The present disclosure relates to compositions and methods for making lithium-transition metal oxide compounds including nickel, cobalt, manganese, and niobium or nickel, cobalt, aluminum, and niobium suitable for use in lithium-ion cathodes for batteries. Further, the present disclosure relates to lithium-ion battery cathodes and an efficient method of preparing the materials thereof and tuning the electrochemical characteristics thereof.
The electric vehicle (EV) market is rapidly expanding and is regarded as an effective pathway to diminish air pollution from on-street vehicles and to strengthen energy security. However, compared with internal combustion engine (ICE) vehicles, the driving range and high price of EVs problematically limits mass deployment, and puts forward higher requirements for lithium-ion batteries (LIBs), the energy conversion and storage systems for EV propulsion. Since cathode material is a limiting factor of energy density and price in Li-ion batteries, developing alternative cathode materials with a higher lithium utilization/specific energy density at a lower price point are needed.
Layered metal oxides are important cathode materials in LIB's since lithium cobalt oxide (LiCoO2) was initially reported. LiCoO2 still dominates the market of portable communication electronics due to good cycle stability, rate capability, and tap density. However, the inventors have found that LiCoO2 is not suitable for electric vehicles because of the relatively low capacity (135 mAh/g) and high price. Layered ternary cathode materials LiNixCoyMnzO2 (NMC) and LiNixCoyAlzO2 (NCA) have been considered as a promising cathode material to replace LiCoO2. The commercial NMC has developed from NMC111 (discharge capacity: 154 mAh/g at 0.1 C) to NMC442 to NMC622, and now NMC811 (discharge capacity: >185 mAh/g at 0.1 C).
Further, to address practical demands for high energy density EVs, high nickel (greater than or equal to 80%) cathodes have received people's attention. However, the inventors have found high nickel cathodes lack stability and problematically induce, among other things, lithium/nickel cation mixing, inter/intragranular cracks, phase transition, and accumulation of an insulating Ni—O impurity phase with oxygen loss, resulting in structural degradation and deterioration of the cycling and thermal stability. Further, interfacial and structural instability causes capacity and voltage fading, potentially blocking their commercialization. Thus, high nickel cathodes remain deficient for having problematically high surface reactivity and/or structural instability.
Prior art of interest includes U.S. Patent Publication No. 2021/0028448 entitled One-Pot Synthesis forLiNBO3 Coated Spinel and U.S. Pat. No. 10,189,719 entitled Process for the manufacture of lithium metal oxide cathode materials (both of which are herein incorporated entirely by reference). However, the disclosures do not show cathodes formed in accordance with the present disclosure or use of lithium free niobium precursors of the present disclosure.
Nanopowders of layered lithium mixed metal oxides for battery applications are also known, see, e.g., U.S. Pat. No. 10,283,763 herein incorporated entirely by reference.
What are needed are methods of manufacturing lithium-ion cathodes and tuning electrochemical characteristics thereof. For example, there is a need for improved cathodes including high nickel embodiments with a high capacity, low surface reactivity, and structural stability.
It is an object of this disclosure to provide an improved method of preparing a cathode material and/or cathode for lithium-ion batteries.
It is an object of the present disclosure to provide an improved method for forming a niobium containing coating disposed upon a preselected cathode powder suitable for use in a lithium metal oxide cathode.
It is an object of the present disclosure to provide an improved method for forming lithium-ion batteries including a transition metal-based cathode such as NMC and NCA modified to include niobium.
A particular feature of the present disclosure is the ability to manufacture lithium-ion metal oxide cathodes formed of NMC and NCA modified to include niobium.
Another embodiment includes the incorporation of a stabilizing coating on the surface of the cathode material wherein the coating inhibits degradation.
The present disclosure relates to compositions and methods for making lithium-transition metal oxide compounds. In embodiments, the present disclosure relates to a process for making lithium-transition metal oxide compounds, including: forming a slurry by mixing a niobium compound including one or more of niobium ethoxide, niobium pentoxide, niobium dioxide, niobium monoxide, niobium chloride, niobium fluoride, ammonium niobium oxalate hydrate, or niobium oxalate, a lithium nickel manganese cobalt oxide cathode powder or a lithium nickel cobalt aluminum oxide cathode powder, and a solvent; and removing the solvent to form a modified lithium nickel manganese cobalt composition including niobium or a modified lithium nickel cobalt aluminum composition including niobium.
In some embodiments, the present disclosure relates to a method of forming a lithium ion cathode, including forming a slurry by mixing a niobium compound including one or more of niobium ethoxide, niobium pentoxide, niobium dioxide, niobium monoxide, niobium chloride, niobium fluoride, ammonium niobium oxalate hydrate, or niobium oxalate, a lithium nickel manganese cobalt oxide cathode powder or a lithium nickel cobalt aluminum oxide cathode powder, and a solvent; removing the solvent to form a modified lithium nickel manganese cobalt composition including niobium or a modified lithium nickel cobalt aluminum composition including niobium; and forming the modified lithium nickel manganese cobalt composition including niobium or a modified lithium nickel cobalt aluminum composition including niobium into a cathode.
In some embodiments, the present disclosure relates to a cathode, or battery including a cathode, wherein the cathode includes a modified lithium nickel manganese cobalt composition including niobium or a modified lithium nickel cobalt aluminum composition including niobium, wherein niobium is present in a molar ratio of 0.01% to 5.0%.
In embodiments, the present disclosure includes a method of forming a lithium-ion cathode material including: mixing a niobium compound including one or more of niobium ethoxide, niobium pentoxide, niobium dioxide, niobium monoxide, niobium chloride, niobium fluoride, ammonium niobium oxalate hydrate, or niobium oxalate, a lithium nickel manganese cobalt oxide cathode powder or a lithium nickel cobalt aluminum oxide cathode powder, and a solvent; and removing the solvent to form a coated composition including a niobium containing coating disposed upon the lithium nickel manganese cobalt composition or the lithium nickel cobalt aluminum composition. In embodiments, the niobium compound is characterized as substantially lithium free, lithium free, or devoid of lithium. In embodiments, the niobium containing coating is characterized as continuous and/or conformal.
In embodiments, the present disclosure includes a cathode including: a niobium modified lithium nickel manganese cobalt composition, or a niobium modified lithium nickel cobalt aluminum composition, wherein niobium is present in a molar ratio of 0.01% to 5.0%. In embodiments, the cathode is formed of lithium-ion cathode material formed by a process sequence including: mixing a niobium compound including one or more of niobium ethoxide, niobium pentoxide, niobium dioxide, niobium monoxide, niobium chloride, niobium fluoride, ammonium niobium oxalate hydrate, or niobium oxalate, a lithium nickel manganese cobalt oxide cathode powder or a lithium nickel cobalt aluminum oxide cathode powder, and a solvent; and removing the solvent to form a coated composition including a niobium containing coating disposed upon the lithium nickel manganese cobalt composition or the lithium nickel cobalt aluminum composition. In embodiments, the niobium compound is characterized as substantially lithium free or devoid of lithium.
In embodiments, the present disclosure includes an electrochemical cell, including: a cathode of the present disclosure, or a cathode formed of material of the present disclosure, or a cathode formed by a process of the present disclosure.
In embodiments, the present disclosure includes a method of altering a high-Ni NMC material and/or high-Ni NCA material, including: providing a high-Ni NMC substrate or high-Ni NCA substrate, wherein the high-Ni NMC substrate or high-Ni NCA substrate include one or more lithium residuals exposed on a top surface, and coating the top surface with niobium oxide in an amount sufficient to contact the niobium oxide and the one or more lithium residuals. In embodiments, coating further includes: mixing a niobium compound including one or more of niobium ethoxide, niobium pentoxide, niobium dioxide, niobium monoxide, niobium chloride, niobium fluoride, ammonium niobium oxalate hydrate, or niobium oxalate, a lithium nickel manganese cobalt oxide cathode powder or a lithium nickel cobalt aluminum oxide cathode powder, and a solvent; and removing the solvent to form a coated high-Ni NMC substrate or coated high-Ni NCA substrate.
In embodiments, the present disclosure includes a method of coating a parent high-Ni NMC material or parent high-Ni NCA material, including: contacting a parent high-Ni NMC material or parent high-Ni NCA material with niobium compound characterized as substantially free of lithium under conditions suitable for forming a coating atop the parent material. In embodiments, the methods further include sintering a coating atop the parent material to distribute niobium into the parent material to form an altered material, wherein the altered material has different structural/electrochemical properties than the parent material.
In embodiments the present disclosure includes a cathode including a niobium coated and/or substituted lithium nickel manganese cobalt composition or a niobium coated and/or substituted lithium nickel cobalt aluminum composition including niobium wherein niobium is present in a molar ratio of 0.01% to 5.0%.
In embodiments the present disclosure includes a cathode including a niobium coated and/or niobium substituted lithium nickel manganese cobalt composition or a niobium coated and/or niobium substituted lithium nickel cobalt aluminum composition, wherein niobium is present in a molar ratio of 0.01% to 5.0%.
The illustrative aspects of the present disclosure are designed to solve the problems herein described and/or other problems not discussed.
The patent or application file contains at least one drawing executed in color. Copies of this patent or patent application publication with color drawing(s) will be provided by the Office upon request and payment of the necessary fee. These and other features of this disclosure will be more readily understood from the following detailed description of the various aspects of the disclosure taken in conjunction with the accompanying drawings that depict various embodiments of the disclosure, in which:
Li3NbO4.
is LiNbO3, ♥ is Li3NbO4.
for Li3NbO4.
It is noted that the drawings of the disclosure are not necessarily to scale. The drawings are intended to depict only typical aspects of the disclosure, and therefore should not be considered as limiting the scope of the disclosure. In the drawings, like numbering represents like elements between the drawings.
The present disclosure is based, at least in part, on the discovery that a lithium free niobium oxide treatment removes surface impurities forming a LiNbO3/Li3NbO4 surface coating, reducing the 1st capacity loss and improving the rate performance. Surprisingly, the inclusion of a niobium compound substantially free or devoid of lithium, such as one or more of niobium ethoxide, niobium pentoxide, niobium dioxide, niobium monoxide, niobium chloride, niobium fluoride, ammonium niobium oxalate hydrate, or niobium oxalate provides an improved surface coating providing one or more cathodes with significantly reduced first capacity loss and improved rate performance.
In embodiments, the present disclosure provides compositions and methods for making lithium-transition metal oxide compounds. For example, embodiments of the present disclosure generally provide compositions, and methods for making lithium-transition metal oxide compounds including nickel cobalt, manganese, and niobium or nickel, cobalt, aluminum, and niobium suitable for use in lithium-ion cathodes for batteries. Further, the present disclosure relates to lithium-ion battery cathode apparatuses and an efficient method of preparing the materials and tuning electrochemical characteristics thereof.
In embodiments, layered ternary cathode materials LiNixCoyMnzO2 (NMC) and LiNixCoyAlzO2 (NCA), each having a high nickel content, i.e., greater than or equal to 80%, is coated and/or doped with niobium composition to make a modified material suitable for use in forming a stable high nickel cathode. In embodiments, the niobium composition is coated via wet chemistry using a niobium composition substantially free or devoid of lithium. In embodiments, LiNbO3/Li3NbO4 is formed atop the substrate. Subsequent heating may reduce the amount of LiNbO3, and/or drive Nb into the substrate materials depending upon process conditions and temperature. See e.g.,
As used in the present specification, the following words and phrases are generally intended to have the meanings as set forth below, except to the extent that the context in which they are used indicates otherwise.
As used herein, the singular forms “a”, “an”, and “the” include plural references unless the context clearly dictates otherwise. Thus, for example, references to “a compound” include the use of one or more compound(s). “A step” of a method means at least one step, and it could be one, two, three, four, five or even more method steps.
As used herein the terms “about,” “approximately,” and the like, when used in connection with a numerical variable, generally refers to the value of the variable and to all values of the variable that are within the experimental error (e.g., within the 95% confidence interval [CI 95%] for the mean) or within ±10% of the indicated value, whichever is greater.
As used herein, the term “forming a mixture” or “forming a slurry” refers to the process of bringing into contact at least two distinct species such that they mix together and interact. “Forming a reaction mixture” and “contacting” refer to the process of bringing into contact at least two distinct species such that they mix together and can react, either modifying one of the initial reactants or forming a third, distinct, species, a product. It should be appreciated, however, the resulting reaction product can be produced directly from a reaction between the added reagents or from an intermediate from one or more of the added reagents which can be produced in the reaction mixture. “Conversion” and “converting” refer to a process including one or more steps wherein a species is transformed into a distinct product.
The term “substantially free,” as used herein, refers to a component of interest that may be substantially or essentially free of other components which normally accompany or interact with the component of interest. For example, a component of interest may be “substantially free” of lithium when the component of interest contains less than about 10%, less than about 5%, less than about 4%, less than about 3%, less than about 2%, or less than about 1% (by dry weight) of contaminating lithium component(s). Thus, a “substantially free” component of interest may have a purity level of about 90%, about 95%, about 96%, about 97%, about 98%, about 99% or greater.
Before embodiments are further described, it is to be understood that this disclosure is not limited to particular embodiments described, as such may, of course, vary. It is also to be understood that the terminology used herein is for the purpose of describing particular embodiments only, and is not intended to be limiting.
Where a range of values is provided, it is understood that each intervening value, to the tenth of the unit of the lower limit unless the context clearly dictates otherwise, between the upper and lower limit of that range and any other stated or intervening value in that stated range, is encompassed within the invention. The upper and lower limits of these smaller ranges may independently be included in the smaller ranges, and are also encompassed within the invention, subject to any specifically excluded limit in the stated range. Where the stated range includes one or both of the limits, ranges excluding either or both of those included limits are also included in the invention.
Unless defined otherwise, all technical and scientific terms used herein have the same meaning as commonly understood by one of ordinary skill in the art to which this invention belongs. Although any methods and materials similar or equivalent to those described herein can also be used in the practice or testing of the present invention, the preferred methods and materials are now described. All publications mentioned herein are incorporated herein by reference to disclose and describe the methods and/or materials in connection with which the publications are cited.
In embodiments, the methods of the present disclosure include a process for making lithium-transition metal oxide compounds, including: forming a slurry by mixing a niobium compound including one or more of niobium ethoxide, niobium pentoxide, niobium dioxide, niobium monoxide, niobium chloride, niobium fluoride, ammonium niobium oxalate hydrate, or niobium oxalate, a lithium nickel manganese cobalt oxide cathode powder or a lithium nickel cobalt aluminum oxide cathode powder, and a solvent; and removing the solvent to form a modified lithium nickel manganese cobalt composition including niobium or a modified lithium nickel cobalt aluminum composition including niobium. In embodiments, the electrochemical characteristics of the compositions and/or cathodes formed from compositions of the present disclosure can be altered or tuned. For example, depending upon pre-selected conditions, niobium may be deposited as a coating directly atop the materials of the present disclosure, or may penetrate the materials of the present disclosure by thermal processing to alter or tune the electrochemical characteristics thereof. By performing a thermal process after the coating process, the thermal energy provided from the thermal process may efficiently diffuse niobium (such as Nb5+) into the composition and/or crystal structure thereof. In some embodiments, by controlling the thermal process and amount of niobium in the coating and/or diffused into the cathode material, electrochemical characteristics of the cathode material may be altered, tuned, or preselected for use in a cathode. Thus, the compositions and methods of the present disclosure advantageously provide improved lithium-transition metal oxide compounds including: nickel cobalt, manganese, and niobium; or nickel, cobalt, aluminum, and niobium, both of which are suitable for use in lithium-ion cathodes for batteries which may include a surface coating. The surface coating may advantageously inhibit degradation caused by liquid-based electrolytes. In some embodiments, niobium penetration may further promote excellent storage capacity, battery life, recharge time, and storage stability.
In some embodiments, the present disclosure provides for enhanced electrochemical performance of Ni-rich material LiNi0.8Co0.1Mn0.1O2 (NMC811) modified by niobium (Nb). For example, in embodiments, a coating layer of LiNbO3 and/or Li3NbO4 may be disposed atop a cathode composition, such as a cathode powder substrate) with optional Nb penetration of the cathode composition controlled by a thermal process such as sintering. In some embodiments, a coating layer of LiNbO3 and/or Li3NbO4 with Nb penetration is created by annealing in low temperature (400° C., 500° C., or 400° C. to 500° C.). Subsequently, Nb substitution with Li3NbO4 layer may be formed by high temperature heating (600° C., 700° C. and 800° C., or 600° C. to 800° C.). In some embodiments, a first discharge capacity and rate performance may be significantly improved in Nb modified NMC 811 with lower sintering temperature. Nb substituted NMC 811 in high annealing temperature may also have a long cycling stability, providing 178.6 mAh/g (700° C.) vs 174.6 mAh/g (500° C.) and 162.9 mAh/g (Pure NMC 811) with capacity retention 93.2% (700° C.) vs. 88.2% (500° C.) and 83.4% (Pure NMC 811) after 250 cycles.
In embodiments, the process 100 may begin at operation 110 by forming a slurry by mixing a niobium compound including one or more of niobium ethoxide, niobium pentoxide, niobium dioxide, niobium monoxide, niobium chloride, niobium fluoride, ammonium niobium oxalate hydrate, or niobium oxalate, a lithium nickel manganese cobalt oxide cathode powder or a lithium nickel cobalt aluminum oxide cathode powder, and a solvent. In embodiments, the niobium compound is provided in an amount sufficient to form the compositions of the present disclosure such as cathode 200. For example, in embodiments, niobium compound may be provided in an amount to provide compositions of the present disclosure with a molar ratio between 0.001% and 5% niobium. In some embodiments, the niobium compound may be one or more of niobium ethoxide, niobium pentoxide, niobium dioxide, niobium monoxide, niobium chloride, niobium fluoride, ammonium niobium oxalate hydrate, or niobium oxalate. In some embodiments, the niobium compound comprises or consist of niobium ethoxide.
In embodiments, the process 100 may begin at operation 110 by forming a slurry by mixing a niobium compound including one or more of niobium ethoxide, niobium pentoxide, niobium dioxide, niobium monoxide, niobium chloride, niobium fluoride, ammonium niobium oxalate hydrate, or niobium oxalate, a lithium nickel manganese cobalt oxide cathode powder, and a solvent. In embodiments, the niobium compound is selected from a group consisting of niobium ethoxide, niobium pentoxide, niobium dioxide, niobium monoxide, niobium chloride, niobium fluoride, ammonium niobium oxalate hydrate, niobium oxalate, and combinations thereof. In embodiments, the niobium compound is substantially free or devoid of lithium. In embodiments, the niobium compound is niobium ethoxide characterized as substantially free of lithium.
In embodiments, the process 100 may begin at operation 110 by forming a slurry by mixing a niobium compound including one or more of niobium ethoxide, niobium pentoxide, niobium dioxide, niobium monoxide, niobium chloride, niobium fluoride, ammonium niobium oxalate hydrate, or niobium oxalate, a lithium nickel cobalt aluminum oxide cathode powder, and a solvent. In embodiments, the niobium compound is selected from a group consisting of niobium ethoxide, niobium pentoxide, niobium dioxide, niobium monoxide, niobium chloride, niobium fluoride, ammonium niobium oxalate hydrate, niobium oxalate, and combinations thereof. In embodiments, the niobium compound is substantially free or devoid of lithium. In embodiments, the niobium compound is niobium ethoxide characterized as substantially free of lithium.
In embodiments, a substrate 210 is provided in the form of lithium nickel manganese cobalt oxide cathode powder or a lithium nickel cobalt aluminum oxide cathode powder and in an amount sufficient to form compositions of the present disclosure such as cathode 200. In some embodiments, suitable lithium nickel manganese cobalt oxide cathode powder includes lithium nickel manganese cobalt oxide (NMC), a class of electrode material suitable for use in the fabrication of lithium-ion batteries. In some embodiments, suitable lithium nickel manganese cobalt oxide cathode powder includes a preselected amount of lithium nickel manganese and/or cobalt. In some embodiments, nickel is selected in an amount of greater than or equal to 80%, greater than or equal to 85%, greater than or equal to 90% of the total lithium nickel manganese cobalt oxide cathode powder. In embodiments, % refers to the weight percent of the total composition. In some embodiments, the lithium nickel manganese cobalt oxide cathode powder is characterized as LiNixCoyMn1-x-yO2, wherein x is 0.8-1, y is 0-0.2, and 1-x-y is 0-0.2, or in embodiments, LiNixCoyMn1-x-yO2 (x≥0.8). In some embodiments, suitable lithium nickel manganese cobalt oxide cathode powder includes a preselected amount of lithium nickel manganese cobalt. In embodiments, the nickel manganese cobalt oxide cathode powder has an average particle size of less than 0.05 micrometers throughout greater than 98% of the total powder. In some embodiments, the nickel manganese cobalt oxide cathode powder is provided in a form that does not include niobium (Nb), thus e.g., in embodiments, lithium containing niobium compounds are not a suitable starting substrate material for use in accordance with the present disclosure.
In some embodiments, suitable lithium nickel cobalt aluminum oxide cathode powder includes lithium nickel cobalt aluminum oxide (NCA), a class of electrode material suitable for use in the fabrication of lithium-ion batteries. In some embodiments, suitable lithium nickel cobalt aluminum oxide cathode powder includes a preselected amount of lithium, nickel, cobalt, and aluminum. In some embodiments, nickel is selected in an amount of greater than or equal to 80%, greater than or equal to 85%, greater than or equal to 90% of the lithium nickel cobalt aluminum oxide cathode powder. In embodiments, % refers to the weight percent of the total composition. In some embodiments, the lithium nickel cobalt aluminum oxide cathode powder is characterized as LiNi0.8, Co0.15Al0.05O2. In some embodiments, the lithium nickel cobalt aluminum oxide cathode powder is characterized as LiNixCoyAl1-x-yO2, wherein x is 0.8-1, y is 0-0.2, and 1-x-y is 0-0.2. In embodiments, the lithium nickel cobalt aluminum oxide cathode powder has an average particle size of less than 0.05 micrometers throughout greater than 98% of the total powder. In some embodiments, the lithium nickel cobalt aluminum oxide cathode powder is initially provided in a form that does not include niobium (Nb), thus e.g., in embodiments, lithium containing niobium compounds are not a suitable starting substrate material for use in accordance with the present disclosure.
In some embodiments, solvent is provided in an amount sufficient to dissolve, solubilize, or slurry one or more niobium compounds and one or more cathode powders described above to form an admixture. Non-limiting examples of suitable solvents include one or more of methanol, ethanol, ethylene glycol, and/or tetraethylene glycol ethanol. In embodiments, ethanol is a suitable solvent.
Referring to
In some embodiments, and depending upon needs, the solvent is removed under conditions which permit the formation of 1) a modified lithium nickel manganese cobalt composition including niobium; or 2) a modified lithium nickel cobalt aluminum composition including niobium. Non-limiting examples of suitable modified lithium nickel manganese cobalt composition including niobium includes niobium in a molar ratio of 0-5%, 0.01 to 5%, 0.01 to 3%, 0.01 to 2%, or 0.01 to 1%. In some embodiments, a modified lithium nickel manganese cobalt composition includes niobium in a molar ratio of 0.7% to 1.4%, or a molar ratio of 0.7% and 1.4%. In some embodiments, the modified lithium nickel manganese cobalt composition including niobium is characterized by a first formula LiNixCoyMnzNbwO2, wherein (x+y+z+w=1), and wherein x is 0.8-1, y is 0-0.2, z is −0.2, and w is 0-0.2, or a second formula LiwNb1-wNixCoyMn1-x-yO2, wherein x is 0.8-1, y is 0-0.2, w is 0-0.2, and 1-x-y is 0-0.2.
Non-limiting examples of suitable modified lithium nickel cobalt aluminum composition includes niobium in a molar ratio of 0-5%, 0.01 to 5%, 0.01 to 3%, 0.01 to 2%, or 0.01 to 1%. In some embodiments, a modified lithium nickel cobalt aluminum composition includes niobium in a molar ratio of 0.7% to 1.4%, or a molar ratio of 0.7% and 1.4%. In embodiments, a modified composition includes a coated composition in accordance with the present disclosure.
Referring back to
In some embodiments, after coating, or sintering the modified lithium nickel manganese cobalt composition including niobium or modified lithium nickel cobalt aluminum composition including niobium each comprise niobium in a molar ratio of 0.01 to 5%, 0.01 to 3%, 0.01 to 2%, or 0.01 to 1%, 0.7% to 1.4%, 0.7%, or 1.4%. In some embodiments, the sintering is performed under conditions suitable to form a doped and/or a substituted modified lithium nickel manganese cobalt composition including niobium, or a doped and/or a substituted modified lithium nickel cobalt aluminum composition including niobium. In embodiments, a doping process introduces a dopant such as Nb or Nb5+ into the crystal lattice of a NMC or NCA materials of the present disclosure. In embodiments, a thermal process drives the dopant to a controlled depth in the underlying substrate such as NMC or NCA. In embodiments, the NMC and NCA are characterized as high nickel compositions, e.g., greater than or equal to 80% nickel.
As shown in
Referring now to
In some embodiments, the present disclosure relates to one or more lithium-ion batteries including one or more anode(s), one or more cathode(s), and electrolyte with a charge-discharge cycle.
In embodiments, the present disclosure includes a method of forming a lithium-ion cathode material including: mixing a niobium compound including one or more of niobium ethoxide, niobium pentoxide, niobium dioxide, niobium monoxide, niobium chloride, niobium fluoride, ammonium niobium oxalate hydrate, or niobium oxalate, a lithium nickel manganese cobalt oxide cathode powder or a lithium nickel cobalt aluminum oxide cathode powder, and a solvent; and removing the solvent to form a coated composition including a niobium containing coating disposed upon the lithium nickel manganese cobalt composition or the lithium nickel cobalt aluminum composition. In embodiments, the niobium compound is characterized as lithium free. In embodiments, the niobium containing coating is characterized as continuous, thus continuous over and around a substrate upon which it is disposed. In embodiments, the niobium containing coating is characterized as conformal. In embodiments, the niobium containing coating has a thickness between 1 to 100 nanometers. In embodiments, the niobium containing coating comprises or consists of LINBO3, Li3NBO4, or combinations thereof. In embodiments, the lithium nickel manganese cobalt oxide cathode powder is characterized as LiNi0.8Co0.10Mn0.10O2 (Ni:Mn:Co=8:1:1). In embodiments, the lithium nickel cobalt aluminum oxide cathode powder is characterized as LiNixCoyAl1-x-yO2, wherein x is 0.8-1, y is 0-0.2, and 1-x-y is 0-0.2. In embodiments, the lithium nickel manganese cobalt oxide cathode powder is characterized as LiNiXCoyMn1-x-yO2, wherein x is 0.8-1, y is 0-0.2, and 1-x-y is 0-0.2. In embodiments, the coated composition comprises 0.001-5 wt. % niobium. In embodiments, the methods of the present disclosure further include sintering the coated composition under conditions sufficient to drive a niobium disposed with the coating into the lithium nickel manganese cobalt composition or the lithium nickel cobalt aluminum composition to form a modified lithium nickel manganese cobalt composition or a modified lithium nickel cobalt aluminum composition. In embodiments, niobium characterized as Nb5+ is driven into the lithium nickel manganese cobalt composition or the lithium nickel cobalt aluminum composition a distance of 1 to 300 nanometers. In embodiments, the modified lithium nickel manganese cobalt composition or the modified lithium nickel cobalt aluminum composition comprise niobium in a molar ratio of 0.7% to 1.4%. In embodiments, the modified lithium nickel manganese cobalt composition or the modified lithium nickel cobalt aluminum composition comprise 0.001-5.0 wt. % niobium. In embodiments, the modified lithium nickel manganese cobalt composition is characterized by a first formula LiNixCoyMnzNbwO2, wherein (x+y+z+w=1), and wherein x is 0.8-1.0, y is 0-0.2, z is 0-0.2, and w is 0-0.2, or a second formula LiwNb1-wNixCoyMn1-x-yO2, wherein x is 0.8-1, y is 0-0.2, w is 0-0.2, and 1-x-y is 0-0.2.
In embodiments, removing the solvent includes evaporating the solvent at over 65 degrees Celsius for at least 5 hours. In embodiments, the solvent is one or more of methanol, ethanol, ethylene glycol, or tetraethylene glycol ethanol.
In embodiments, the sintering is performed in an atmosphere comprising oxygen at a temperature of at least 400 degrees Celsius, at least 500 degrees Celsius, at least 600 degrees Celsius, at least 700 degrees Celsius, at least 800 degrees Celsius, a temperature between 400 degrees Celsius and 800 degrees Celsius, a temperature between 400 degrees Celsius and 500 degrees Celsius, a temperature between 500 degrees Celsius and 600 degrees Celsius, a temperature between 600 degrees Celsius and 700 degrees Celsius, or a temperature between 700 degrees Celsius and 800 degrees Celsius. In embodiments, the atmosphere including oxygen consists of oxygen. In embodiments, sintering is for a duration between 2-5 hours, 3 hours, or about 3 hours.
In embodiments, the present disclosure includes a cathode including: a niobium modified lithium nickel manganese cobalt composition or a niobium modified lithium nickel cobalt aluminum composition including niobium wherein niobium is present in a molar ratio of 0.01% to 5.0%. In embodiments, the cathode is formed by or formed of the methods and materials of the present disclosure. In embodiments, the cathode is formed of lithium-ion cathode material formed by a process sequence including: mixing a niobium compound comprising one or more of niobium ethoxide, niobium pentoxide, niobium dioxide, niobium monoxide, niobium chloride, niobium fluoride, ammonium niobium oxalate hydrate, or niobium oxalate, a lithium nickel manganese cobalt oxide cathode powder or a lithium nickel cobalt aluminum oxide cathode powder, and a solvent; and removing the solvent to form a coated composition comprising a niobium containing coating disposed upon the lithium nickel manganese cobalt composition or the lithium nickel cobalt aluminum composition. In embodiments, the niobium compound is characterized as substantially lithium free or devoid of lithium.
In embodiments, the present disclosure includes an electrochemical cell, including: a cathode as described herein, or a cathode formed of modified cathode powders having a high nickel content as described herein.
In embodiments, the present disclosure includes a method of altering a high-Ni NMC material and/or high-Ni NCA material, including: providing a high-Ni NMC substrate or high-Ni NCA substrate, wherein the high-Ni NMC substrate or high-Ni NCA substrate comprises one or more lithium residuals exposed on a top surface, and coating the top surface with niobium oxide in an amount sufficient to contact the niobium oxide and the one or more lithium residuals. In embodiments, coating further includes: mixing a niobium compound comprising one or more of niobium ethoxide, niobium pentoxide, niobium dioxide, niobium monoxide, niobium chloride, niobium fluoride, ammonium niobium oxalate hydrate, or niobium oxalate, a lithium nickel manganese cobalt oxide cathode powder or a lithium nickel cobalt aluminum oxide cathode powder, and a solvent; and removing the solvent to form a coated high-Ni NMC substrate or coated high-Ni NCA substrate. In embodiments, the niobium compound is characterized as substantially free of lithium. In embodiments, the high-Ni NMC material and/or high-Ni NCA materials each have nickel in the amount of 80% or more, such as 85%, 90%, 95%, 99%, or between 80% and 85%, between 80% and 90%, between 85% and 90%, or between 80% and 99%.
In embodiments, the methods further include sintering at a low temperature for a duration sufficient to form LixNbOy phases at the top surface. Referring to
In embodiments, the present disclosure includes a method of coating a parent high-Ni NMC material or parent high-Ni NCA material, including: contacting a parent high-Ni NMC material or parent high-Ni NCA material with niobium compound characterized as substantially free of lithium under conditions suitable for forming a coating atop the parent material. In embodiments, the methods further include sintering the coating atop the parent material to distribute niobium into the parent material to form an altered material, wherein herein the altered material has different structural/electrochemical properties than the parent material. In embodiments,
Preparation of Nb coated and doped/substituted NMC 811. LiNi0.8Co0.1Mn0.1O2 materials were obtained from Ecopro Company. Niobium ethoxide (Sigma Aldrich) was used as precursor. Ecopro NMC 811 powders were mixed with niobium ethoxide in a flask and ethanol was added to the mixture. They were stirred overnight, then ethanol was evaporated at 80° C. Pristine NMC 811, 0.7% and 1.4%, 2.1% and 3.5% Nb (molar ratio) modified NMC 811 were sintered in pure oxygen atmosphere for 3 h from 400 to 800° C. and cooled down with a cooling rate of 5.0° C./min. Here, 0.7% Nb modified NMC 811 heated from 400 to 800° C. as NMC811-0.7Nb-400° C., NMC811-0.7Nb-500° C., NMC811-0.7Nb-600° C., NMC811-0.7Nb-700° C. and NMC811-0.7Nb-800° C. However, the high temperature treatment samples are no longer NMC 811 due to Nb modification.
X-ray powder diffraction (XRD) patterns of 0.7% Nb modified NMC 811 samples heated in different temperature was scanned with a BRUKER diffractometer (D8 Advance) equipped with Cu Kα source (λ=1.54178 Å) with spinning. The synchrotron XRD pattern of pristine NMC 811 and 1.4% Nb modified NMC 811 were performed at sector 28-ID-2 of National Synchrotron Light Source II (NSLS-II) at Brookhaven National Laboratory. The wavelength of the X-ray was 0.18266 Å. The neutron diffraction (ND) patterns of the pure NMC 811 and the Nb modified NMC 811 samples were measured at the VULCAN instrument (See e.g., An, K.; Skorpenske, H. D.; Stoica, A. D.; Ma, D.; Wang, X.-L.; Cakmak, E. First in situ Lattice Strains Measurements under Load at VULCAN. Metall. Mater. Trans. 2011, 42, 95-99), at the Spallation Neutron Source, Oak Ridge National Laboratory. The neutron data were processed using VDRIVE software (See e.g., An, K. VDRIVE-Data reduction and Interactive Visualization Software for Event Mode Neutron Diffraction. ORNL Report No. ORNL-TM-2012-621 2012), and Rietveld refinement was carried out using GSAS software and EXPGUI interface (See e.g., Larson, A.; Von Dreele, R. General Structure Analysis System (GSAS) (Report LAUR 86-748). Report LAUR 86-748 2004, and Toby, B. H. EXPGUI, a Graphical User Interface for GSAS. J. Appl. Crystallogr. 2001, 34, 210-213) to calculate the phase fractions, lattice parameters and site occupancy fractions. X-ray Photoemission Spectroscopy (XPS) was performed using a Phi VersaProbe 5000 system with a monochromated Al Kα source and hemispherical analyzer at the Analytical and Diagnostics Laboratory (ADL) at Binghamton University. All samples were mixed with graphite to be used as reference. The core-levels (O 1s, Ni 2p, Nb 3d) were measured with a pass energy of 23.5 eV, corresponding to an instrumental resolution of 0.5 eV from analyzing both the Au 4f7/2 and Fermi edge of the Au foil. A flood gun was used to neutralize any charge build up during measurements. Samples for X-ray absorption near edge structure (XANES) and Extended X-ray absorption fine structure (EXAFS) were prepared by mixing ˜10 mg of materials with graphite and pressed in the form of pellets. Nb K-edge XANES and EXAFS for 0.7% Nb modified NMC 811 samples heated from 400 to 800° C. were tested using a fluorescence detector and calibrated using Nb reference foil in beamline 20 BM in Advanced Photon Source, Argonne National Lab. The samples morphology was determined using a Zeiss SUPRA 55 VP field emission scanning electron microscopy (SEM) at an operating voltage of 5 kV. High-angle annular dark-field (HAADF) scanning transition electron microscopy (STEM), energy-dispersive X-ray spectroscopy (EDS), High resolution transition electron microscopy (HR-TEM) images were collected using a FEI Talos F200X (200 keV) at the Center for Functional Nanomaterials in Brookhaven National Lab. The magnetic properties were tested by a Quantum Design SQUID magnetometer (MPMS XL-5). Field-cooled (FC) and zero-field-cooled (ZFC) magnetizations were measured from 298 to 2 K in magnetic fields of 10 Oe. The thermal stability tests were performed via differential scanning calorimetry (DSC) (Q200, TA) at the scan rate of 2.5° C./min. The test cathodes were charged to 4.4V versus lithium in 2032-type coin cells and disassembled in the glovebox. After washing with Dimethyl carbonate (DMC) to remove the residues, the electrode was cut into a small piece of 5 mg and sealed in a gold-capped stainless-steel crucible with 3 μL electrolyte (1 M LiPF6 in EC/DMC) to do the DSC test.
Nb modified NMC 811, heated from 400 to 800° C. and pristine NMC 811 samples were mixed with acetylene black and polyvinylidene fluoride (PVDF) powders with a weight ratio of 90:5:5 in 1-methyl-2-pyrrolidinone (NMP) solvent to form a slurry. Then the slurry was cast onto an aluminum (Al) foil using doctor blade and dried in vacuum oven at 80° C. for overnight. The average mass loading of the electrode was 13-15 mg/cm2 and was calendared to 3.0 g/cm3. All of this was done in our dry room (Temperature: 20-21° C.; Dew point: <−50). For the coin cells, Li foil was used as a counter/reference electrode, a Celgard 3501 membrane as a separator and 1.0 M LiPF6 dissolved in ethylene carbonate/dimethyl carbonate (EC/DMC, 1:1 in volume) as the electrolyte solution. For the first cycle test of the electrode, a current density of C/10 (1 C=200 mAh/g) was used between 2.8 and 4.6 V. Different rate performance (C/10, C/5, C/2, C, and 2C) was also tested. The cycling was set in the current density of C/3 charge and C/3 discharge. For long cycling, we set 2.8 to 4.4 V for the first two cycles in the current density of C/10, then C/10 charge, hold at 4.4 V for 1 h or the current drop down to C/60 and C/3 discharge for the following cycles. These data were obtained on a multichannel Biologic system.
Valence information for pristine NMC 811 and Nb modified NMC 811 samples was investigated by magnetic susceptibility tests.
At 10.0 K a magnetic transition is observed, below which FC and ZFC curves depart in NMC 811 samples. For Nb modified NMC 811 samples, the transition temperature does not change in samples heated at 400 and 500° C., while in the samples heated at higher temperatures (600° C., 700° C. and 800° C.), the magnetic transition shifts to 11.5 K (See e.g.,
Nickel-rich layered metal oxide LiNi1-y-zCoyMnzO2 (1-y-z≥0.8) materials are the most promising cathodes for next generation lithium-ion batteries in electric vehicles. However, they lose more than 10% of their capacity on the 1st cycle and interfacial/structural instability causes capacity fading. Coating and substitution are direct and effective solutions to solve these challenges. As described herein, Nb coating and Nb substitution on LiNi0.8Co0.1Mn0.1O2 (NMC811) is easily produced through a scalable wet chemistry method followed by sintering from 400 to 800° C. A Li-free Nb oxide treatment is found to remove surface impurities forming a LiNbO3/Li3NbO4 surface coating, reducing the 1st capacity loss and improving the rate performance. Nb substitution stabilizes the structure, providing excellent long cycling stability with a 93.2% capacity retention after 250 cycles.
The layered mixed metal oxides, such as LiNi0.8Mn0.1Co0.1O2, are the dominant cathodes used in Li-ion batteries for electric vehicles and grid storage. However, they lose 10-18% of their capacity on the first charge/discharge cycle, as described in thisjournal. (See e.g., Zhou, H.; Xin, F.; Pei, B.; Whittingham, M. S. What limits the capacity of layered oxide cathodes in lithium batteries? ACS Energy Letters 2019, 4, 1902). If the ultimate capacity of these materials is to be realized, then this capacity must be retained. This lost capacity is at potentials below 4 volts well within the stability limit of the electrolyte unlike that at very low lithium contents attainable only above 4.4 V. In addition, these very high Ni content materials are very sensitive to the environment (See e.g., Faenza, N. V.; Bruce, L.; Lebens-Higgins, Z. W.; Plitz, I.; Pereira, N.; Piper, L. F.; Amatucci, G. G. Growth of Ambient Induced Surface Impurity Species on Layered Positive Electrode Materials and Impact on Electrochemical Performance. J. Electrochem. Soc. 2017, 164 (14), A3727), which is detrimental to their electrochemical behavior (See e.g., Pereira, N.; Matthias, C.; Bell, K.; Badway, F.; Plitz, I.; Al-Sharab, J.; Cosandey, F.; Shah, P.; Isaacs, N.; Amatucci, G. Stoichiometric, Morphological, and Electrochemical Impact of the Phase Stability of LixCoO2. J. Electrochem. Soc. 2004, 152 (1), A114), so they need protection from moisture and CO2 prior to cell fabrication. Raising the temperature to 45° C. essentially eliminated the first cycle loss (See e.g., Zhou, H.; Xin, F.; Pei, B.; Whittingham, M. S. What limits the capacity of layered oxide cathodes in lithium batteries? ACS Energy Letters 2019, 4, 1902), so it should be possible to mimic this small energy kT by modifying the NMC lattice through surface or lattice modification. Here, the use of a lithium-free NbOy treatment that both reduces the 1st cycle loss and stabilizes the surface is reported. Depending on the temperature of treatment, the Nb is retained in the surface region or diffuses into the bulk of the structure. The latter stabilizes the lattice resulting in improved capacity retention on extended cycling.
NMC 811, stirred with a niobium ethoxide solution overnight, was heated from 400 to 800° C. in pure oxygen for 3 hours. The XRD patterns of the 0.7% (Molar ratio) Nb modified NMC 811 are shown in
But the parameters (a, c V) gradually increase for temperature above that, indicating Nb substitution into NMC 811 starting at ˜600° C. and more substitution with increased temperature.
Neutron powder diffraction (See e.g.,
However, the large mismatches of both the valence and the ionic radii of Nb5+ and Li+ reduces the possibility of the Nb at the Li site. If any element is likely to be found on the Li site it is Ni2+, as it is closer in size. (3) Nb occupies the transition metal site. Refinement of the NMC phase agrees that the Nb most possibly substitutes on the TM site in NMC 811 (see e.g.,
The morphology and composition of Nb modified NMC 811 sintered from 400 to 800° C. were characterized by SEM and TEM technique. NMC811-0.7Nb-500° C. and NMC811-0.7Nb-700° C. are the representative samples for the low (400° C., 500° C.) and high (600, 700° C. and 800° C.) temperature.
An XPS study confirmed the Nb5+ oxidation state for the 0.7% Nb modified NMC 811 (See e.g.,
A magnetic susceptibility study (See e.g.,
Table 5. Magnetic parameters of Nb modified NMC 811 and pure NMC 811 in different temperature. At 10.0 K a magnetic transition is observed for the initial and the Nb treated 400 and 500° C. materials, whereas for those materials heated at higher temperatures, the magnetic transition shifts to 11.5 K confirming lattice modification by Nb substitution.
The combination of XRD, ND patterns, refined lattice parameters, SEM, TEM, XPS and magnetic test, confirms that a Nb coating on the surface of NMC 811 is found at the lower temperature (400° C. and 500° C.), whereas Nb substitution at the higher temperatures (600° C., 700° C. and 800° C.). The main coating layer is LiNbO3 and within the lattice Nb occupies the TM sites.
The electrochemical behavior of this Nb modified NMC 811 is shown in
The capacity retention of these materials, at a C/3 rate for mass loading of 13-15 mg/cm2 and calendaring density of 3.0 g/cm3 in the 2.8-4.6 V cycling regime are shown in
Further, a differential capacity (dQ/dV) study was carried out to determine the impact of the Nb treatment on the structural stability of the 811. The results are shown in
In summary, Nb coated and substituted NMC 811 were successfully synthesized and showed that Nb improved the electrochemical behavior of NMC 811. The Nb coating stabilizes the surface and decreases the 1st cycle loss and improves the rate capability, whereas Nb substitution improves capacity retention on extended cycling by stabilizing the lattice. In embodiments, the coating includes or consists of LiNbO3/Li3NbO4 surface species. On substitution, Nb resides on the transition metal sites ejecting some Mn into the niobate surface layer. The improvement of electrochemical performance and structure stability makes Nb modified NMC 811 a potential cathode material for the application in high energy density electric vehicles. Further, combining coating and substitution may be a better way to the whole electrode.
Referring now to
Referring now to
Nb modified NMC 811, heated from 400 to 800° C. and pristine NMC 811 samples were separately mixed with acetylene black and polyvinylidene fluoride (PVDF) powders with a weight ratio of 90:5:5 in 1-methyl-2-pyrrolidinone (NMP) solvent to form a slurry. Then the slurry was cast onto an aluminum (Al) foil using doctor blade and dried in vacuum oven at 80° C. for overnight. The average mass loading of the electrode was 13-15 mg/cm2 and was calendared to 3.0 g/cm3. All of this was done in our dry room (Temperature: 20-21° C.; Dew point: <−50).
More details: The weight ratio of active material for the electrode (Nb modified NMC 811° C. heated at 400° C. or Nb modified NMC 811° C. heated at 500° C. or Nb modified NMC 811° C. heated at 600° C. or Nb modified NMC 811° C. heated at 700° C. or Nb modified NMC 811° C. heated at 800° C.) is between 90% to 96%. The weight ratio of conductive carbon (acetylene black) for the electrode is between 2% to 5%; and binder (polyvinylidene fluoride (PVDF)) in the electrode is between 2% to 5%.
The details for the slurry making process: PVDF (binder) was firstly added to 1-methyl-2-pyrrolidinone (NMP) solvent, and mixed 5 to 10 mins using a mixer machine, then acetylene black (conductive carbon) was added to the mixture and mixed 5 to 10 mins using the mixer machine. Finally active material of the present disclosure (Nb modified NMC 811) and mixed 5 to 10 mins.
Surface coating is commonly employed by industries to improve the cycling and thermal stability of high-nickel (Ni) transition metal (TM) layered cathodes for their practical use in lithium-ion batteries. Niobium (Nb) coating/substitution has been shown above as effective in stabilizing LiNi0.8Mn0.1Co0.1O2 (NMC811) cathodes, further, electrochemical performance of the final products varies depending on the post processing. In this follow-up example, in situ synchrotron X-ray diffraction is used to investigate the kinetic processes and involved structural evolution in Nb-coated NMC811 upon heat treatment. Quantitative structure analysis reveals thermo-driven concurrent changes in the bulk and surface, in particular, the phase evolution of the coating layer and Nb/TM inter-diffusion that facilitates Nb penetration into the bulk and particle growth at the elevated temperatures. Findings from this study highlight the new opportunities for intended control of the structure and surface properties of high-Ni cathodes through surface coating in conjunction with post processing. (See e.g., Xin F, Zhou H, Bai J, Wang F, Whittingham MS. Conditioning the Surface and Bulk of High-Nickel Cathodes with a Nb Coating: An In Situ X-ray Study. J Phys Chem Lett. 2021 Aug. 26; 12(33):7908-7913. doi: 10.1021/acs.jpclett.1c01785. Epub 2021 Aug. 12. PMID: 34383509) (herein incorporated entirely by reference including all supporting information and color figures).
The general process conditions and certain embodiments of the present disclosure are depicted in
The transition metal (TM) layered oxides have been the most used cathode materials in lithium-ion batteries (LIBs) since LiCoO2 was initially reported by Goodenough (See e.g., Mizushima, K.; Jones, P.; Wiseman, P.; Goodenough, J. B. LixCoO2 (0<x<−1): A New Cathode Material for Batteries of High Energy Density. Mater. Res. Bull. 1980, 15, 783-789) and then commercialized in 1991 by Sony Company. (See e.g., Nagaura, T. Lithium Ion Rechargeable Battery. Progress in Batteries & Solar Cells 1990, 9, 209). Even today, LiCoO2 dominates the portable electronics market due to its good cycling stability, rate capability and high tap density. However, it is not suitable for use in electric vehicles (EVs) predominantly because of the high price of Co. So much of the Co has been replaced by other transition metals as in LiNi1-y-zMnyCozO2 (NMC) and LiNi1-y-zCoyAlzO2 (NCA). Amongst these, the high Ni materials, where y+z≤50.2 are attracting the most attention due to their higher energy densities and lower cost. (See e.g., Li, W.; Erickson, E. M.; Manthiram, A. High-nickel Layered Oxide Cathodes for Lithium-based Automotive Batteries. Nat. Energy 2020, 5, 26-34, Choi, J. U.; Voronina, N.; Sun, Y. K.; Myung, S. T. Recent Progress and Perspective of Advanced High-Energy Co-Less Ni-Rich Cathodes for Li-lon Batteries: Yesterday, Today, and Tomorrow. Adv. Energy Mater. 2020, 10, 2002027, Xin, F.; Whittingham, M. S. Challenges and Development of Tin-Based Anode with High Volumetric Capacity for Li-lon Batteries. Electrochem. Energ. Rev. 2020, 3, 643-655, Xu, G. L.; Liu, X.; Daali, A.; Amine, R.; Chen, Z.; Amine, K. Challenges and Strategies to Advance High-Energy Nickel-Rich Layered Lithium Transition Metal Oxide Cathodes for Harsh Operation. Adv. Funct. Mater. 2020, 30, 2004748, Zhou, H.; Xin, F.; Pei, B.; Whittingham, M. S. What Limits the Capacity of Layered Oxide Cathodes in Lithium Batteries? ACS Energy Lett. 2019, 4, 1902-1906).
However, they face multiple challenges, such as Li/Ni cationic mixing, decreased thermal stability, and the formation of surface impurities on air exposure, such as Li2CO3. There have been several approaches to mitigate these issues, in particular coating and doping/substitution or Ni concentration gradient. Surface coating using Al2O3, ZrO2, Li3PO4, Li2ZrO3, Li—Nb—O has been shown effective in suppressing the dissolution of transition metal ions, alleviating the side reactions between the electrolyte and electrode and reducing the first cycle loss. (See e.g., Wise, A. M.; Ban, C.; Weker, J. N.; Misra, S.; Cavanagh, A. S.; Wu, Z.; Li, Z.; Whittingham, M. S.; Xu, K.; George, S. M.; Toney, M. F. Effect of Al2O3Coating on Stabilizing LiNi0.4Mn0.4Co0.2O2 Cathodes. Chem. Mater. 2015, 27, 6146-6154, Ho, V.-C.; Jeong, S.; Yim, T.; Mun, J. Crucial Role of Thioacetamide for ZrO2 Coating on the Fragile Surface of Ni-rich Layered Cathode in Lithium Ion Batteries. J. Power Sources 2020, 450, 227625, Jo, C.-H.; Cho, D.-H.; Noh, H.-J.; Yashiro, H.; Sun, Y.-K.; Myung, S. T. An Effective Method to Reduce Residual Lithium Compounds on Ni-rich Li[Ni0.6Co0.2Mn0.2]O2 Active Material using a Phosphoric Acid Derived Li3PO4 Nanolayer. Nano Res. 2014, 8, 1464-1479, Song, B.; Li, W.; Oh, S. M.; Manthiram, A. Long-Life Nickel-Rich Layered Oxide Cathodes with a Uniform Li2ZrO3 Surface Coating for Lithium-Ion Batteries. ACS Appl. Mat. Interfaces 2017, 9, 9718-9725, and Xin, F.; Zhou, H.; Chen, X.; Zuba, M.; Chernova, N.; Zhou, G.; Whittingham, M. S. Li—Nb—O Coating/Substitution Enhances the Electrochemical Performance of the LiNi0.8Mn0.1Co0.1O2 (NMC 811) Cathode. ACS Appl. Mat. Interfaces 2019, 11, 34889-34894). Cation substitution like Al3+,13 Zr4+,14 Nb5+,15-16 Mg2+,17 W6+,16 is applied to the bulk for improving the conductivity and stability of the lattice, thereby enhancing capacity retention on extended cycling.
Nb oxide coatings can react with surface Li-residuals on high-Ni NMC (LiNi0.8Co0.1Mn0.1O2; 811), with the processes strongly dependent on sintering temperature. At low temperatures, LixNbOy phases, such as LiNbO3/Li3NbO4 were formed at particle surface and are beneficial to performance by reducing the 1st-cycle capacity loss; at further elevated temperatures Nb element was found to penetrate deeply into the bulk, leading to improved cycling performance. (See e.g., Xin, F.; Zhou, H.; Zong, Y.; Zuba, M.; Chen, Y.; Chernova, N. A.; Bai, J.; Pei, B.; Goel, A.; Rana, J. What is the Role of Nb in Nickel-Rich Layered Oxide Cathodes for Lithium-Ion Batteries? ACS Energy Lett. 2021, 6, 1377-1382). It is interesting to understand how the interaction between the Nb coating and the parent NMC811 particles occurs and how the Nb distribution and chemical states are impacted by the sintering conditions (i.e., temperature/duration), giving rise to different structural/electrochemical properties of NMC811.
In situ X-ray diffraction (XRD) has been proven powerful for real-time tracking of the reaction and processes during material synthesis/processing, through probing the structural evolution of the involved intermediates. (See e.g., Bai, J.; Hong, J.; Chen, H.; Graetz, J.; Wang, F. Solvothermal Synthesis of LiMn1-xFexPO4 Cathode Materials: A Study of Reaction Mechanisms by Time-Resolved in Situ Synchrotron X-ray Diffraction. J. Phys. Chem. C 2015, 119, 2266-2276, and Wang, D.; Kou, R.; Ren, Y.; Sun, C. J.; Zhao, H.; Zhang, M. J.; Li, Y.; Huq, A.; Ko, J. P.; Pan, F. Synthetic control of kinetic reaction pathway and cationic ordering in high-Ni layered oxide cathodes. Adv. Mater. 2017, 29, 1606715).
However, when small concentration of the coated materials is present, only 0.7% in Example I, it is technically challenging to identify their re-distribution during the sintering process. Here, high flux and high energy synchrotron X-ray is used for the in situ XRD studies, on a NMC811 system intentionally coated with high concentration of Nb (1.4%) to improve the detectability of Nb distribution. (See e.g., Zhang, M. J.; Hu, X.; Li, M.; Duan, Y.; Yang, L.; Yin, C.; Ge, M.; Xiao, X.; Lee, W. K.; Ko, J. Y. P. Cooling Induced Surface Reconstruction during Synthesis of High-Ni Layered Oxides. Adv. Energy Mater. 2019, 9, 1901915). Through quantitative analysis of the chemical and structural evolution, the concurrent conditioning of the surface and bulk of NMC811 are revealed, arising from the interplay between the thermo-driven transformation of the Nb-containing phases at the particle surface and the Nb/TM inter-diffusion in the bulk.
The reaction in the 1.4% Nb coated NMC 811 was tracked in real time by time and temperature-resolved in situ synchrotron XRD, with 50-min hold at each of the destination temperatures during the heating process. XRD patterns were recorded during heating from room temperature to 475° C., 520° C., 560° C., 600° C., 645° C., 690° C., 730° C., 770° C., 815° C. and final cooling down, as presented in
Further quantitative analysis is performed on the evolution of Nb-containing phases, with the main results presented in
In contrast to significant change of the surface coating layer induced by heating, the change in the bulk is hardly observable from the XRD patterns (as given in
Nb substitution into the TM sites consequently caused cationic disordering, evidenced by the reduced peak intensity ratio, I(003)/I(104) in
More specifically,
Rietveld refinements were made to the XRD patterns taken during holding at each of the destination temperatures (475, 520, 560, 600, 645, 690, 730, 770, 815° C.), to obtain the changes in the lattice, cationic ordering and particle size, with the main results provided in
Interplay between the Processes at Particle Surface and in the Bulk
For better understanding the kinetics of the structural change and the associated Nb substitution, non-linear fitting, using y=Ax2+Bx+C, was made to the lattice changes during holding at each of the destination temperatures, as exampled in
Besides the Nb substitution, the structural change in NMC811 may also be induced by heat treatment itself. Our previous studies showed that the lattice parameters a, c and V were almost constant with increasing temperature, combined with overall constant Ni occupancy in NMC811 (See e.g.
In summary, the thermo-driven reactions and processes occurred in Nb-coated NMC811 were investigated to elucidate the role of Nb coating in conditioning the surface and bulk of the parent NMC811 particles. Through in situ synchrotron XRD measurements coupled with quantitative structure analysis, the kinetic processes during the heat treatment was revealed, involving initial formation of LiNbO3/Li3NbO4 phase and their dynamic evolution with temperature, accompanied by structural change in the bulk. As high temperature (above 690° C.), the fast decomposition of LiNbO3 and thermo-driven Nb/TM inter-diffusion accelerated Nb penetration into the bulk and, consequently, the rapid lattice expansion, cationic disordering (i.e., Li+/Ni2+ mixing), along with fast particle growth. Those observations, only becoming accessible by in situ observation, provide important insights into the kinetic processes governing structural/chemical changes, occurred concomitantly in the bulk and surface of the NMC811 particles. The findings facilitate optimization of the coating and heating processes in tuning the structural and electrochemical properties of high-Ni cathode materials.
Sample Preparation. NMC811 materials and niobium ethoxide were purchased from the Ecopro Company and Sigma Aldrich, separately. For the preparation process, NMC 811 was mixed with niobium ethoxide solution in a flask and stirred overnight. Typically, 2 g NMC 811 was added into 4 mL niobium ethoxide solution (0.096 g niobium ethoxide was dissolved in 4 mL ethanol). After stirring overnight, the ethanol was evaporated at 80° C. to get Nb-coated NMC811.
In situ Synchrotron Characterization. The in situ synchrotron XRD experiments were performed at sector 28-ID-1 of the National Synchrotron Light Source II (NSLS-II) at Brookhaven National Laboratory. The wavelength of the X-ray was 0.16625 Å. The produced ultrahigh flux allows us to track the fast reaction kinetics and detection of the minor phases, besides the main crystalline phases. For in situ experiments, the material was pressed into a pellet (1 mm thick and 7 mm in diameter), then loaded into in a furnace (Linkam TS 1500) vertically, with a window perpendicular to the X-ray beam. A 2D X-ray detector was applied to collect the XRD patterns from the pellet during heating in the air. At each of the destination temperatures, the sample was held at constant temperature for about 60 minutes. Here we need to mention that the use of air is likely to increase Ni/Li disordering but does not influence the kinetics process. Quantitative structural analysis was made by Rietveld refinement of individual ex situ and in situ synchrotron XRD patterns, using the same structure models from neutron diffraction analysis. (See e.g., Xin, F.; Zhou, H.; Zong, Y.; Zuba, M.; Chen, Y.; Chernova, N. A.; Bai, J.; Pei, B.; Goel, A.; Rana, J. What is the Role of Nb in Nickel-Rich Layered Oxide Cathodes for Lithium-Ion Batteries? ACS Energy Lett. 2021, 6, 1377-1382) (This reference is entirely incorporated by reference herein, including Supporting information, and all color Figures).
The entire disclosure of all applications, patents, and publications cited herein are herein incorporated by reference in their entirety. While the foregoing is directed to embodiments of the present disclosure, other and further embodiments of the disclosure may be devised without departing from the basic scope thereof.
The present disclosure claims priority or the benefit under 35 U.S.C. § 119 of U.S. provisional application No. 63/092,755 filed 16 Oct. 2020, herein entirely incorporated by reference.
This invention was made with government support under grant no. DE-EE0007765 awarded by The U.S. Department of Energy. The government has certain rights in the invention.
Filing Document | Filing Date | Country | Kind |
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PCT/US2021/055328 | 10/16/2021 | WO |
Number | Date | Country | |
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63092755 | Oct 2020 | US |