Recycling method for valuable element in waste lithium ion battery electrode material
A lithium-ion battery and electrode material technology, which is applied in the field of recycling waste lithium battery electrode materials, can solve the problems of large reducing agent consumption, high equipment requirements, and high cost, so as to reduce costs and material losses, reduce recycling costs, and improve The effect of recovery
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Embodiment 1
[0012] After crushing and sorting waste lithium-ion batteries containing nickel-cobalt-manganese positive electrode materials, a mixture of positive electrode materials, negative electrode graphite powder and part of the electrolyte is obtained, containing 15%wt of nickel, 8%wt of cobalt, 10%wt of manganese, and 5% of lithium. %wt, carbon 35%wt, fluorine 1.2%wt, calcination under the air, the calcination temperature is 700 ℃, and keep warm for 30 minutes. The roasted slag in [H + ] The sulfuric acid solution with a concentration of 0.5mol / L is mixed according to the mass ratio of 1:10, and leached at a leaching temperature of 90°C and a leaching time of 1h. After the leaching is completed, filter and separate to obtain the leaching solution and leaching residue; the leaching solution is used for further recovery of nickel and cobalt , manganese and lithium, the leaching residue is used to recover carbon materials. The analysis results show that the leaching rates in terms of ...
Embodiment 2
[0014] After crushing and sorting waste lithium-ion batteries containing nickel-cobalt-aluminum cathode materials, a mixture of cathode materials, negative electrode graphite powder, and part of the electrolyte is obtained, containing 30%wt of nickel, 6%wt of cobalt, 5%wt of aluminum, and 4% of lithium. %wt, carbon 20%wt, fluorine 0.5%wt, calcination under the air, the calcination temperature is 600 ℃, and keep warm for 60 minutes. The roasted slag in [H + ] The hydrochloric acid solution with a concentration of 1mol / L is mixed according to the mass ratio of 1:8, and leached at a leaching temperature of 70°C and a leaching time of 3h. Manganese and Lithium, leach residues are used to recover carbon materials. The analysis results show that the leaching rates in terms of slag are 91.87% for lithium, 91.92% for nickel, 91.96% for cobalt, and 91.82% for aluminum.
Embodiment 3
[0016] After crushing and sorting waste lithium-ion batteries containing different proportions of nickel-cobalt-manganese cathode materials, a mixture of cathode materials, negative electrode graphite powder, and part of the electrolyte is obtained, which contains 22%wt of nickel, 12%wt of cobalt, and 6% of manganese wt, aluminum 0.01%wt, lithium 2%wt, carbon 30%wt, fluorine 1.0%wt, were calcined in air at 400°C and kept for 120 minutes. The roasted slag in [H + ] Sulfuric acid solution and hydrochloric acid solution with a concentration of 2mol / L are mixed at a mass ratio of 1:6, and leached at a leaching temperature of 50°C and a leaching time of 5h. After the leaching is completed, filter and separate to obtain the leaching solution and leaching residue; the leaching solution is used to further recover nickel , cobalt, manganese and lithium, the leaching residue is used to recover carbon materials. The analysis results show that the leaching rates in terms of slag are 88.1...
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