Waste lithium battery pyrolyzation, defluorination and dechlorination method
A technology for used lithium batteries and lithium batteries, which is applied in battery recycling, chemical instruments and methods, and solid waste removal to achieve high resource utilization and high efficiency.
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Embodiment 1
[0033] Manually disassemble the power battery pack into modules. The additive is added to crush the battery once, and the crushed product is subjected to steam drying treatment, and after drying, it is sorted once to select large pieces of metal, diaphragm, and plastic. Secondary crushing is carried out, and the crushed products are subjected to secondary sorting to sort out plastics and metals. A certain amount of absorbent is added, and pyrolysis is carried out in a three-layer rotary kiln, and the pyrolysis product is broken up and screened to obtain black powder. The specific operation of the pyrolysis process is as follows.
[0034] After checking the performance of the airtight structure of the rotary kiln to meet the standard, the rotary kiln is deoxygenated, and the nitrogen replacement gas in the kiln is combined with vacuuming to remove the oxygen in the kiln, and the rotary kiln is preheated to reach a high temperature zone of 500-550°C. Put battery waste and abso...
Embodiment 2
[0038] Vacuum pyrolysis + alkali leaching defluorination process
[0039] After 2 crushing and sorting of recovered waste lithium batteries, the particle size is <2cm, take 40g and put it into the middle kiln of the closed three-layer rotary kiln, carry out a vacuum treatment until the vacuum pressure is <100Pa, heat to 400°C, and roast for 0.75 h, 37.96g of roasted material was obtained. After roasting, it was dispersed through a 100-mesh sieve to obtain 30.11g of black powder. After testing and analysis, the tailings contained Ni 11.96%, Co12.04, Mn11.60%, Li 4.88%, and Cu0.5%. , Al 0.32%, F 2.04%, Cl<0.016%. After the traditional wet alkali elution fluorine treatment, the black powder F<0.1%.
Embodiment 3
[0041] Nitrogen protected pyrolysis + absorbent defluorination
[0042] Recycling waste lithium batteries after 2 times of crushing and sorting, particle size <1cm, take 200g and put it into the middle kiln of the closed three-layer rotary kiln, add 100g of absorbing material to the inner kiln, carry out pyrolysis under nitrogen protection, heat to 450°C, and roast After 1.20 hours, the roasted material rate was 95.2%. After roasting, it was dispersed through a 100-mesh sieve to obtain 75.38% black powder. The black powder contained Ni 12.56%, Co 12.38, Mn11.96%, Li 5.08%, Cu0.52 %, Al 0.43%, F 1.04%, Cl<0.001%, compared with the F content (F 2.04%) after defluorination pyrolysis in Example 2, the defluorination rate is increased by about 50%.
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