Method for recovering valuable material from used lithium-ion battery
US-2019386354-A1 · Dec 19, 2019 · US
US2021269894A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2021269894-A1 |
| Application number | US-201816306326-A |
| Country | US |
| Kind code | A1 |
| Filing date | Nov 20, 2018 |
| Priority date | Nov 13, 2018 |
| Publication date | Sep 2, 2021 |
| Grant date | — |
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The present disclosure provides a method for recovering nickel and cobalt, the method comprising: a first step of heat-treating lithium nickel cobalt aluminum oxide to produce a mixture; a second step of water-washing the mixture produced in the first step to obtain a residue; and a third step of heat-treating the residue obtained in the second step.
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What is claimed is: 1 . A method for recovering nickel and cobalt, the method comprising: a first step of heat-treating lithium nickel cobalt aluminum oxide to produce a mixture; a second step of water-washing the mixture produced in the first step to obtain a residue; and a third step of heat-treating the residue obtained in the second step. 2 . The method of claim 1 , wherein the lithium nickel cobalt aluminum oxide is obtained from a waste lithium nickel cobalt aluminum oxide battery. 3 . The method of claim 2 , wherein the first step is performed in a reducing atmosphere. 4 . The method of claim 3 , wherein the reducing atmosphere in the first step is composed of carbon dioxide, carbon monoxide and a mixture thereof. 5 . The method of claim 4 , wherein the heat treatment in the first step is performed in a range of about 600 degrees Celsius to 1000 degrees Celsius. 6 . The method of claim 5 , wherein the heat-treatment in the first step is performed for about 1 to 3 hours. 7 . The method of claim 6 , wherein the mixture produced in the first step contains lithium carbonate (Li 2 CO 3 ), nickel oxide (NiO), cobalt oxide (CoO) and nickel cobalt oxide (NiCoO). 8 . The method of claim 2 , wherein the method further comprises, after the washing in the second step, a step of separating the residue. 9 . The method of claim 8 , wherein the residue contains nickel oxide, cobalt oxide and nickel cobalt oxide. 10 . The method of claim 1 , wherein the heat-treatment in the third step includes primary and secondary heat-treatments performed respectively in first and second reactors connected to each other via a guide line, wherein a gaseous product produced from the primary heat treatment in the first reactor is transferred to the second reactor via the guide line and, then, in the secondary reactor, the secondary heat treatment is performed. 11 . The method of claim 10 , wherein in the primary heat-treatment, the residue is heat-treated in the first reactor. 12 . The method of claim 11 , wherein the primary heat treatment is performed in a reducing atmosphere. 13 . The method of claim 12 , wherein the reducing atmosphere in the primary heat treatment is composed of carbon dioxide, carbon monoxide and a mixture thereof. 14 . The method of claim 13 , wherein the primary heat treatment is performed in a temperature range of 50 degrees Celsius to 200 degrees Celsius. 15 . The method of claim 13 , wherein the primary heat treatment is performed at a temperature at which Ni(CO) 4 is produced. 16 . The method of claim 14 , wherein in the primary heat treatment, a cobalt metal powder, and nickel-containing gas are produced. 17 . The method of claim 16 , wherein the nickel-containing gas contains Ni(CO) 4 . 18 . The method of claim 17 , wherein the guide line is maintained at a temperature range of about 60 degrees Celsius to 100 degrees Celsius. 19 . The method of claim 10 , wherein the secondary heat treatment is performed in an atmosphere composed of Ni(CO) 4 . 20 . The method of claim 19 , wherein the secondary heat treatment is performed at a temperature range of about 150 degrees Celsius to 350 degrees Celsius. 21 . The method of claim 20 , wherein in the secondary heat treatment, a nickel metal powder is produced. 22 . A method for recovering nickel and cobalt, the method comprising: (a) heat-treating a lithium nickel cobalt aluminum oxide in a range of about 600 degrees Celsius to 800 degrees Celsius and for 1 hour to 3 hours in a reducing atmosphere containing carbon dioxide, carbon monoxide and mixtures thereof, to produce a mixture containing lithium carbonate (Li 2 CO 3 ), nickel oxide (NiO), cobalt oxide (CoO) and nickel cobalt oxide (NiCoO); (b) water-washing the mixture to obtain a residue; and (c) heat-treating the residue, wherein the heat-treatment of the residue includes primary and secondary heat-treatments performed respectively in first and second reactors connected to each other via a guide line, wherein the primary heat treatment includes heat-treating the residue at about 50 degrees Celsius to 200 degrees Celsius in the first reactor having a reducing atmosphere containing carbon dioxide, carbon monoxide and a mixture thereof, to produce a cobalt metal powder and a nickel-containing gas from the residue, wherein the nickel-containing gas produced in the primary heat treatment is transferred from the first reactor to the second reactor via the guide line maintained at a temperature of about 70 degrees Celsius to 90 degrees Celsius, wherein in the secondary heat treatment, a heat treatment is performed in the second reactor having an atmosphere of the nickel-containing gas transferred from the first reactor at about 150 degrees Celsius to 350 degrees Celsius, to produce nickel.
Obtaining lithium · CPC title
by gases · CPC title
separation of nickel from cobalt · CPC title
Energy storage using batteries · CPC title
Li-accumulators · CPC title
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