Method for acid-free leaching of cobalt intermediate product from sulfate
A technology of acid leaching and sulfate, applied in the direction of improving process efficiency, etc., can solve the problems of ammonia nitrogen or sodium pollutants, large consumption of auxiliary materials, large consumption of acid and alkali, etc., achieve good filtration performance, high-efficiency leaching, avoid The effect of alkali consumption
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Embodiment 1
[0036] This specific embodiment is the method for extracting the cobalt intermediate product by sulfate acid-free leaching, and its specific steps are:
[0037] Step 1, batching; Thick cobalt hydroxide and the cobalt leaching solution containing ferrous sulfate (Fe in its solution 2+ The concentration is 30g / L) according to the molar ratio of cobalt element and ferrous sulfate molar ratio is 0.8:1 to carry out proportioning and mixing, it is added in the leaching tank;
[0038]Step 2, acid-free leaching; blow oxygen into the mixed materials in step 1, and carry out leaching at a temperature of 90°C for 2 hours, and control the liquid-solid ratio during the leaching process to 10; at the same time, during the leaching process, By adding ferrous sulfate or cobalt intermediates, the cobalt intermediates are fully leached, and the pH of the solution when the cobalt intermediates are fully leached is controlled to be 3.0-3.5, Fe 2+ If the content is less than 0.1g / L, the leaching ...
Embodiment 2
[0041] This specific embodiment is the method for extracting the cobalt intermediate product by sulfate acid-free leaching, and its specific steps are:
[0042] Step 1, batching; Thick cobalt carbonate and ferrous sulfate solution (Fe in its solution 2+ The concentration is 32g / L) according to the molar ratio of cobalt element and ferrous sulfate molar ratio 1:1, mix it, and add it into the leaching tank;
[0043] Step 2, acid-free leaching; blow oxygen into the mixed materials in step 1, and carry out leaching at a temperature of 85°C for 5 hours, and control the liquid-solid ratio during the leaching process to be 7; at the same time, during the leaching process, By adding ferrous sulfate or cobalt intermediates, the cobalt intermediates are fully leached, and the pH of the solution when the cobalt intermediates are fully leached is controlled to be 3.0-3.5, Fe 2+ If the content is less than 0.1g / L, the leaching is complete;
[0044] Step 3: Filtration; solid-liquid separa...
Embodiment 3
[0046] This specific embodiment is the method for extracting the cobalt intermediate product by sulfate acid-free leaching, and its specific steps are:
[0047] Step 1, batching; Thick cobalt hydroxide and the cobalt leaching solution containing ferrous sulfate (Fe in its solution 2+ The concentration is 35g / L) according to the molar ratio of cobalt element and ferrous sulfate molar ratio is 1.05:1 carry out proportioning mixing, it is added in the leaching tank;
[0048] Step 2, acid-free leaching; air is blown into the mixed materials in step 1, and leaching is carried out at a temperature of 90°C for 6 hours, and the liquid-solid ratio during the leaching process is controlled to be 6; at the same time, during the leaching process, By adding ferrous sulfate or cobalt intermediates, the cobalt intermediates are fully leached, and the pH of the solution when the cobalt intermediates are fully leached is controlled to be 3.0-3.5, Fe 2+ If the content is less than 0.1g / L, the ...
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