Method for treating lithium ion battery waste

US2020277704A1 · US · A1

Patent metadata
FieldValue
Publication numberUS-2020277704-A1
Application numberUS-201816765225-A
CountryUS
Kind codeA1
Filing dateOct 22, 2018
Priority dateNov 24, 2017
Publication dateSep 3, 2020
Grant date

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  4. Key dates

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  5. First independent claim

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Abstract

Official abstract text for this publication.

Provided is a treatment method whereby it becomes possible to recovery copper, nickel and cobalt, which are valuable metals, contained in a lithium ion battery waste and to separate copper, nickel and cobalt from one another effectively. A method for treating a lithium ion battery waste according to the present invention includes: an alloy production step S1 of introducing the lithium ion battery waste into a furnace and then melting the lithium ion battery waste by heating, thereby producing an alloy containing copper, nickel and cobalt; and an electrolytic purification step S2 of subjecting the alloy to such an electrolytic treatment that the alloy is charged as an anode into a sulfuric acid solution and then electricity is conducted between the anode and a cathode to electrodeposit copper contained in the alloy onto the cathode, thereby separating nickel and cobalt from each other.

First claim

Opening claim text (preview).

1 . A method for treating a lithium ion battery waste, the method comprising: an alloy production step of introducing the lithium ion battery waste into a furnace and then melting the lithium ion battery waste by heating, thereby producing an alloy containing copper, nickel and cobalt; and an electrolytic purification step of subjecting the alloy to such an electrolytic treatment that the alloy is charged as an anode into a sulfuric acid solution and then electricity is conducted between the anode and a cathode to electrodeposit copper contained in the alloy onto the cathode, thereby separating copper from nickel and cobalt. 2 . The method for treating a lithium ion battery waste according to claim 1 , wherein in the electrolytic purification step, a current density of the anode is set in a range of 3 A/m 2 or more and 3000 A/m 2 or less. 3 . The method for treating a lithium ion battery waste according to claim 1 , wherein in the electrolytic purification step, the electrolytic treatment is performed while a copper concentration in the sulfuric acid solution that is an electrolyte solution is maintained in a range of 5 g/L or more and 50 g/L or less. 4 . The method for treating a lithium ion battery waste according to claim 1 , wherein the alloy contains phosphorus in a range of 0.5 wt % or more and 2.0 wt % or less, and the alloy is used as an anode in the electrolytic purification. 5 . The method for treating a lithium ion battery waste according to claim 1 , further comprising an electrowinning step of supplying an electrolyte solution obtained after the electrolytic treatment in the electrolytic purification step to an electrolysis tank and electrodepositing copper remaining the electrolyte solution by using an insoluble anode. 6 . The method for treating a lithium ion battery waste according to claim 5 , wherein the electrolyte solution obtained through the electrowinning step and discharged from the electrolysis tank is repeatedly supplied as the electrolyte solution to be used in the electrolytic purification step. 7 . The method for treating a lithium ion battery waste according to claim 1 , further comprising an impurity removing step of removing an impurity component by recovering at least a part of an electrolyte solution obtained after the electrolytic treatment in the electrolytic purification step and adding an oxidizing agent and a neutralizing agent to the electrolyte solution to adjust an oxidation-reduction potential (reference electrode: silver/silver chloride electrode) to 570 mV or more and to adjust a pH in a range of 3 or more and 5 or less, wherein after the impurity removing step, sulfuric acid is added to a filtrate obtained by solid-liquid separation to adjust the pH to 1.5 or less, and the pH-adjusted filtrate is repeatedly supplied as the electrolyte solution to be used in the electrolytic purification step. 8 . The method for treating a lithium ion battery waste according to claim 1 , further comprising an impurity removing step of removing an impurity component by recovering at least a part of an electrolyte solution obtained after the electrolytic treatment in the electrolytic purification step, adding an oxidizing agent to the electrolyte solution at a stage in which a pH of the electrolyte solution is 1.5 or less to adjust an oxidation-reduction potential (reference electrode: silver/silver chloride electrode) to 570 mV or more, and then further adding an oxidizing agent and a neutralizing agent to increase the pH to 3 and to adjust the oxidation-reduction potential to 300 mV or more, wherein after the impurity removing step, sulfuric acid is added to a filtrate obtained by solid-liquid separation to adjust the pH to 1.5 or less, and the pH-adjusted filtrate is repeatedly supplied as the electrolyte solution to be used in the electrolytic purification step. 9 . The method for treating a lithium ion battery waste according to claim 2 , wherein in the electrolytic purification step, the electrolytic treatment is performed while a copper concentration in the sulfuric acid solution that is an electrolyte solution is maintained in a range of 5 g/L or more and 50 g/L or less. 10 . The method for treating a lithium ion battery waste according to claim 2 , wherein the alloy contains phosphorus in a range of 0.5 wt % or more and 2.0 wt % or less, and the alloy is used as an anode in the electrolytic purification. 11 . The method for treating a lithium ion battery waste according to claim 3 , wherein the alloy contains phosphorus in a range of 0.5 wt % or more and 2.0 wt % or less, and the alloy is used as an anode in the electrolytic purification. 12 . The method for treating a lithium ion battery waste according to claim 9 , wherein the alloy contains phosphorus in a range of 0.5 wt % or more and 2.0 wt % or less, and the alloy is used as an anode in the electrolytic purification. 13 . The method for treating a lithium ion battery waste according to claim 2 , further comprising an electrowinning step of supplying an electrolyte solution obtained after the electrolytic treatment in the electrolytic purification step to an electrolysis tank and electrodepositing copper remaining the electrolyte solution by using an insoluble anode. 14 . The method for treating a lithium ion battery waste according to claim 3 , further comprising an electrowinning step of supplying an electrolyte solution obtained after the electrolytic treatment in the electrolytic purification step to an electrolysis tank and electrodepositing copper remaining the electrolyte solution by using an insoluble anode. 15 . The method for treating a lithium ion battery waste according to claim 4 , further comprising an electrowinning step of supplying an electrolyte solution obtained after the electrolytic treatment in the electrolytic purification step to an electrolysis tank and electrodepositing copper remaining the electrolyte solution by using an insoluble anode. 16 . The method for treating a lithium ion battery waste according to claim 9 , further comprising an electrowinning step of supplying an electrolyte solution obtained after the electrolytic treatment in the electrolytic purification step to an electrolysis tank and electrodepositing copper remaining the electrolyte solution by using an insoluble anode. 17 . The method for treating a lithium ion battery waste according to claim 10 , further comprising an electrowinning step of supplying an electrolyte solution obtained after the electrolytic treatment in the electrolytic purification step to an electrolysis tank and electrodepositing copper remaining the electrolyte solution by using an insoluble anode. 18 . The method for treating a lithium ion battery waste according to claim 13 , wherein the electrolyte solution obtained through the electrowinning step and discharged from the electrolysis tank is repeatedly supplied as the electrolyte solution to be used in the electrolytic purification step. 19 . The method for treating a lithium ion battery waste according to claim 14 , wherein the electrolyte solution obtained through the electrowinning step and discharged from the electrolysis tank is repeatedly supplied as the electrolyte solution to be used in the electrolytic purification step. 20 . The method for treating a lithium ion battery waste according to claim 15 , wherein the electrolyte solution obtained through the electrowinning step and discharged from the electrolysis tank is repeatedly supplied as the electrolyte solution to be used in

Assignees

Inventors

Classifications

  • involving thermal treatment, e.g. evaporation (processes using mineral binders involving a melting or softening step B09B3/29; involving radiation B09B3/50) · CPC title

  • Recycling of batteries or fuel cells · CPC title

  • Recycling · CPC title

  • Energy storage using batteries · CPC title

  • H01M10/54Primary

    Reclaiming serviceable parts of waste accumulators · CPC title

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What does patent US2020277704A1 cover?
Provided is a treatment method whereby it becomes possible to recovery copper, nickel and cobalt, which are valuable metals, contained in a lithium ion battery waste and to separate copper, nickel and cobalt from one another effectively. A method for treating a lithium ion battery waste according to the present invention includes: an alloy production step S1 of introducing the lithium ion batte…
Who is the assignee on this patent?
Sumitomo Metal Mining Co
What technology area does this patent fall under?
Primary CPC classification H01M10/54. Mapped technology areas include Electricity.
When was this patent published?
Publication date Thu Sep 03 2020 00:00:00 GMT+0000 (Coordinated Universal Time) (A1). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 8 related publications on this page (citations in our corpus or others sharing the same primary CPC).