Leaching method of metals in lead-zinc sulfide mineral tailings and application of leaching method
A sulfide ore and leaching technology, applied in the direction of improving process efficiency, etc., can solve the problems of inability to realize full recovery of metals, low lead leaching rate, waste of resources, etc., to achieve waste of resources, less loss of valuable metals, and full recovery Effect
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Embodiment 1
[0025] This embodiment is a specific embodiment of recovering lead and zinc in the tailings according to a method for leaching metals in the tailings of lead-zinc sulfide mines provided by the present invention. After testing, in this embodiment, the lead content in the lead-zinc sulfide tailings used is 4381 mg / kg, and the zinc content in the lead-zinc sulfide tailings used is 5467 mg / kg.
[0026] At room temperature, soak 0.005kg of lead-zinc sulfide ore tailings in 0.1L of bioleaching solution 1, and stir at 100rpm for 50 days. In this example, the pH of the bioleaching solution 1 used was adjusted to 1.5 with a sulfuric acid solution, and the active ingredient of the bioleaching solution 1 was Thiobacillus ferrooxidans. After soaking, the solid-liquid separation is carried out by suction filtration, and the filter residue is collected. The filter residue is pickled with dilute sulfuric acid with a pH of 2, and then dried to obtain the first product 1. The filtrate obtaine...
Embodiment 2
[0030] This embodiment is a specific embodiment of recovering lead and zinc in the tailings according to a method for leaching metals in the tailings of lead-zinc sulfide mines provided by the present invention. After testing, in this embodiment, the lead content in the lead-zinc sulfide tailings used is 4381 mg / kg, and the zinc content in the lead-zinc sulfide tailings used is 5467 mg / kg.
[0031] At room temperature, soak 0.10 kg of lead-zinc sulfide ore tailings in 1 L of bioleaching solution 2, and stir at a speed of 160 rpm for 20 days. In this embodiment, the pH of the bioleach solution 2 used is adjusted to 2 with a sulfuric acid solution, and the active ingredient of the bioleach solution 2 is Thiobacillus ferrooxidans. After soaking, natural sedimentation was used for solid-liquid separation, and after sedimentation for 30 minutes, the filter residue was collected, and the filter residue was acid-washed with dilute sulfuric acid with a pH of 2, and then dried to obtai...
Embodiment 3
[0035] This embodiment is a specific embodiment of recovering lead and zinc in the tailings according to a method for leaching metals in the tailings of lead-zinc sulfide mines provided by the present invention. After testing, in this embodiment, the lead content in the lead-zinc sulfide tailings used is 4381 mg / kg, and the zinc content in the lead-zinc sulfide tailings used is 5467 mg / kg.
[0036] At room temperature, soak 0.4kg of lead-zinc sulfide ore tailings in 2L of bioleaching solution 3, and stir at 200rpm for 40 days. In this embodiment, the pH of the bioleach solution 3 used is adjusted to 3 with a sulfuric acid solution, and the active ingredient of the bioleach solution 3 is Thiobacillus ferrooxidans. After soaking, natural sedimentation was used for solid-liquid separation, and after sedimentation for 120 minutes, the filter residue was collected, and the filter residue was acid-washed with dilute sulfuric acid with a pH of 2, and then dried to obtain the first pr...
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