Method for treating nickel sulfide ore biological heap leaching solution
A nickel sulfide ore and treatment method technology, applied in the direction of process efficiency improvement, etc., can solve the problems of high recovery rate of valuable metals, difficulty in nickel/magnesium separation, small reagent consumption, etc., and achieve high recovery rate and low treatment cost The effect of low and strong economic benefits
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[0022] Example 1
[0023] (1) A proper amount of limestone powder (with a particle size of less than 120 mesh) is added into water to slurry, and the slurry-to-solid ratio is 3:1.
[0024] (2) Leach the biopile to about 1m 3 Enter into the iron removal tank, pass in an appropriate amount of air and stir, add the limestone powder slurry to the reaction kettle in the iron removal tank at a certain flow rate (60-100L / h), and control the pH of the reaction liquid in the reaction kettle to 2-4.5 And aeration oxidation time is 2-6 hours, make the Fe in the bio-pile leaching solution at room temperature 2+ Oxidized to Fe 3+ , And hydrolyzed to produce Fe(OH) 3, Co-precipitated with the calcium sulfate produced in the heap leaching solution to form a thick iron slag slurry.
[0025] Table 1 The chemical composition of the supernatant of the heap leaching solution after regular warming
[0026] ingredient
[0027] (3) Fill the ion exchange column with 20-25L of the transformed special resin...
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[0034] Example 2
[0035] (1) First oxidize the heap leaching solution with self-cultured bacteria for a certain period of time, and analyze Fe 3+ / Fe 2+ , The value ratio is greater than 9 for standby.
[0036] (2) Leach the biopile to about 1m 3 Enter into the iron removal tank, pass in an appropriate amount of air and stir, add the limestone powder slurry to the reactor in the iron removal tank at a certain flow rate (60-100L / h), and control the pH of the reaction liquid in the reactor to be about 4.2 and The aeration oxidation time is 2 hours, and the remaining Fe 2+ Oxidized to Fe 3+ , And hydrolyzed to produce Fe(OH) 3, Co-precipitated together with calcium sulfate produced in the heap leaching solution to form a thick iron slag slurry.
[0037] Table 3 The chemical composition of the supernatant of the heap leaching solution after regular warming of iron
[0038] ingredient
[0039] (3) Other conditions are the same as in Example 1. As a result, the Fe concentration in the ...
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