Cation-substituted spinel oxide and oxyfluoride cathodes for lithium ion batteries

Abstract

The present invention includes compositions and methods of making cation-substituted and fluorine-substituted spinel cathode compositions by firing a LiMn2−y−zLiyMzO4 oxide with NH4HF2 at low temperatures of between about 300 and 700° C. for 2 to 8 hours and a η of more than 0 and less than about 0.50, mixed two-phase compositions consisting of a spinel cathode and a layered oxide cathode, and coupling them with unmodified or surface modified graphite anodes in lithium ion cells.

Description

TECHNICAL FIELD OF THE INVENTION

The present invention relates in general to the field of lithium-ion cathode materials, more particularly to cation-substituted spinel oxide cathodes having substitutions of fluoride ion for oxide ion.

BACKGROUND OF THE INVENTION

Without limiting the scope of the invention, its background is described in connection with lithium ion batteries.

Generally, lithium ion batteries transport lithium ions between the anode and cathode with the simultaneous oxidation or reduction of the host electrodes, respectively. Cathode materials common in the art include transition metal oxides containing lithium, e.g., layered lithium cobalt oxide (LiCoO₂), spinel lithium manganese oxide (LiMn₂O₄), and olivine lithium iron phosphate (LiFePO₄). For example, lithium ion batteries use layered lithium cobalt oxide cathodes; however, these materials are expensive and environmentally unfriendly due to their cobalt content. As a result, alternative materials are being developed as electrodes that have the desired discharge capacity, which is related to the amount of lithium that can be reversibly extracted, and discharge voltage, which depends on the transition metal ion and crystal structure.

For example, common electrode materials include spinel LiMn₂O₄ and olivine LiFePO₄ that include Mn and Fe respectively, and hence are inexpensive and environmentally benign. However, the spinel LiMn₂O₄ cathode has been plagued by severe capacity fade at elevated temperatures.^1-7 The spinel electrodes are unstable in the cell environment, and particularly unstable when operated at temperatures above room temperature.

The capacity fade is generally thought to be due to the dissolution of manganese from the lattice into the electrolyte and then into the carbon anode. Alternative spinel compositions achieved through cationic substitutions have been pursued, but they could not completely overcome the capacity fade problem.

In addition, the process of synthesizing the spinel structure and chemical substitutions could result in local defects and microstructural differences that could influence the electrochemical performance factors including capacity retention, rate (power) capability, and storage characteristics.

For example, U.S. Pat. No. 5,674,645 (the '645 Patent) entitled “Lithium Manganese Oxy-Fluorides for Li-Ion Rechargeable Battery Electrodes” issued to Amatucci, et al. on Oct. 7, 1997. The '645 Patent discloses that the cycling stability and capacity of Li-ion rechargeable batteries are improved by the use of lithium manganese oxy-fluoride electrode component intercalation materials having the general formula, Li_1+xM_y Mn_2−x−y O_4−z, where M is a transition metal, e.g., Co, Cr, or Fe.

Similarly, U.S. Pat. No. 6,087,042, entitled, “Positive Electrode Material for Secondary Lithium Battery” issued to Sugiyama, et al. discloses a positive electrode material for a secondary lithium battery excellent in high temperature cycle characteristics which is a lithium manganese oxyfluoride having a spinel structure, wherein the oxyfluoride has a composition represented by the composition formula Li_1+xMn_2−xO_4−yF_z: wherein x represents a number from 0.0133 to 0.3333; y represents a number from 0 to 0.2 (exclusive of 0); and z represents a number of from 0.01 to 0.2 (exclusive of 0.01), with the proviso that (y-z) is more than 0 but not more than 0.07. The positive electrode material for a secondary lithium battery of is said to exhibit not only a high cycle durability of charge/discharge but also a minimum drop of a charge/discharge initial capacity to provide a high energy density.

SUMMARY OF THE INVENTION

The present inventors recognized that the current method of making a fluorine-substituted oxyfluorides composition were inadequate in that they did not teach the compositions of the present invention and could not be used to incorporate the desired fluorine content to make the compositions of the present invention.

The present inventors recognized that the cyclability at elevated temperatures, rate capability, and storage characteristics could be improved significantly by reducing the lattice parameter difference Δa between the two cubic phases formed during cycling by appropriate cationic substitutions.^8-11 However, cationic substitutions generally leads to a decrease in the reversible capacity values, which may make the cation-substituted spinel compositions unattractive for practical applications.

The present inventors recognized that the substitution of fluoride ion for oxide ion in cation-substituted spinel oxide cathodes increased the reversible capacity due to a decrease in the oxidation state of Mn. In addition, the present inventors recognized that the cyclability at elevated temperatures, the rate capability, and the storage characteristics could be improved significantly by reducing the lattice parameter difference Δa between the two cubic phases formed during cycling by appropriate cationic substitutions.

The present inventors recognized a need to increase the reversible capacity, while preserving the other electrochemical performance features. The present inventors used the partial substitution of fluoride ions for oxide ions in the cation-substituted spinel oxides to obtain the corresponding spinel oxyfluoride cathodes. In order to maximize the fluorine content in the spinel lattice, the present inventors developed a low temperature procedure involving the firing of the already synthesized cation-substituted spinel oxides LiMn_2−y−zLi_yM_zO₄ with ammonium hydrogen fluoride (NH₄HF₂) at a low temperature of 450° C. for a short period.

The present invention provides a method of making fluorine-substituted oxyfluoride compositions by firing a LiMn_2−y−zLi_yM_zO₄ oxide with NH₄HF₂ at a temperature within the range of about 200 to about 700° C. for 2 to 8 hours to form a cation-substituted, fluorine-substituted LiMn_2−y−zLi_yM_zO_4−ηF_η spinel oxide structure. Generally, M may be Mg, Al, Ti, V, Cr, Fe, Co, Ni, Cu, Zn, Zr, Nb, Mo, Ga, Sn, or combinations thereof The fluorine incorporated into the spinel lattice in the cation-substituted, fluorine-substituted LiMn_2−y−zLi_yM_zO_4−ηF_η spinel structure is between about η=0 and η=0.30. Some specific, non-limiting examples of compositions having the cation-substituted, fluorine-substituted LiMn_2−y−zLi_yM_zO_4−ηF_η spinel structure include LiMn_1.8Li_0.2O_3.88F_0.12, LiMn_1.8Li_0.2O_3.79F_0.21, LiMn_1.8Li_0.1Ti_0.1O_3.9F_0.1, LiMn_1.8Li_0.1Cu_0.1O_3.9F_0.1, LiMn_1.8Li_0.1Ni_0.1O_3.9F_0.1, or LiMn_1.8Li_0.1Ni_0.1O_3.8F_0.2.

The present invention also provides a lithium cathode composition having a cation-substituted, fluorine-substituted LiMn_2−y−zLi_yM_zO_4−ηF_η composition with a spinel crystal structure. M may be Mg, Al, Ti, V, Cr, Fe, Co, Ni, Cu, Zn, Zr, Nb, Mo, Ga, Sn, or combinations thereof

Furthermore, the present invention provides a method of making a spinel cathode by mixing a LiMn_2−y−zLi_yM_zO_4−ηF_η composition with a conductive diluent and a binder to form a cation-substituted fluorine-substituted LiMn_2−y−zLi_yM_zO_4−ηF_η composition. The cation-substituted fluorine-substituted LiMn_2−y−zLi_yM_zO_4−ηF_η composition can then be formed into a cathode shape, e.g., generally cylindrical or generally disk shaped.

One example of the spinel cathode includes a binder of powdered polytetrafluoroethylene at about 1 to about 10 weight percent of the cathode mixture, a conductive diluent of acetylene black at about 5 to about 25 weight percent of the cathode mixture and the LiMn_2−y−zLi_yM_zO_4−ηF_η powder composition of about 70 to about 95 weight percent of the cathode mixture.

The present invention also provides a mixed cathode consisting of a spinel and layered oxide. The cathode includes a mixture of a cation-substituted spinel oxide material and a layered oxide material. In some instances, the cation-substituted spinel oxide material is also fluorine-substituted, e.g., LiMn_2−y−zLi_yM_zO_4−ηF_η where y is within the range of about 0 to about 0.3, z is within the range of about 0 to about 1.0, and η is within the range of about 0 to about 0.5. The mixture may contain between about 20 weight percent and about 95 weight percent of the cation-substituted spinel oxide or oxyfluoride and between about 80 weight percent and about 5 weight percent for the layered oxide material (e.g., between about 70 weight percent and about 80 weight percent LiMn_1.85Li_0.075Ni_0.04Al_0.035O₄ and between about 20 weight percent and about 30 weight percent LiCoO₂, or between about 70 weight percent and about 80 weight percent LiMn_1.8Li_0.1Ni_0.1O_3.8F_0.2 and between about 20 weight percent and about 30 weight percent LiCoO₂.

The present invention also provides a carbon anode surface modification having a spinel Li₄Ti₅O₁₂ or TiO₂ coating in contact with the carbon anode surface. Both Li₄Ti₅O₁₂ and TiO₂ offer the advantage of contributing capacities to the anode. The skilled artisan will recognize that other oxides or conductive polymers that may or may not contribute capacity may also be used, e.g., oxides of Mg, Al, Si, V, Cr, Fe, Co, Ni, Cu, Zn, Ga, Ge, Y, Zr, Nb, Mo, Cd, In, Sn, Sb, La, Ce, Hf, Ta, W, Bi and combinations thereof and polyaniline, polypyrrole, polythiophene, polyphenol, polyacetylene, polyphenylene and combinations thereof.

A method of making a spinel and layered oxide cathode is also provided. The cathode is formed from a mixture of a cation-substituted spinel oxide material and a layered oxide material. In some instances, the cation-substituted spinel oxide material is also fluorine-substituted, and has the composition LiMn_2−y−zLi_yM_zO_4−ηF_η where y is within the range of about 0 to about 0.3, z is within the range of about 0 to about 1.0, and η is within the range of about 0 to about 0.5. The mixture may contain between about 60 weight percent and about 90 weight percent of the cation-substituted spinel oxide and between about 40 weight percent and about 10 weight percent of the layered oxide material (e.g., between about 70 weight percent and about 80 weight percent LiMn_1.85Li_0.075Ni_0.04Al_0.035O₄ and between about 20 weight percent and about 30 weight percent LiCoO₂, or between about 70 weight percent and about 80 weight percent LiMn_1.8Li_0.1Ni_0.1O_3.8F_0.2 and between about 20 weight percent and about 30 weight percent LiCoO₂).

BRIEF DESCRIPTION OF THE DRAWINGS

For a more complete understanding of the features and advantages of the present invention, reference is now made to the detailed description of the invention along with the accompanying figures and in which:

FIG. 1 is the X-ray diffraction patterns of selected parent LiMn_2−y−zLi_yM_zO_4−ηF_η and chemically delithiated Li_1−xLiMn_2−y−zLi_yM_zO_4−ηF_η spinel cathodes;

FIG. 2 (top graph) and (bottom graph) are graphs comparing the electrochemical cycling performances at different temperatures;

FIG. 3 is a graph comparing the discharge profiles at various C rates;

FIG. 4 (top graph) and (bottom graph) are graphs that illustrate the correlation of the capacity fade to 4A the degree of manganese dissolution and 4B the lattice parameter difference Δa between the two cubic phases formed during the charge-discharge process;

FIG. 5 is a graph that compares the percent capacity retention after storing at various depths of discharge for LiMn₂O₄, LiMn_1.8Li_0.2O₄, LiMn_1.8Li_0.2O_3.79F_0.21, and LiMn_1.8Li_0.1Ni_0.1O_3.8F_0.2;

FIG. 6 is a graph that compares the cycling performance of lithium ion cells having various ratios of spinel and layered oxide mixture cathodes and commercial carbon anode; and

FIG. 7 is a graph of the cycling performance of lithium ion cells having various ratios of spinel and layered oxide mixture cathodes and commercial carbon anode.

DETAILED DESCRIPTION OF THE INVENTION

While the making and using of various embodiments of the present invention are discussed in detail below, it should be appreciated that the present invention provides many applicable inventive concepts that can be embodied in a wide variety of specific contexts. The specific embodiments discussed herein are merely illustrative of specific ways to make and use the invention and do not delimit the scope of the invention.

The present inventors recognized a need for Li_1+x M_y Mn_2−x−y O_4−z F_z (and specifically, LiMn_1.8Li_0.1Ni_0.1O_4−ηF_η compositions, methods of using the composition (cells, batteries, etc.) and methods of making the compositions. Existing references fail to teach Li_1+x M_y Mn_2−x−y O_4−z F_z (and specifically, LiMn_1.8Li_0.1Ni_0.1O_4−ηF_η) compositions, method of making or using. Although the '645 Patent states that compositions of Li_1+x M_y Mn_2−x−y O_4−z F_z, where M is a transition metal can be made the present inventors also recognized that, the '645 Patent does not teach or enable the making of the compositions of the present invention.

For example, the present inventors recognized that the '645 Patent claims a lithium manganese oxy-fluoride compound having the general formula, Li_1+x M_y Mn_2−x−y O_4−z F_z, where x≦0.4, y≦0.3, and 0.05≦z≦1.0. The '645 Patent claims M is a transition metal and further defines the transition metal as Co, Cr, or Fe. However, the present inventors recognized that the methods of the '645 Patent do not teach the compositions of the present invention and the '645 Patent cannot be used to make the present invention.

The present inventors have tried to synthesize LiMn_1.8Li_0.1Ni_0.1O_4−ηF_η by the procedure described in U.S. Pat. No. 5,674,645 (the '645 Patent). The synthesis was carried out by heating required amounts of Li₂CO₃, LiF, MnO₂, and NiO at 800° C. in air for various nominal fluorine contents as described by the '645 Patent. The samples were then characterized by X-ray diffraction, lithium content analysis by atomic absorption spectroscopy, and oxidation state analysis by a redox titration. The fluorine contents in the synthesized samples were calculated based on the experimental values of lithium content and oxidation state of manganese/nickel, employing charge neutrality principle and assuming the total anion (O+F) content to be 4.0. TABLE 1 compares the experimental compositions obtained based on these chemical analysis data with the nominal compositions. As seen, it is difficult to incorporate any fluorine into LiMn_1.8Li_0.1Ni_0.1O_4−ηF_η by the synthesis method described by the '645 Patent. This is because LiF is volatile at the higher synthesis temperature of 800° C. used by the '645 Patent. To overcome this problem and to maximize the fluorine content, the present inventors adopted a low temperature procedure in which the LiMn_1.8Li_0.1Ni_0.1O₄ oxide is synthesized first by firing at 800° C. and the oxide is then heat treated with NH₄HF₂ at a moderate temperature of 450° C. The low temperature process employed by the present inventors helps to increase the fluorine content in LiMn_1.8Li_0.1Ni_0.1O_4−ηF_η.

			Lattice
Sample	Nominal	Experimental	parameter
#	composition	composition	(Å)
1	Li1.1Mn1.8Ni0.1O4	Li1.10Mn1.80Ni0.1O4	8.2046
1	Li1.1Mn1.8Ni0.1O3.8F0.2	Li1.06Mn1.84Ni0.1O4	8.2062
2	Li1.1Mn1.8Ni0.1O3.7F0.3	Li1.04Mn1.86Ni0.1O4	8.2086
3	Li1.1Mn1.8Ni0.1O3.6F0.4	Li1.03Mn1.87Ni0.1O4	8.2181
4	Li1.1Mn1.8Ni0.1O3.5F0.5	Li1.01Mn1.89Ni0.1O4	8.2208

TABLE 1 also gives the experimentally determined lattice parameters for various nominal fluorine contents in LiMn_1.8Li_0.1Ni_0.1O_4−ηF_η. The lattice parameter increases with increasing nominal fluorine content, which is in general similar to that reported by the '645 Patent. Although one may think that the observed increase in lattice parameter with increasing nominal fluorine content could be due to a substitution of monovalent F⁻ for divalent O²⁻ and a consequent reduction of the smaller Mn⁴⁺ ion to larger Mn³⁺ ions, atomic absorption spectroscopy data indicate that the experimental value of lithium contents in the LiMn_1.8Li_0.1Ni_0.1O_4−ηF_η samples prepared by the method of the '645 Patent are lower than the nominally expected lithium content values (TABLE 1). This is due to a volatilization of LiF itself at the high synthesis temperature of 800° C. employed by the '645 Patent. The decrease in lithium content with increasing nominal fluorine content leads to a lowering of the oxidation state of manganese and a consequent increase in lattice parameter. Therefore, the observed increase in lattice parameter with increasing nominal fluorine content is not due to fluorine incorporation into the spinel lattice, but rather due to a volatilization of LiF. In contrast, our procedure involving the firing of already synthesized LiMn_1.8Li_0.1Ni_0.1O₄ oxide at a moderate temperature of 450° C. avoids such volatilization of lithium and helps to maximize the fluorine content in LiMn_1.8Li_0.1Ni_0.1O_4−ηF_η.

In contrast to the '645 Patent, the present invention overcomes these problems and maximizes the fluorine content, by using a low temperature procedure in which the LiMn_1.8Li_0.1Ni_0.1O₄ oxide is synthesized first by firing at about 800° C. and the oxide is then heat treated with NH₄HF₂ at a moderate temperature of about 450° C. The low temperature process employed by the present invention helps to increase the fluorine content in LiMn_1.8Li_0.1Ni_0.1O_4−ηF_η

It will thus be appreciated that the '645 Patent fails to teach the compositions of the present invention, or the methods of making or using these compositions as disclosed herein.

To facilitate the understanding of this invention, a number of terms are defined below. Terms defined herein have meanings as commonly understood by a person of ordinary skill in the areas relevant to the present invention. Terms such as “a”, “an” and “the” are not intended to refer to only a singular entity, but include the general class of which a specific example may be used for illustration. The terminology herein is used to describe specific embodiments of the invention, but their usage does not delimit the invention, except as outlined in the claims.

As used herein the term “Ampere-hour (Ah)” refers to the units used in specifying the storage capacity of a battery. For example, a battery with 1 Ah capacity can supply a current of one ampere for one hour or 0.5 A for two hours, etc. 1 Ampere-hour (Ah) is the equivalent of 3600 coulombs of electrical charge.

As used herein the term “C Rate” refers to the charging or discharging rate of a cell or battery, expressed in terms of its total storage capacity in Ah or mAh. For example, a rate of 1 C means utilization of all of the stored energy in one hour; a 0.1 C means utilization of 10% of the energy in one hour and the full energy in 10 hours; and a 5 C means full utilization of the energy in 12 minutes.

As used herein the term metal oxides include precursors of the metal oxides such as nitrates, carbonates, and acetates which can be converted to their corresponding metal oxides by heat treatment.

Substitution of fluoride ion for oxide ion in cation-substituted spinel oxide cathodes increases the reversible capacity due to a decrease in the oxidation state of Mn. Cation-substituted spinel oxyfluoride cathodes such as LiMn_1.8Li_0.1Ni_0.1O_3.79F_0.21 exhibit superior capacity retention at 60° C. with excellent rate capability compared to other spinel compositions like LiMn₂O₄, LiMn₂O_4−ηF_η, LiMn_1.8Li_0.2O₄, and LiMn_1.8Li_0.2O_4−ηF_η. The incorporation of fluoride ion in LiMn_2−y−zLi_yM_zO_4−ηF_η may range from a η of greater than about 0.0 to about 0.5; however, the range may be between about 0.05 to about 0.27, between about 0.1 to about 0.25, between about 0.1 to about 0.21, or between about 0.1 to about 0.1. The value of y in LiMn_2−y−zLi_yM_zO_4−ηF_η may be between about 0.0 to about 0.3; however, the range may be between about 0.05 to about 0.27, between about 0.1 to about 0.25, between about 0.1 to about 0.2, or between about 0.1 to about 0.15. Similarly, z in LiMn_2−y−zLi_yM_zO_4−ηF_η may be between about 0.0 to about 1; however, the range may be between about 0.1 to about 0.9, between about 0.2 to about 0.8, between about 0.3 to about 0.7, between about 0.4 to about 0.6, between about 0.5 to about 0.6, or between about 0.01 to about 5.

Lithium ion batteries currently use the layered LiCoO₂ cathodes, but the high cost and toxicity of Co have prompted the development of alternative cathodes particularly for electric vehicle and hybrid electric vehicle applications. In this regard, both spinel LiMn₂O₄ and olivine LiFePO₄ have become appealing as Mn and Fe are inexpensive and environmentally benign. However, the LiMn₂O₄ spinel cathode has been plagued by severe capacity fade at elevated temperatures. Several mechanisms such as Jahn-Teller distortion,¹ manganese dissolution into the electrolyte,^2-5 formation of two cubic phases during the charge-discharge process,^6,7 and development of microstrain due to the difference in lattice parameter Δa between the two cubic phases formed during cycling^8-11 have been proposed to account for the capacity fade.

The present inventors recognized that the cyclability at elevated temperatures, rate capability, and storage characteristics could be improved significantly by reducing the lattice parameter difference Δa between the two cubic phases formed during cycling by appropriate cationic substitutions.^9-11 For example, doubly substituted spinel compositions such as LiMn_1.85Li_0.075Ni_0.075O₄ exhibit superior electrochemical performance compared to that of the unsubstituted LiMn₂O₄.

However, the substitution of lower valent cations such as Li⁺ and Ni²⁺ for Mn^3+/4+ in LiMn_2−2yLi_yNi_yO₄ increases the average oxidation state of Mn and decreases the reversible capacity to <about 100 mAh/g. The present inventors used the partial substitution of fluoride ions for oxide ions in the cation-substituted spinel oxides to obtain the corresponding spinel oxyfluoride cathodes. In this regard, Amatucci et al.^12-14 have investigated the substitution of F⁻ for O²⁻ in Li_1+xMn_2−xO_4−ηF_η and LiMn_2−yAl_yO_4−ηF_η by synthesizing them using LiF at 800° C. and found that the fluorine substituted cathodes exhibit higher discharge capacity and better cyclability than LiMn₂O₄. More recently, Kang et al¹⁵ have also found an improvement in cyclability with Li_1.05Mn_1.85Al_0.1O_4−ηF_η synthesized at 850° C. with LiF; however, the amount of fluorine incorporated into the lattice is strongly influenced by the firing temperature and time due to the volatilization of fluorine at elevated temperatures. In order to maximize the fluorine content in the spinel lattice, the present inventors developed a low temperature procedure involving the firing of the already synthesized cation-substituted spinel oxides LiMn_2−y−zLi_yM_zO₄ with a fluorine source (preferably ammonium hydrogen fluoride NH₄HF₂) at 450° C. for a short period of 5 hours. A comparison of the cyclability and rate capability of the oxyfluoride cathodes LiMn_2−y−zLi_yM_zO_4−ηF_η (M=Mg, Al, Ti, V, Cr, Fe, Co, Ni, Cu, Zn, Zr, Nb, Mo, Ga, Sn or a combination thereof and 0≦η≦0.2) with those of the corresponding oxide cathodes and a correlation of the electrochemical performance to the lattice parameter difference Aa between the two cubic phases formed during cycling and the degree of manganese dissolution are presented.

In some embodiments the firing of the already synthesized cation-substituted spinel oxides LiMn_2−y−zLi_yM_zO₄ with fluoride source at a temperature of between 200 and 649° C., between 300-600° C., between 350-550° C., between 400-500° C., or between 425-475° C. Similarly, the time that the already synthesized cation-substituted spinel oxides LiMn_2−y−zLi_yM_zO₄ and fluoride source are fired may be varied between 2-8 hours, between 2-6 hours, between 2-5 hours, between 2-4 hours, between 3-5 hours, or between 4-5 hours.

The cation-substituted LiMn_2−y−zLi_yM_zO₄ (M=Mg, Al, Ti, V, Cr, Fe, Co, Ni, Cu, Zn, Zr, Nb, Mo, Ga, Sn or a combination thereof) spinel oxides were synthesized by firing required amounts of Li₂CO₃ and Mn₂O₃ with TiO₂, NiO, or CuO at 800° C. for 48 hours in air. The fluorine-substituted LiMn_2−y−zLi_yM_zO_4−ηF_η oxyfluorides were prepared by firing the LiMn_2−y−zLi_yM_zO₄ oxide with a required amount of ammonium hydrogen difluoride (NH₄HF₂) at 450° C. for 5 hours in air. The skilled artisan will recognize that other similar compounds with similar characteristics may be substituted for ammonium hydrogen difluoride, e.g., ammonium fluoride NH₄F. Chemical extraction of lithium was carried out by stirring the LiMn_2−y−zLi_yM_zO_4−ηF_η powder with an acetonitrile solution of the oxidizer NO₂BF₄ for two days under argon atmosphere, followed by washing the products with acetonitrile.¹⁶ The lithium contents in the products were determined by atomic absorption spectroscopy (AAS) and the average oxidation state of manganese was determined by a redox titration involving sodium oxalate and potassium permanganate. Lattice parameters of the initial samples as well as the two cubic phases formed during chemical delithiation were determined by the Rietveld analysis of the X-ray diffraction (XRD) data.¹⁷ The degree of manganese dissolution was assessed by soaking the parent sample powders in the electrolyte containing 1 M LiPF₆ in 1:1 ethylene carbonate (EC) and diethyl carbonate (DEC) at 55° C. for seven days and determining the amount of manganese in the electrolyte with AAS.

Electrochemical performances were evaluated with CR2032 coin cells fabricated with metallic lithium anode, 1 M LiPF₆ in 1:1 ethylene carbonate (EC) and diethyl carbonate (DEC) electrolyte, Celgard polypropylene separator, and the cathodes. The cathodes were prepared by mixing the LiMn_2−y−zLi_yM_zO_4−ηF_η powders with about 20 weight percent conductive carbon and 5 weight percent polytetrafluoroethylene (PTFE) binder, rolling the mixture into thin sheets, and cutting into circular electrodes of 0.64 cm² area. The skilled artisan will recognize that the electrodes may be of shapes other than circular (e.g., polygonal, rectangular, oval, square, etc.) and that the electrode area may be any range.

Electrochemical data was collected between about 3.5 and 4.3 volts at both room temperature and about 60° C. at various rates ranging from C/10 to 4C. The chemical, structural, and electrochemical characterization data of spinel manganese oxyfluorides and the average oxidation state values of the transition metal ions determined by the redox titration are given in TABLE 2 below.

TABLE 2
					Capacity loss
			Lattice	Initial	in	Mn
Sample		Mn	parameter	capacity	50 cycles (%)	dissolutionb
#	Composition	valencea	(Å)	(mAh/g)	25° C.	60° C.	(%)
1	Li Mn2O4	3.50	8.2451	119	35.2	53.5	3.2
2	Li Mn2O3.92F0.08	3.46	8.2497	119	29.4	43.3	2.6
3	LiMn1.8Li0.2O4	3.78	8.2002	78	2.5	4.4	1.5
4	LiMn1.8Li0.2O3.88F0.12	3.71	8.2034	86	1.2	3.0	1.0
5	LiMn1.8Li0.2O3.79F0.21	3.66	8.2113	100	2.3	3.4	1.1
6	LiMn1.8Li0.1Ti0.1O4	3.61	8.2142	103	19.2	28.5	2.5
7	LiMn1.8Li0.1Ti0.1O3.9F0.1	3.56	8.2191	109	11.3	20.4	1.9
8	LiMn1.8Li0.1Cu0.1O4	3.72	8.2069	86	9.5	18.8	2.0
9	LiMn1.8Li0.1Cu0.1O3.9F0.1	3.67	8.2087	93	6.4	11.1	1.7
10	LiMn1.8Li0.1Ni0.1O4	3.72	8.2091	82	1.1	2.6	1.1
11	LiMn1.8Li0.1Ni0.1O3.9F0.1	3.67	8.2138	90	0.9	2.1	0.6
12	LiMn1.8Li0.1Ni0.1O3.8F0.2	3.61	8.2252	104	0.9	1.9	0.8
aCalculated by assuming Li+, Ti4+, Ni2+, Cu2+, and F−.
b% dissolution based on sample weight.

With a given cationic composition, the oxidation state decreases with fluorine substitution due to the replacement of the divalent O²⁻ ions by the monovalent F⁻ ions. The fluorine contents in the synthesized samples were calculated based on the lithium content and the average oxidation state values of the transition metal ions obtained from, respectively, the AAS and redox titration data, employing charge neutrality principle and assuming the total anion (O+F) content to be 4.0. Based on the analytical data, a significant amount of fluorine (0≦η≦0.21) has been incorporated into the spinel lattice. The firing of the already synthesized oxide powders with NH₄HF₂ at a low temperature of about 450° C. helps to minimize the volatilization problems and maximize the fluorine content in the samples compared to the conventional high temperature (about 800° C.) synthesis of LiMn₂O_4−ηF_η with LiF as a fluorine source;^12-14 NH₄HF₂ decomposes above about 220° C. and acts as a facile fluorine source.

FIG. 1 is an image of the X-ray diffraction patterns of selected parent LiMn_2−y−zLi_yM_zO_4−ηF_η and chemically delithiated Li_1−xMn_2−y−zLi_yM_zO_4−ηF_η spinel cathodes. An enlargement of the patterns over a small 2θ region of about 27 to 330 and about 63 to 67° to illustrate, respectively, the presence of Mn₅O₈ impurity phase and the formation of two cubic phases for the delithiated compositions is shown on the right. The reflections marked with * refer to Mn₅O₈ impurity.

FIG. 1 compares the XRD patterns of some spinel oxide and oxyfluoride compositions. The cation-substituted oxyfluorides such as LiMn_1.8Li_0.2O_3.79F_0.21 and LiMn_1.8Li_0.1Ni_0.1O_3.8F_0.2 exhibit patterns similar to that of the parent cation-substituted oxides without any impurity phases. Attempts to incorporate more than about 0.2 fluorine into the cation-substituted spinel oxides resulted in the formation of Mn₅O₈ as an impurity phase. In contrast, a trace amount of Mn₅O₈ impurity phase was found even at a low fluorine content of about 0.08 (e.g., LiMn₂O_3.92F_0.08) in the absence of cation substitutions and the intensity of the reflections corresponding to Mn₅O₈ impurity increased with increasing fluorine content in LiMn₂O_4−ηF_η. This could be due to the difficulty of lowering the oxidation state of Mn significantly below about 3.5+ in the case of LiMn₂O_4−ηF_η (without any cation substitution for Mn). TABLE 1 gives the lattice parameter values of the LiMn_2−y−zLi_yM_zO_4−ηF_η samples. With a given cationic composition, the lattice parameter increases with increasing fluorine content due to a reduction of the smaller Mn⁴⁺ ions into larger Mn³⁺ ions, confirming the replacement of O²⁻ by F⁻ in the bulk of the spinel lattice. This observation of the increase in lattice parameters is in agreement with that found before with the Li_1+xMn_2−x−yAl_yO_4−ηF_η system.^14,15

FIG. 2 compares the cycling performances of the LiMn₂O_4−ηF_η, LiMn_1.8Li_0.2O_4−ηF_η, and LiMn_1.8Li_0.1Ni_0.1O_4−ηF_η cathodes at room temperature and about 60° C. at C/5 rate. FIG. 2 (top graph) compares the electrochemical cycling performances of the cathodes at about 25° C. FIG. 2 (bottom graph) compares the electrochemical cycling performances of the cathodes at about 60° C. of LiMn_2−y−zLi_yM_zO_4−ηF_η: (●) LiMn₂O₄, (◯) LiMn₂O_3.92F_0.08, (▴) LiMn_1.8Li_0.2O₄, (Δ) LiMn_1.8Li_0.2O_3.88F_0.12, (∇) LiMn_1.8Li_0.2O_3.79F_0.21, (▪) LiMn_1.8Li_0.1Ni_0.1O₄, (□) LiMn_1.8Li_0.1Ni_0.1O_3.9F_0.1, and (⋄) LiMn_1.8Li_0.1Ni_0.1O_3.8F_0.2. The initial capacity values and the percent capacity loss after 50 cycles at about 25° C. and about 60° C. are summarized in TABLE 1 above. The oxyfluoride spinel compositions exhibit up to about 20 mAh/g higher capacities than the corresponding oxide counterparts due to a lowering of the oxidation state of manganese. For example, LiMn_1.8Li_0.1Ni_0.1O₄, LiMn_1.8Li_0.1Ni_0.1O_3.9F_0.1, and LiMn_1.8Li_0.1Ni_0.1O_3.8F_0.2 exhibit initial capacities of 82, 90, and 104 mAh/g with capacity fades of only 1.1, 0.9, and 0.9%, respectively, in about 50 cycles at room temperature. LiMn_1.8Li_0.1Ni_0.1O₄, LiMn_1.8Li_0.1Ni_0.1O_3.9F_0.1, and LiMn_1.8Li_0.1Ni_0.1O_3.8F_0.2 show capacity fades of, respectively, 2.6, 2.1, and 1.9% in 50 cycles at about 60° C. compared to around 50% fade for LiMn₂O₄. LiMn₂O_3.92F_0.08 also exhibits an improvement in the capacity retention compared to LiMn₂O₄ as has been found before,^12-14 but without any increase in the initial capacity, possibly due to the presence of the electrochemically inactive impurity phase Mn₅O₈.^13,18 Although fluorine substitution is known before in the literature to improve the cyclability as in the cases of Li_1+xMn_2−xO_4−ηF_η,^12-14 LiMn_2−yAl_yO_4−η,^12-14 and Li_1.05Mn_1.85Al_0.1O_4−ηF_η,¹⁵ the substitution of fluorine in certain optimized cation-substituted compositions such as LiMn_1.8Li_0.1Ni_0.1O_3.8F_0.2 offers much superior capacity retention at elevated temperatures without sacrificing the capacity values significantly (>100 mAh/g). Furthermore, the improved capacity retention with fluorine substitution in the spinels is also consistent with similar observations made recently with layered oxides by Kang et al^19,20 and Kim et al.²¹

FIG. 3 is a graph comparing the discharge profiles at various C rates, illustrating the rate capabilities of LiMn₂O₄, LiMn_1.8Li_0.2O_4−ηF_η, and LiMn_1.8Li_0.1Ni_0.1O_4−ηF_η at different rates (C/10 to 4C) after charging up to about 4.3 V at C/10 rate. The cation-substituted oxide samples LiMn_1.8Li_0.2O₄ and LiMn_1.8Li_0.1Ni_0.1O₄ retain, respectively, 95% and 98% of their capacity on going from C/10 to 4C rate, but with low capacity values of about 75 and about 81 mAh/g at a 4C rate. In contrast, the cation-substituted oxyfluoride samples LiMn_1.8Li_0.2O_3.79F_0.21 and LiMn_1.8Li_0.1Ni_0.1O_3.8F_0.2 retain, respectively, 92% and 96% of their C/10 capacity at 4C rate, but still with reasonable capacities of about 92 and about 100 mAh/g at 4C rate. Thus the cation-substituted oxyfluorides exhibit a combination of excellent cyclability with acceptable capacity values without sacrificing the rate capability significantly.

The evolution of the cubic to cubic phase transition and the two-phase region that occur around (1−x)≈0.3 to 0.5 during the charge-discharge process of the spinel cathodes was monitored. Oxide spinel cathodes studied have revealed a correlation of the electrochemical performance to the lattice parameter difference Aa between the two cubic phases formed.^9,10 FIG. 1 compares the XRD patterns of the Li_1−xMn₂O_4−ηF_η, Li_1−xMn_1.8Li_0.2O_4−ηF_η, and Li_1−xMn_1.8Li_0.1Ni_0.1O_4−ηF_η (0.35≦(1−x)≦0.4) samples obtained by chemical delithiation with an acetonitrile solution of NO₂BF₄. While Li_0.37Mn₂O₄ shows two distinct peaks around 2θ≈65° corresponding to the two cubic phases with a larger lattice parameter difference Δa, the fluorine-substituted Li_1−xMn₂O_3.92F_0.08 (without cation substitution) shows a reduced separation between the two peaks. On the other hand, both Li_0.37Mn_1.8Li_0.2O_3.79F_0.21 and Li_0.34Mn_1.8Li_0.1Ni_0.1O_3.8F_0.2 (with cation substitutions) show only a broad peak due to a much smaller lattice parameter difference Δa between the two cubic phases. The broad reflections could nevertheless be resolved by Rietveld analysis to obtain the lattice parameters for the two cubic phases.

FIG. 4 (top graph) shows graphs that correlate the capacity fade in about 50 cycles at about 60° C. to the degree of manganese dissolution and FIG. 4 (bottom graph) shows graphs that correlate the capacity fade in about 50 cycles at 60° C. to the lattice parameter difference Δa between the two cubic phases formed during the charge-discharge process. Closed squares and open triangles refer, respectively, to the oxide and oxyfluoride cathodes. The numbers refer to the sample numbers in TABLE 2. FIG. 4 (bottom graph) correlates the capacity fade to the lattice parameter difference Δa. Both the cationic and fluorine substitutions lower Δa, and the capacity fade decreases with decreasing Δa. The Δa values vary slightly with the lithium content, and the Δa values used in FIG. 4 are the maximum values in the two-phase region with (1−x)≈0.35−0.40. FIG. 4 (top graph) also compares the degree of manganese dissolution and correlates the capacity fade to manganese dissolution. The capacity fade decreases with decreasing degree of manganese dissolution, confirming the manganese dissolution as a cause of capacity fade as has been widely believed in the literature. The degree of manganese dissolution decreases significantly with some cationic substitutions such as the co-substitution of Li and Ni for Mn compared to Li and Ti for Mn. More importantly, with a given cationic substitution, the anionic substitution with fluorine causes a further reduction in the degree of manganese dissolution. The surface passivation by fluoride ions as well as the more ionic Mn—F bond compared to the Mn—O bond may lead to a suppression of manganese dissolution. Manganese dissolution bears a relationship to the lattice parameter difference Δa, and the capacity fade decreases with both decreasing Δa and manganese dissolution as seen in FIG. 4. Thus, the reduced interfacial lattice strain due to the smaller Δa in the two-phase region as well as the suppressed manganese dissolution leads to improved capacity retention.

The superior electrochemical performance of LiMn_1.8Li_0.1Ni_0.1O_3.79F_0.21 with a capacity of 104 mAh/g is found to be due to a significantly suppressed manganese dissolution caused by a much smaller lattice parameter difference between the two cubic phases formed during the charge-discharge process. The study demonstrates that appropriate cationic and anionic substitutions in the manganese-based spinel cathodes may offer a viable strategy to develop them for EV and HEV applications. FIG. 5 is a graph that compares the percentage capacity retention after storing at 60° C. for 7 days at different depth of discharge (DOD): (●) LiMn₂O₄, (▴) LiMn_1.8Li_0.2O₄, (∇) LiMn_1.8Li_0.2O_3.79F_0.21, and (⋄) LiMn_1.8Li_0.1Ni_0.1O_3.8F_0.2. The storage performances were evaluated by subjecting the coin cells to one charge-discharge cycle at room temperature between 4.3 and 3.5 V, followed by discharging to various depths of discharge (DOD) in the second cycle. The sample was then stored at 60° C. for 7 days at various DOD. The second discharge cycle was completed after cooling to ambient temperature. The full discharge capacity in the third cycle was evaluated at room temperature. The percent capacity retention was obtained as a ratio of the third discharge capacity to the first discharge capacity. Although LiMn₂O₄ loses a significant amount of capacity after storage (20-40%), the cation-substituted oxyfluorides retain >95% of their initial capacity, illustrating excellent storage characteristics. Thus, the oxyfluoride cathodes offer a combination of excellent cyclability and storage characteristics.

The major issue with the spinel cathodes is the severe capacity fade at elevated temperatures, which is largely believed to be due to the dissolution of manganese from the lattice into the electrolyte and then its migration into and interaction with the carbon anode. The manganese dissolution is due to a disproportionation of the Mn³⁺ ions into Mn⁴⁺ and Mn²⁺ ions in the presence of trace amounts of protons (acidic HF) generated by LiPF₆ and trace amounts of water present in the electrolyte. Cationic and anionic (fluorine) substitutions help to reduce significantly the manganese dissolution and the lattice parameter difference Δa between the two cubic phases formed during the charge-discharge process, which lead to good electrochemical performance. Alternatively, the protons generated may be captured within another material in the beginning stages of the charge-discharge process to lower the manganese dissolution.

Chemical delithiation studies with an oxidizer NO₂BF₄ in acetonitrile medium have shown that layered oxide cathode compositions such as Li_1−xCoO₂ and Li_1−xMn_0.5Ni_0.5O₂, and Li_1−xMn_1/3Ni_1/3Co_1/3O₂ incorporate protons into the lattice due to an ion exchange of Li⁺ with H⁺ at deep lithium extraction.²² One way to suppress manganese dissolution from the spinel cathodes is to employ a mixed cathode consisting of predominantly the spinel and small amounts of a layered oxide, charge the mixture initially to high enough voltages (e.g., about 4.7 V) to overcharge (deep lithium extraction) the layered oxide and trap the protons into the over-charged layered oxide lattice. The mixture can then be cycled under the normal operating voltage region of about 3.5 to about 4.3 volts. The present invention includes a mixture of an optimized cation- and anion-substituted spinel cathode and a layered oxide cathode such as LiCoO₂ and LiMn_0.5Ni_0.5O₂.

FIG. 6 is a graph of the cycling performance of lithium ion cells having spinel LiMn₂O₄, a mixture of spinel LiMn_1.85Li_0.075Ni_0.04Al_0.035O₄ and layered LiCoO₂, and a mixture of spinel LiMn_1.8Li_0.1Ni_0.1O_3.8F_0.2 and layered LiCoO₂ cathodes and commercial carbon anode at 60° C. at C/5 rate. The studies were carried out by first charging up to 4.7 volts in the first cycle and then cycling between 4.3 and 3.5 volts at 60° C.: (●) LiMn₂O₄, (▴) LiMn_1.85Li_0.075Ni_0.04Al_0.035O₄ (Δ) 80 wt % LiMn_1.85Li_0.075Ni_0.04Al_0.035O₄ and 20 wt % LiCoO₂, (∇) 70 wt % LiMn_1.85Li_0.075Ni_0.04Al_0.035O₄ and 30 wt % LiCoO₂, (▪) LiMn_1.8Li_0.1Ni_0.1O_3.8F_0.2, and (□) 70 wt % LiMn_1.8Li_0.1Ni_0.1O_3.8F_0.2 and 30 wt % LiCoO₂. Each lithium ion cell was charged up to 4.7 volts in the first cycle and allowed to rest in open-circuit (no load applied) for 2 hours. The lithium ion cells were then cycled between 3.5 and 4.3 volts. While LiMn₂O₄ shows severe capacity fade of 33% after 30 cycles with a continuous decline in capacity, the cation-substituted LiMn_1.85Li_0.075Ni_0.04Al_0.035O₄ exhibits a better cycling performance, with the capacity value becoming more stable after 7 cycles.

The mixtures of spinel and layered oxide cathode not only provide much better cyclability but also a significant increase in capacity. For example, LiMn_1.85Li_0.075Ni_0.04Al_0.035O₄, a mixture of 80 wt % LiMn_1.85Li_0.075Ni_0.04Al_0.035O₄ and 20 wt % LiCoO₂, and a mixture of 70 wt % LiMn_1.85Li_0.075Ni_0.04Al_0.035O₄ and 30 wt % LiCoO₂ exhibit initial capacities of 87, 91, and 103 mAh/g with capacity fades of only 21.9, 13.8, and 14.4%, respectively, in 30 cycles. Furthermore, an initial capacity of 102 mAh/g was achieved with a capacity fade of 11.2% with a cathode mixture of 70 wt % LiMn_1.8Li_0.1Ni_0.1O_3.8F_0.2 and 30 wt % LiCoO₂.

Similar improvements in cyclability are also seen with lithium ion cells fabricated with a mixture of spinel and layered LiNi_0.5Mn_0.5O₂ oxide cathode. FIG. 7 is a graph of the cycling performance of lithium ion cells having various ratios of spinel and layered oxide mixture cathodes and commercial carbon anode. The studies were carried out by first charging up to 4.7 volts in the first cycle and then cycling between 4.3 and 3.5 volts at 60° C.: (▴) LiMn_1.85Li_0.075Ni_0.04Al_0.035O₄ and (Δ) 80 wt % LiMn_1.85Li_0.075Ni_0.04Al_0.035O₄ and 20 wt % LiNi_0.5Mn_0.5O₂. As seen in FIG. 7, a mixture of 80 wt % LiMn_1.85Li_0.075Ni_0.04Al_0.035O₄ and 20 wt % LiNi_0.5Mn_0.5O₂ shows better cyclability than the corresponding spinel cathode alone. Further work with this strategy is in progress.

The manganese dissolution with lithium ion cells (coin cells) fabricated with the mixture of spinel and layered cathodes has also been studied. The mixture in deed shows lower manganese dissolution compared to the corresponding spinel alone cathodes, demonstrating that the layered oxide cathodes could help to capture the protons on initially subjecting the cells to over-charge to >4.3 volts.

In addition, the surface of the carbon anode may be modified or coated with an oxide anode like spinel Li₄Ti₅O₁₂ or TiO₂. Such a surface modification will help to avoid the interaction of the dissolved manganese with the carbon anode and the consequent degradation in electrochemical performance. Advantageously, both spinel Li₄Ti₅O₁₂ or TiO₂ will contribute to the anode capacity. These materials could be generated on the graphite surface by solution-based techniques, followed by firing at moderate temperatures between 300 and 900° C. in an inert atmosphere. Such surface modification of carbon anodes could also be adopted with other oxides that may or may not contribute to capacity, e.g., oxides of Mg, Al, Si, V, Cr, Fe, Co, Ni, Cu, Zn, Ga, Ge, Y, Zr, Nb, Mo, Cd, In, Sn, Sb, La, Ce, Hf, Ta, W, and Bi. The surface modification could also be pursued with conductive polymers, e.g., polyaniline and polypyrrole. The amount of the surface modifying material could be 1 wt % to 10 wt %. The modification of the carbon surface with other species may eliminate the direct interaction of any dissolved manganese from the cation-substituted spinel oxide or oxyfluoride cathodes and thereby provide long term stability and good cyclability to the lithium ion cells.

In addition, dopants may be incorporated into the present invention. Dopants as used herein are elements or compounds selected to demonstrate the concept. The dopants are used to replace the transition metal M and are not used to take the place of lithium ions in the lithium metal oxide. For example, dopants for use in the present invention include metals and nonmetals such as Mg, Al, Ti, V, Cr, Fe, Co, Ni, Cu, Zn, Zr, Nb, Mo, Ga, Sn, Si, and B and combinations thereof.

Although the present invention contemplates many fluorine sources known to the skilled artisan (e.g., NH₄HF₂), other fluorine sources may be used as well. For example, the spinel oxide powder may be dispersed in a dilute hydrofluoric acid solution, evaporated, and fired at lower temperatures (200-500° C.) to obtain the oxyfluoride compositions. Ammonium hydrogen fluoride or ammonium fluoride may be dissolved in a solvent (e.g., methanol or ethanol) and the spinel oxide powder may be disperse therein, evaporated, and fired at lower temperatures (e.g., 200-500° C.) to obtain the oxyfluoride compositions. Ammonium hydrogen fluoride may be dissolved in a solvent (e.g., methanol or ethanol) and the spinel oxide powder dispersed therein, refluxed, filtered, and fired at lower temperatures (e.g., 200-500° C.) to obtain the oxyfluoride compositions. Ammonium hydrogen fluoride may be dissolved in a solvent like ethanol, iso-propanol, or water, and the spinel oxide powder dispersed therein. The mixture may be kept in an autoclave under hydrothermal or solvothermal condition at 80-250° C., filtered, and fired at lower temperatures (e.g., 200-500° C.) to obtain the oxyfluoride compositions. Also, the oxide spinel powder may be mixed with ammonium hydrogen fluoride solid, ground, pelletized, and fired at between about 300 and 500° C.

It is contemplated that any embodiment discussed in this specification can be implemented with respect to any method, kit, reagent, or composition of the invention, and vice versa. Furthermore, compositions of the invention can be used to achieve methods of the invention.

It will be understood that particular embodiments described herein are shown by way of illustration and not as limitations of the invention. The principal features of this invention can be employed in various embodiments without departing from the scope of the invention. Those skilled in the art will recognize, or be able to ascertain using no more than routine experimentation, numerous equivalents to the specific procedures described herein. Such equivalents are considered to be within the scope of this invention and are covered by the claims.

All publications and patent applications mentioned in the specification are indicative of the level of skill of those skilled in the art to which this invention pertains. All publications and patent applications are herein incorporated by reference to the same extent as if each individual publication or patent application was specifically and individually indicated to be incorporated by reference.

The use of the word “a” or “an” when used in conjunction with the term “comprising” in the claims and/or the specification may mean “one,” but it is also consistent with the meaning of “one or more,” “at least one,” and “one or more than one.” The use of the term “or” in the claims is used to mean “and/or” unless explicitly indicated to refer to alternatives only or the alternatives are mutually exclusive, although the disclosure supports a definition that refers to only alternatives and “and/or.” Throughout this application, the term “about” is used to indicate that a value includes the inherent variation of error for the device, the method being employed to determine the value, or the variation that exists among the study subjects.

As used in this specification and claim(s), the words “comprising” (and any form of comprising, such as “comprise” and “comprises”), “having” (and any form of having, such as “have” and “has”), “including” (and any form of including, such as “includes” and “include”) or “containing” (and any form of containing, such as “contains” and “contain”) are inclusive or open-ended and do not exclude additional, unrecited elements or method steps.

The term “or combinations thereof” as used herein refers to all permutations and combinations of the listed items preceding the term. For example, “A, B, C, or combinations thereof” is intended to include at least one of: A, B, C, AB, AC, BC, or ABC, and if order is important in a particular context, also BA, CA, CB, CBA, BCA, ACB, BAC, or CAB. Continuing with this example, expressly included are combinations that contain repeats of one or more item or term, such as BB, AAA, AB, BBC, AAABCCCC, CBBAAA, CABABB, and so forth. The skilled artisan will understand that typically there is no limit on the number of items or terms in any combination, unless otherwise apparent from the context.

All of the compositions and/or methods disclosed and claimed herein can be made and executed without undue experimentation in light of the present disclosure. While the compositions and methods of this invention have been described in terms of preferred embodiments, it will be apparent to those of skill in the art that variations may be applied to the compositions and/or methods and in the steps or in the sequence of steps of the method described herein without departing from the concept, spirit and scope of the invention. All such similar substitutes and modifications apparent to those skilled in the art are deemed to be within the spirit, scope and concept of the invention as defined by the appended claims.

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Claims

1. A method of making an oxyfluoride composition comprising the steps of: firing a solid state mixture comprising lithium, manganese, and M to obtain a first composition having the formula LiMn2−y−zLiyMzO4;mixing the first composition with a fluorine source to form a second mixture;and heating the second mixture at a temperature within the range of about 200° C. to about 700° C. for 2 hours to 8 hours to form a cation-substituted, fluorine-substituted LiMn2−y−zLiyMzO4−ηFη spinel oxide structure, wherein M is a metal, y is within the range of about 0 to about 0.3, z is within the range of about 0 to about 1.0, and wherein η is greater than 0 and less than about 0.5, and wherein the fluorine source is a solid or liquid selected from the group consisting of NH4HF2, ammonium fluoride, or hydrogen fluoride.

2. The method of claim 1, wherein M is selected from the group consisting of Mg, Al, V, Cr, Fe, Ti, Co, Ni, Cu, Zn, Zr, Nb, Mo, Ga, Sn and combinations thereof.

3. The method of claim 1, wherein the fluorine source comprises NH4HF2.

4. The method of claim 1, wherein y is within the range of about 0 to about 0.3, z is within the range of about 0 to about 1.0, and η is within the range of about 0.05 to about 0.25.

5. The method of claim 1, wherein the first composition is heated in the presence of the fluorine source to a temperature within the range of about 425° C. to about 500° C.

6. The method of claim 1, wherein the cation-substituted fluorine-substituted LiMn2−y−zLiyMzO4−ηFη spinel oxide structure is selected from the group consisting of LiMn1.8Li0.2O3.88F0.12, LiMn1.8Li0.2O3.79F0.21, LiMn1.8Li0.1Ti0.1O3.9F0.1, LiMn1.8Li0.1Cu0.1O3.9F0.1, LiMn1.8Li0.1Ni0.1O3.9F0.1, and LiMn1.8Li0.1Ni0.1O3.8F0.2.

7. The method of claim 1, wherein the second composition, when incorporated in a lithium-ion battery, has a capacity greater than about 80 mAh/g.

8. The method of claim 1, wherein M is Ni.

9. The method of claim 1, wherein M is Ti.

10. The method of claim 1, wherein M is Cu.

11. The method of claim 1, wherein η is within the range of about 0.05 to about 0.27.

12. The method of claim 1, wherein η is within the range of about 0.1 to about 0.25.

13. The method of claim 1, wherein y is within the range of about 0.05 to about 0.27.

14. The method of claim 1, wherein y is within the range of about 0.1 to about 0.25.

15. The method of claim 1, wherein y is within the range of about 0.1 to about 0.2.

16. The method of claim 1, wherein y is within the range of about 0.1 to about 0.15.

17. The method of claim 1, wherein z is within the range of about 0.1 to about 0.9.

18. The method of claim 1, wherein y is within the range of about 0.2 to about 0.8.

19. The method of claim 1, wherein y is within the range of about 0.3 to about 0.7.

20. The method of claim 1, wherein y is within the range of about 0.4 to about 0.6.

21. The method of claim 1, wherein the first composition is heated in the presence of the fluorine source at a temperature within the range of about 200° C. to about 649° C.

22. The method of claim 1, wherein the first composition is heated in the presence of the fluorine source at a temperature within the range of about 300° C. to about 600° C.

23. The method of claim 1, wherein the first composition is heated in the presence of the fluorine source at a temperature within the range of about 350° C. to about 550° C.

24. The method of claim 1, wherein the first composition is heated in the presence of the fluorine source at a temperature within the range of about 400° C. to about 500° C.

25. The method of claim 1, wherein the first composition is heated in the presence of the fluorine source at a temperature within the range of about 425° C. to about 475° C.

26. The method of claim 1, wherein the first composition is heated in the presence of the fluorine source for about 2 hours to about 6 hours.

27. The method of claim 1, wherein the first composition is heated in the presence of the fluorine source for about 2 hours to about 5 hours.

28. The method of claim 1, wherein the first composition is heated in the presence of the fluorine source for about 2 hours to about 4 hours.

29. The method of claim 1, wherein the fluorine source comprises NH4F.

30. The method of claim 1, wherein the second composition is LiMn1.8Li0.2O3.88F0.12.

31. The method of claim 30, wherein the fluorine source comprises NH4HF2.

32. The method of claim 31, wherein the first composition is heated in the presence of a fluorine source at a temperature within the range of about 400° C. to about 500° C.

33. The method of claim 1, wherein the second composition is LiMn1.8Li0.2O3.79F0.21.

34. The method of claim 33, wherein the fluorine source comprises NH4HF2.

35. The method of claim 34, wherein the first composition is heated in the presence of a fluorine source at a temperature within the range of about 400° C. to about 500° C.

36. The method of claim 1, wherein the second composition is LiMn1.8Li0.1Ti0.1O3.9F0.1.

37. The method of claim 36, wherein the fluorine source comprises NH4HF2.

38. The method of claim 37, wherein the first composition is heated in the presence of a fluorine source at a temperature within the range of about 400° C. to about 500° C.

39. The method of claim 1, wherein the second composition is LiMn1.8Li0.1Cu0.1O3.9F0.1.

40. The method of claim 39, wherein the fluorine source comprises NH4HF2.

41. The method of claim 40, wherein the first composition is heated in the presence of a fluorine source at a temperature within the range of about 400° C. to about 500° C.

42. The method of claim 1, wherein the second composition is LiMn1.8Li0.1Ni0.1O3.9F0.1.

43. The method of claim 42, wherein the fluorine source comprises NH4HF2.

44. The method of claim 43, wherein the first composition is heated in the presence of a fluorine source at a temperature within the range of about 400° C. to about 500° C.

45. The method of claim 1, wherein the second composition is LiMn1.8Li0.1Ni0.1O3.8F0.2.

46. The method of claim 45, wherein the fluorine source comprises NH4HF2.

47. The method of claim 46, wherein the first composition is heated in the presence of a fluorine source at a temperature within the range of about 400° C. to about 500° C.