Method for recovering cobalt in cobalt-containing waste residues from zinc smelting
A zinc smelting and waste residue technology is applied in the field of recovering cobalt from zinc smelting cobalt-containing waste residue to achieve the effect of reducing separation and recovery costs
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Embodiment 1
[0023] Step 1 Ball milling: Weigh 2 tons of cobalt-containing waste slag from zinc smelting and add water for wet ball milling. The weight ratio of water: slag is 4.8:1; after ball milling, the particle size -200 mesh is greater than 60%, and the ore slurry is sent into 15m 3 Leach out the stirring tank and start stirring;
[0024] Step 2 leaching: Slowly add 1.54 tons of concentrated sulfuric acid with a weight percentage concentration of 93% to the leaching stirring tank; at the same time, heat the liquid in the leaching stirring tank, the reaction temperature is 65-75 ° C, the time for adding concentrated sulfuric acid is 1.5 hours, and the concentrated sulfuric acid is added After finishing, continue to stir and react to pH value 4.5; Obtain leaching pulp;
[0025] Step 3 press filter lead slag: put the leaching pulp obtained in step 2 into a filter press; obtain lead slag and leaching filtrate; lead slag is stored as a lead refining raw material for transportation; lead s...
Embodiment 2
[0034] Step 1 ball milling: Weigh 2 tons of cobalt-containing waste slag from zinc smelting and add water to carry out wet ball milling. The weight ratio of water: slag is 4.5:1; the rest is the same as in Example 1;
[0035] Step 2 leaching: add 1.46 tons of concentrated sulfuric acid to the leaching stirring tank; the time for adding the concentrated sulfuric acid is 1.0 hour, after adding the concentrated sulfuric acid, continue to stir and react until the pH value is 5.0; the rest are the same as in Example 1;
[0036] Step 3 press filter lead slag: with embodiment 1; Obtain lead slag 290kg, lead content is 31%;
[0037] Step 4 removes iron and manganese: the leaching filtrate that step 3 obtains enters 15m 3 Remove iron and manganese stirring tank, and analyze the iron and manganese content of the leaching filtrate. The measured iron and manganese contents in the leachate are 372mg / l and 390mg / l respectively, and the volume of the leaching liquid in the iron and manganese...
Embodiment 3
[0044] Step 1 ball milling: Weigh 2 tons of cobalt-containing waste slag from zinc smelting and add water to carry out wet ball milling. The weight ratio of water: slag is 5.5:1; the rest is the same as in Example 1;
[0045] Step 2 leaching: Add 1.50 tons of concentrated sulfuric acid to the leaching stirring tank; the time for adding the concentrated sulfuric acid is 80 minutes, after adding the concentrated sulfuric acid, continue to stir and react until the pH value is 4.7; the rest are the same as in Example 1;
[0046] Step 3 press filter lead slag: with embodiment 1; Get lead slag 260kg, lead content is 35%;
[0047] Step 4 removes iron and manganese: the leaching filtrate that step 3 obtains enters 15m 3 Remove iron and manganese stirring tank, and analyze the iron and manganese content of the leaching filtrate, the measured iron and manganese contents in the leach solution are 308mg / l and 320mg / l respectively, and the volume of the leaching liquid in the iron and mang...
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