Method for recovering lead from waste lead-acid storage batteries
A lead-acid battery and waste technology, applied in the direction of improving process efficiency, can solve the problems of environmental pollution, low recovery rate and high energy consumption, and achieve the effect of solving high energy consumption and improving recovery rate
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Embodiment 1
[0021] A method for recovering lead from waste lead-acid batteries, including the following steps:
[0022] (1) Punch holes at the bottom of the shelled waste lead-acid battery to discharge the waste acid, and then use a wet hammer crusher to crush the lead-acid battery to a particle size of 10mm;
[0023] (2) Sieving the lead-acid battery fragments processed in step (1). The objects on the sieve are waste plastics, grids and connectors, and the objects under the sieve are lead mud. The lead mud is lead, lead oxide and sulfuric acid. Lead mixture
[0024] (3) The lead sludge obtained in step (2) is oxidized and leached with nitric acid, the liquid-to-solid ratio is adjusted to 2, the concentration of nitric acid is 3M, the leaching temperature is 92°C, and the leaching time is 3h to obtain a leachate. Lead in the leachate The content is 180g / L;
[0025] (4) Add sodium sulfate to the leachate, stir and react for 1 hour at room temperature, and then press and filter for solid-liquid se...
Embodiment 2
[0030] A method for recovering lead from waste lead-acid batteries, including the following steps:
[0031] (1) Punch holes at the bottom of the shelled waste lead-acid battery to discharge the waste acid, and then use a wet hammer crusher to crush the lead-acid battery to a particle size of 20mm;
[0032] (2) Sieving the lead-acid battery fragments processed in step (1). The objects on the sieve are waste plastics, grids and connectors, and the objects under the sieve are lead mud. The lead mud is lead, lead oxide and sulfuric acid. Lead mixture
[0033] (3) The lead mud obtained in step (2) is oxidized and leached with nitric acid, the liquid-solid ratio is adjusted to 2-3, the concentration of nitric acid is 3-4M, the leaching temperature is 92-95°C, and the leaching time is 3-3.5h , Obtain a leachate, the content of lead in the leachate is 180-200g / L;
[0034] (4) Add sodium sulfate to the leachate, stir and react for 1h at room temperature, and then press and filter for solid-li...
Embodiment 3
[0039] A method for recovering lead from waste lead-acid batteries, including the following steps:
[0040] (1) Punch holes at the bottom of the shelled waste lead-acid battery to discharge the waste acid, and then use a wet hammer crusher to crush the lead-acid battery to a particle size of 15mm;
[0041] (2) Sieving the lead-acid battery fragments processed in step (1). The objects on the sieve are waste plastics, grids and connectors, and the objects under the sieve are lead mud. The lead mud is lead, lead oxide and sulfuric acid. Lead mixture
[0042] (3) The lead sludge obtained in step (2) is oxidized and leached with nitric acid, the liquid-to-solid ratio is adjusted to 2, the concentration of nitric acid is 4M, the leaching temperature is 93°C, and the leaching time is 3.3h to obtain a leachate. The lead content is 190g / L;
[0043] (4) Add sodium sulfate to the leachate, stir and react for 1h at room temperature, and then press filter for solid-liquid separation to obtain lea...
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