Doped cathode material precursors from recycled lithium-ion batteries

Abstract

To provide a doped cathode material precursor from a recycled lithium-ion battery.SOLUTION: A battery recycling process aggregates a recycling stream including charge material metals from exhausted Li-ion batteries and generates recycled battery charge material having comparable or improved cycle life as well as a recycled charge material precursor having fewer cracking defects using doping substances in a coprecipitation phase in a recycling sequence. In a coprecipitation process, a solution of co-mingled charge material metals is produced, the ratio of the charge material metals is adjusted based on recycled battery specifications, and a relatively small quantity of a doping salt is added.SELECTED DRAWING: Figure 1

Description

[Background technology]

[0001] background Lithium-ion (Li-ion) batteries are the preferred chemistry for secondary (rechargeable) batteries in high-discharge applications such as electric vehicles (EVs) and power tools where electric motors are needed for rapid acceleration. Li-ion batteries contain charge materials applied or deposited on a current collector (typically a planar sheet of copper or aluminum), conductive powders, and binders. The charge materials include an anode charge material, typically graphite or carbon, and a cathode charge material, which contains metals such as lithium, nickel, manganese, cobalt, aluminum, iron, and phosphorus in predetermined ratios, defining the so-called "battery chemistry" of the Li-ion cell. The preferred battery chemistry varies by vendor and application, and Li-ion battery recycling efforts typically follow a predetermined molar ratio of battery chemistry in the recycled charge material product. The purity of the constituent products has a significant bearing on the quality and performance of the recycled cells, and often depends on so-called "battery grade" materials, meaning 99.5% purity. Summary of the Invention [Means for solving the problem]

[0002] overview In the battery recycling process, a recycle stream containing charge material metals from exhausted Li-ion batteries is collected and a doping material is used in the co-precipitation step of the recycling sequence to produce a recycled battery charge material precursor with fewer crack defects and a recycled battery charge material with comparable or improved cycle life. In the co-precipitation process, a solution of mixed charge material metals is adjusted to have a ratio of charge material metals based on the specifications of the recycled battery and to contain a relatively small amount of dopant salt. The doped charge material precursor results from pH adjustment, co-precipitation of charge material metals and dopant salts, which are then sintered with lithium to form a doped cathode active charge material for the recycled battery with a predetermined chemical composition (ratio). Additional doping salts can also be added before sintering to improve performance characteristics.

[0003] The configurations described herein are based in part on the observation that recycling Li-ion batteries for EVs and other industries produces large amounts of charge material metals in the form of spent cathode charge materials (cathode materials). Unfortunately, conventional approaches to recycling batteries suffer from the disadvantage that the history and quality of these recycled cathode materials are unknown, which can lead to variability in the performance of the resulting cathode material precursors and cathode materials prepared therefrom. For example, the surface properties of the cathode material precursors, such as cracks, and the cycle life of the cathode materials can vary depending on the source and properties of the recycled materials used to produce them.

[0004] Thus, the configurations herein substantially overcome performance problems including cycle life and surface cracking by adding a doping material, particularly a dopant salt, to the recycled battery charge material to co-precipitate and sinter the charge material with the doping material. The doping material is typically another metal salt added in small amounts to the leachate prior to co-precipitation and contains a metal different from that of the battery charge material being recycled. Typical dopant salts include magnesium or aluminum, which have been surprisingly found to improve the surface morphology of the cathode material precursor and also improve the cycle life of the cathode material, i.e., the number of times the battery can be recharged.

[0005] More specifically, the present invention produces a doped cathode material precursor prepared from recycled lithium-ion battery streams based on a co-precipitation mixture of at least one dopant salt and a selected or predetermined ratio of metal elements obtained by leaching black mass from the recycled lithium-ion battery streams. The co-precipitation reaction produces a particulate form of charge material (typically in hydroxide form) containing the dopant, which can be used as a precursor (pCAM, precursor cathode active material) for the formation of a cathode active material (CAM) that can be used in the manufacture of new / recycled batteries. Before the co-precipitation, additional metal salts are provided to adjust the ratio of the metal elements to a selected ratio, and one or more dopant salts are added separately (before or after) or during the adjustment of the ratio to obtain the desired performance improvement. Additional dopant salts can be added to the precipitated mixture. From the precursor, a sintering process incorporating the lithium salt can be used to produce the corresponding CAM. In this manner, doped cathode active material precursors and doped cathode active materials are prepared from recycled lithium ion battery streams and comprise sintered combinations of ratio-controlled metal salts, one or more dopant salts, and lithium salts.

[0006] BRIEF DESCRIPTION OF THE DRAWINGS The foregoing and other features will become apparent from the following description of specific embodiments disclosed herein, as illustrated in the accompanying drawings, in which like reference characters refer to the same parts throughout the different views, and in which the drawings are not necessarily to scale, emphasis instead being placed upon illustrating the principles of the invention. [Brief description of the drawings]

[0007] [Figure 1] FIG. 1 is a context diagram of a recycling environment suitable for use in the configurations herein. [Diagram 2] 2 is a flow chart for introducing dopants to improve the performance of the charge material in the recycling process of FIG. 1. [Diagram 3] 3 is a scanning electron micrograph (SEM) showing the surface morphology of charge material precursor particles resulting from the process of FIG. 2. [Figure 4] 3 is a scanning electron micrograph (SEM) showing the surface morphology of charge material precursor particles resulting from the process of FIG. 2. [Diagram 5] 3 is a graph of the charge cycle improvement obtained as a result of doping according to the flow chart of FIG. 2. DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS

[0008] Detailed Description Below are examples of methods and approaches for recycling batteries such as NMC batteries. Li-ion batteries employ a so-called battery chemistry that specifies the type and ratio of metal ions used to form the cathode material. The anode material is most often a carbon or graphite-based formulation. The configurations herein employ the NMC battery chemistry as an example. However, the disclosed approach can be implemented with any suitable battery chemistry. The specific ratios are set by the manufacturer or recipient of the recycled charge material, and the charge material and charge material precursors can be produced to meet the manufacturer's given specifications.

[0009] FIG. 1 is a contextual diagram of a recycling environment suitable for use in the context of the present disclosure. With reference to FIG. 1, a recycling scenario 100 typically begins with the placement of Li-ion batteries 102 from an EV. Li-ion batteries 102 have a finite number of charge cycles before the charge material's ability to accept a sufficient charge is significantly reduced. To this are added batteries that have terminated prematurely due to vehicle failure, collision damage, etc. This collective end-of-life recycling stream contributes to an abundant supply of depleted batteries, including used cells and charge material. The batteries are discharged and agitated by physically crushing, shredding, and pulverizing into a granular black mass 104, which includes the charge material and any associated casings and copper and aluminum current collectors. The black mass, which includes both the cathode material of the cathode material metal salts and the anode material of carbon and graphite, is used to form a leachate 106 of dissolved charge material metals.

[0010] The leachate includes salts of Ni, Mn and Co, such as sulfates from a sulfuric acid leach, although other charge material metals and / or leach acids may be employed. The leachate 106 has a molar ratio of Ni, Mn and Co based on the constituent composition of the incoming recycle stream. The molar ratio is adjusted with additional Ni, Mn and Co salts, such as sulfates (typically in virgin or control form from fresh material), to obtain a solution 108 adjusted to the target ratio.

[0011] The co-precipitation reaction in one or more tanks 110 begins with adjusting the pH of the leachate to precipitate the charge material metals (charge materials) in the desired resulting ratio. Sodium hydroxide or other strong base precipitates the NMC from the solution, typically as the hydroxide, in a granular form that can be separated by filtration. This granular form precipitated by adjusting the pH of the leachate defines the pCAM (cathode active material precursor) with the desired molar ratio for the target battery chemistry of the new recycled battery. Sintering with lithium carbonate or other lithium salt in a furnace 112 forms the cathode active material 114 (CAM) for the recycled Li-ion battery. In the example configuration, the cathode active material LiNix Mn y Co z O2 is Ni x Mn y Co z They are synthesized by sintering (OH)2 and Li2CO3, where x, y, and z represent the respective molar ratios of Ni, Mn, and Co. Common chemical compositions include NMC111, NMC811, NMC622, and NMC532, which represent equimolar components of Ni, Mn, and Co, although any suitable molar ratio can be achieved by ratioing and sintering the leachates 106-108. The recycled cathode material can then be combined back into the recycle stream as cathode material.

[0012] Figure 2 is a flow chart 200 for introducing a dopant to obtain an improved performance charge material in the recycling process of Figure 1. The dopant comprises a relatively small amount of salt that is added to the leachate for co-precipitation 110. Optionally, an additional dopant can be introduced into the lithium mixture for sintering 112.

[0013] 1 and 2, a method for producing doped cathode material from a recycled lithium-ion battery stream includes, in step 202, leaching black mass from the recycled lithium-ion battery stream to obtain a leachate containing a ratio of metal elements. After removing impurities, such as by filtration, the leachate is a substantially pure composition of metal elements including nickel, manganese and cobalt, as shown in step 204. Depending on the source of the recycled battery stream, other cathode material metals may also be dissolved. The anode material generally does not dissolve after leaching in 202, which can be removed when the substantially pure leachate is withdrawn. Separate recycling of the residual anode material may also be performed. As shown in step 206, the ratio of metal elements is adjusted to a selected ratio with additional metal salts corresponding to the selected cathode material ratio, which often corresponds to the targeted recycled battery chemical composition.

[0014] One or more doping agents are also added to the leachate. With reference to step 208, doping can be accomplished with a number of materials, typically water-soluble salts, in various concentrations, that are added to the leachate prior to co-precipitation to achieve improved performance.

[0015] As a result, following the addition of the dopant salt, the metal elements are co-precipitated from the leachate to form a doped cathode material precursor having a selected ratio of the metal elements, as disclosed in step 214. The co-precipitation involves adjusting (raising) the pH to pull the mixed charge material out of solution in a controlled ratio that includes the doping salt.

[0016] In an exemplary configuration, the dopant salt is a salt containing a dopant metal selected from the group consisting of Mg, Ca, Al, Fe, Nb, Cu, Cr, Zn, and Zr, as shown in step 210. This results in a doped cathode material precursor containing 0.5-5000 ppm of the dopant metal, as shown in step 212. As mentioned above, additional dopant salts can optionally be added to the co-precipitation mixture prior to sintering with the lithium salt (typically lithium carbonate).

[0017] Specific examples of dopant concentrations (ppm) for specific doping salts are given in Table I below.

[0018] [Table 1]

[0019] Surprisingly, it has been found that the incorporation of low levels of various dopant salts prior to co-precipitation results in the formation of doped cathode material precursors with significantly improved properties. In particular, it is believed that the doping of the leachate relieves internal particle stresses present during the formation of the cathode material precursor, resulting in precursor particles with significantly improved physical and surface properties. Advantages of the particle morphology include fewer cracks than comparable cathode material precursors prepared without the addition of dopant salts to the leachate prior to co-precipitation.

[0020] The amount of cracking can be evaluated using any method known in the art. For example, it has been found that the doped cathode material precursor has a lower BET value than the BET surface area value of a comparative cathode material precursor prepared without adding dopant salt to the leachate prior to coprecipitation. The BET value of the doped cathode material precursor can be 2-3 times lower than the BET value of the comparative cathode material precursor.

[0021] Surface morphology can also be evaluated by microscopy. Specific evaluation results are shown in Figures 3 and 4. These are SEM (scanning electron micrograph) images showing the surface morphology of charge material precursor particles obtained from the dopant method described in Figure 2. Figure 3 shows a control group of undoped charge material particles at various times during the co-precipitation process. In comparison, Figure 4 shows the formation of doped charge material precursor particles of the present disclosure with dopant salt added before co-precipitation. In this specific example, the process includes adding aluminum nitrate salt to the nickel manganese cobalt sulfate solution before co-precipitation.

[0022] As shown, surface cracks are greatly reduced. This is believed to be a result of the internal stress relief provided by the dopant salt during particle growth, which prevents particle cracking. In FIG. 4, a clear continuous particle surface with a single crystal morphology can be seen, which is a significant improvement over the visible cracks seen in FIG. 3. As a result, the doped cathode material precursor particles were found to have fewer visible cracks within a single precursor particle. In addition, it was found that most of the formed precursor particles had no visible cracks. Preferably, less than 10%, more preferably less than 5%, and most preferably less than 1% of the resulting doped cathode material precursor particles have cracks.

[0023] In certain configurations, high nickel cathode materials have been found to be particularly beneficial from the doping process, so the doped cathode material precursor contains greater than 60% nickel. These include NMC622 and NMC811. Other configurations with less nickel may also benefit, such as where the doped cathode material is 60% nickel or less, such as 10% to 50% nickel, such as NMC532.

[0024] It has also been found that the doped pCAM improves the lattice structure resulting in a sintered CAM, thereby improving charge cycle performance. For example, as shown in step 216, a doped cathode material precursor and a lithium salt can be combined to form a mixture, and then the mixture is sintered, as shown in step 218, whereby a doped cathode active material is formed. After sintering, the doped cathode active material is received for harvesting and / or evaluation, as shown in step 220.

[0025] FIG. 5 is a graph 500 of the charge cycle improvement resulting from doping according to the flow chart of FIG. 2. In FIG. 5, the capacity retention refers to the percentage of full charge remaining after a number of charge / discharge cycles, as indicated by the charge index. Surprisingly, it has been found that the inclusion of a dopant salt prior to the co-precipitation reaction to form the doped charge material precursor also significantly improves the cycle life of the doped charge material prepared therefrom. For example, doping with a relatively small amount of Mg, on the order of 200 ppm, improved the cycle performance, maintaining more than 90% of the full charge capacity after about 1240 cycles and 80% of the full charge capacity after about 5000 cycles. Other doping salts can be employed to obtain similar or improved performance.

[0026] In certain configurations, the dopant salt is a Mg salt or an Al salt. For example, certain configurations are doped cathode material precursors having 1-100 ppm Al dopant salt. In yet other configurations, the dopant salt is a Li salt and the doped cathode material precursor has less than 0.01 ppm Li. Note that the Li dopant is added in the leaching step prior to co-precipitation and should not be confused with the lithium carbonate added for sintering of the precipitated material.

[0027] Although the systems and methods defined herein have been shown and described with particular reference to embodiments thereof, it will be understood by those skilled in the art that various changes in form and details may be made therein without departing from the scope of the invention as encompassed by the appended claims. [Explanation of symbols]

[0028] 100 Recycling Scenarios 102 Li-ion battery 104 Black Mass 106 Exudate 107 Exudate 108 Exudate 110 tanks 112 Furnace 114 Cathode active material 200 Flowchart

Claims

1. 1. A method for producing a doped cathode material precursor from a recycled lithium ion battery stream, comprising: leaching black mass from said recycled lithium ion battery stream to obtain a leachate containing the elemental metals nickel, manganese and cobalt in proportions; adjusting the ratio of the metal elements to a selected ratio with an additional metal salt selected from the group consisting of nickel salts, manganese salts and cobalt salts; adding one or more dopant salts to the leach solution, the salts comprising dopant metals selected from the group consisting of Ca, Fe, Nb, Cu, Cr, Zn and Zr; co-precipitating the metal elements and dopant salts from the leachate to form the doped cathode material precursor having the selected ratio of metal elements; The method includes:

2. The method of claim 1 , wherein the doped cathode material precursor comprises 0.5 to 5000 ppm of the dopant metal.

3. The method of claim 1 , wherein the dopant salt is a Mg salt or an Al salt.

4. The method of claim 1 , wherein the dopant salt is aluminum nitrate.

5. The method of claim 4, wherein the doped cathode material precursor comprises 1 to 100 ppm Al.

6. 10. The method of claim 1 , wherein the doped cathode material precursor comprises greater than 60% nickel.

7. The method of claim 6 , wherein the doped cathode material precursor comprises less than 60% nickel.

8. The method of claim 7, wherein the doped cathode material precursor comprises between 10% nickel and 50% nickel.

9. 10. The method of claim 1, wherein the doped cathode material precursor has fewer cracks than a comparative cathode material precursor prepared without adding the dopant salt to the leach solution prior to co-precipitation.

10. 10. The method of claim 9, wherein less than 10% of the doped cathode material precursor has cracks.

11. 10. The method of claim 9, wherein less than 5% of the doped cathode material precursor has cracks.

12. 10. The method of claim 9, wherein less than 1% of the doped cathode material precursor has cracks.

13. the doped cathode material precursor has a BET value that is lower than a BET value of a comparative cathode material precursor prepared without adding the dopant salt to the leach solution prior to co-precipitation; The method of claim 1.

14. The method of claim 13, wherein the BET value of the doped cathode material precursor is 2 to 3 times lower than the BET value of the comparative cathode material precursor.

15. 1. A doped cathode material precursor prepared from recycled lithium ion battery streams, comprising: the metallic elements nickel, manganese and cobalt in certain proportions obtained by leaching black mass from said recycled lithium ion battery stream; an additional metal salt selected from the group consisting of nickel salts, manganese salts and cobalt salts, which is provided to adjust the ratio of the metal elements to a selected ratio; one or more dopant salts provided prior to coprecipitation, the salts comprising dopant metals selected from the group consisting of Ca, Fe, Nb, Cu, Cr, Zn and Zr; 1. A doped cathode material precursor comprising a co-precipitated mixture of:

16. 16. The doped cathode material precursor of claim 15 comprising 0.5 to 5000 ppm of said dopant metal.

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