching rate was 92.3%.
Embodiment 3
[0038] Step 1: Mix the zinc leaching slag and sulfuric acid evenly at a roasting temperature of 250°C, the amount of sulfuric acid is 70% of the mass of the zinc leaching slag, and roast in an atmosphere furnace with a preset temperature of 250°C under normal pressure 2.5 hours;
[0039] Step 2, after the roasting is completed, take out the calcined sand, cool and grind;
[0040] Step 3, at normal temperature and pressure, put the ground calcined sand into a container filled with tap water, then place the container in a parallel magnetic field with a magnetic induction intensity of 2T, stir and leaching at a stirring speed of 500r / min, and stir The direction should make the positive ions generate upward Lorentz force, the volume-to-mass ratio of liquid to solid during water leaching is 4:1; the leaching time is 1h;
[0041] Step 4: After the leaching is completed, solid-liquid separation is carried out.
[0042] At this time, the zinc leaching rate was 98.2%.
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