Patent Application
20110250508
The present invention relates to a positive electrode material which is a blended combination of lithium nickel cobalt oxide (and aluminum substituted compounds thereof) and lithium nickel manganese cobalt oxide, that may be used in a non-aqueous electrolyte lithium secondary battery.
Lithium nickel cobalt oxide (LNCO) is a well known lithium ion battery (LIB) cathode material. Its attributes are high specific capacity, measured in units of Coulombs/g, or, more commonly, Ah/kg, and high rate (power) capability. However, LNCO at temperatures of approximately 200° C. or higher, and when in the charged state, can oxidize the organic electrolyte in an LIB cell, resulting in thermal runaway or degradation of the battery components. This undesirable oxidation is due to the release of oxygen from the Ni4+ and Co4+ oxides in the structure of the charged cathode and from NiO on the surface of the crystallites.
The overall safety of an LIB is an issue of cell design and/or battery pack design. Safety in an LIB design can be influenced by choices among electrolyte, separator, anode, and cell overcharge protection circuitry. However, for consumer electronics such as cell phones and laptop computers, which require high energy cells, and handheld power tools, which require high energy and power cells, LNCO has not been used due to concerns over thermal runaway as discussed. If a way could be found to utilize commercially available LNCO in an LIB by enhancing thermal stability, this would represent a useful contribution to the art.
Lithium nickel manganese cobalt oxide (LNMCO) has the same crystallographic structure (O3) as LNCO, that is, layered. The addition of manganese to the metal slab layer in the material increases the safety of the material by decreasing the amount of oxygen released during thermal decomposition. In addition, when additional “excess” lithium is added (i.e. lithium that occupies sites in the metal slab), the material is further stabilized by creating a highly stable Li2MnO3 (lithium manganite)-like rock salt structure within the material. At charging voltages typically used in LIB's (≦4.4V), LNMCO materials have lower specific capacity than LNCO materials.
Cathode materials derived from lithium manganese oxide spinal (LiMn2O4) and LNCO are known. However, the resulting spinet-type structures are not layered, and contain relatively high amounts of manganese.
LNMCO, its addition derivatives, and LNCO materials all have a layered structure or a tunnel structure capable of absorbing or desorbing (intercalating or deintercalating) lithium ions in a reversible manner. If a way could be found to combine LNCMO and LNCO in a blend that retained relatively high specific capacity while enhancing thermal stability of the cathode-electrolyte system, this would also represent a useful contribution to the art.
Furthermore, non-aqueous electrolyte secondary batteries comprising a lithium negative electrode are highly promising as the power source for driving cordless electronic or electric appliances because they generate a high voltage, providing high energy density. However, in order to satisfy a recent demand for high energy density, it is necessary to obtain a higher capacity. Thus, a need exists for improved battery designs incorporating stable active positive electrode materials that can be used in secondary LIB's.
In one embodiment, the present invention describes a positive electrode active material blend comprising
xLNMCO(1−x)LNM1O where 0<x<1 and M1 is at least one of Co or Al;
wherein LNMCO is Li(1+y)M2(1−y)O2 where 0≦y≦0.9 and M2=MnaNibCOc where a+b+c=1 and (1+y)/(1−y)−1 and 0<b/c≦100; and
wherein LNM1O is selected from the group consisting of LiNidCoeO2 where d+e=1 and 0<d/e≦100; and LiNi1−(z+z′)COzAlz′O2 where 0<z+z′<1.
in another embodiment, the present invention provides a non-aqueous electrolyte lithium secondary battery comprising a positive electrode, a negative electrode, and a non-aqueous electrolyte, wherein the positive electrode comprises a blend xLNMCO(1−x)LNM1O where 0<x<1 and M1 is at least one of Co or Al;
wherein LNMCO is Li(1+y)M2(1−y)O2 where 0≦y≦0.9 and M2=MnaNibCoc where a+b+c=1 and (1+y)/(1−y)−1≦a≦1 and 0<b/c≦100; and
wherein LNM1O is selected from the group consisting of LiNidCoeO2 where d+e=1 and 0<d/e≦100; and LiNi1−(z+Z′)COzAlz′O2 where 0<z+z′<1.
The present invention provides positive electrode materials for use in a battery which are a blended combination of lithium nickel cobalt oxide (and aluminum substituted compounds thereof) and lithium nickel manganese cobalt oxide, that may be used in a non-aqueous electrolyte lithium secondary battery.
The term “cycle” refers to a combined charge one-half cycle and a discharge one-half cycle, whereby the cell or battery takes in and stores electrical energy in a charge one-half cycle and releases electrical energy in a discharge one-half cycle.
The term “cathode” refers to an electrode containing a compatible cathodic material which functions as a positive pole (cathode) in a secondary electrolytic cell and which is capable of being recharged (recycled).
The term “lithium anode” or “lithium negative electrode” refers to anodes comprising lithium, including metallic lithium, lithium alloys, such as alloys of lithium with aluminum, mercury, zinc, and the like, and intercalation based anodes containing lithium such as those based on carbon, vanadium oxides tungsten oxides, and the like.
The term “electrolyte solvent” or simply “solvent” refers to the organic solvent used for the purpose of solubilizing salts during operation of electrochemical cells. The solvent can be any low voltage aprotic polar solvent. Preferably, these materials are characterized by a boiling point greater than about 85° C. Suitable electrolyte solvents include, for example, propylene carbonate, ethylene carbonate, dimethyl carbonate, diethyl carbonate, ethyl methyl carbonate, diethyl pyrocarbonate, 1,2-dimethoxyethane, 1,2-diethoxyethane, gamma-butyrolactone, tetrahydrofuran, 2-methyltetrahydrofuran, 1,3-dioxolane, 4-methyl-1,3-dioxolane, diethyl ether, sulfolane, acetonitrile, propionitrile, glutaronitrile, anisole, pyrrolidinone, glyme, diglyme, triglyme, tetraglyme, dimethyl sulfoxide, and the like, or mixtures thereof. Preferred solvents include mixtures of organic carbonates.
The term “salt” refers to any ion conducting inorganic salt which is suitable for use in a non-aqueous electrolyte. Representative examples are alkali metal salts, in particular lithium salts, of less mobile anions of weak bases having a large anionic radius. Examples of such anions are I−, Br−, SCN−, ClO4−, BF4−, PF6−, AsF6−, etc. Specific examples of suitable lithium salts include LiN(SO2CF3)2, LiN(SO2C2F6)2, LiASF6, LiPF6, LiBF4, LiB(C6H5)4, LiCl, LiBr, LiL, CH3SO3Li, CF3SO3Li, LiClO4, LiSCN, and the like.
Electrode Active Materials
The present invention provides mixtures or blends of electrochemically active materials (herein “electrode active materials”). The term “blend” or “mixture” refers to a combination of two or more individual active materials in a physical mixture. Preferably, each individual active material in a blend retains its individual chemical composition after mixing under normal operating conditions, except such variation as may occur during substantially reversible cycling of the battery in which the material is used. Such mixtures comprise discrete regions, or particles, each comprising an active material with a given chemical composition, preferably a single active material. Preferably, the materials of this invention comprise a substantially homogeneous distribution of particles.
The positive electrode active materials of the present invention include a blend of LNCO and LNMCO materials, which unexpectedly maintain high capacity while enhancing thermal stability of the cathode-electrolyte system. In the following formulae, LNCO materials are represented by the term LNM1O where M1 is at least one of Co or Al.
In an embodiment, the blend can be written as xLNMCO(1−x)LNM1O where 0<x<1 and M1 is at least one of Co or Al;
wherein LNMCO is Li(1+y)M2(1−y)O2 where 0≦y≦0.9 and M2=MnaNibCoc where a+b+c=1 and (1+y)/(1−y)−1≦a≦1 and 0≦b/c≦100 for c not equal to 0, or b=1−a for c=0; and
wherein LNM1O is selected from the group consisting of LiNidCoeO2 where d+e=1 and 0≦d/e≦100 for e not equal to 0, or d=1 for e=0; and LiNi1−(z+z′)CozAlz′O2 where 0<z+z′<1.
In an alternative embodiment, the blend is xLNMCO(1−x)LNM1O where 0<x<1 and M1 is at least one of Co or Al;
wherein LNMCO is Li(1+y)M2(1−y)O2 where 0≦y≦0.9 and M2=MnaNibCoc where a+b+c=1 and (1+y)/(1−y)−1≦a≦1 and 0<b/c≦100; and
wherein LNM1O is selected from the group consisting of LiNidCoeO2 where d+e=1 and 0<d/e≦100; and LiNi1−(z+z′)CozAlz′O2 where 0<z+z′<1.
A preferred LNMCO is LiNi1/3Mn1/3Co1/3O2 obtained from Argonne National Laboratory (Argonne, Ill.).
A preferred LNCO compound is LiNi0.8Co0.2O2, available as “LNCO-1” from BASF Catalysts, LLC (Iselin, N.J.). Another useful LNCO is LiNi0.8Co0.016Al0.05O2, available from Toda Kogyo, Hiroshima, Japan.
The inventive active cathode blends provide a useful layered structure. Also, the inventive active cathode blends have a much lower manganese content than other known lithium mixed metal oxides.
The following examples further illustrate the invention but, of course, should not be construed as in any way limiting its scope. In the examples the following organic solvent acronyms are used: ethylene carbonate (EC), dimethyl carbonate (DMC), and diethyl carbonate (DEC).
The following four active cathode material compositions were used.
1. LiNi1/3Mn1/3Co1/3O2 100% (reference DR28)
2. LiNi1/3Mn1/3CO1/3O2 75%, LNCO-1 25% (reference DR29)
3. LiNi1/3Mn1/3CO1/3O2 25%, LNCO-1 75% (reference DR30)
4. LNCO-1 100% (reference DR31)
Reference samples DR29 and DR30 were prepared as active cathode material blends.
Exemplary cathode active slurry formulations were prepared using each reference material as shown in Table 1.
1PVDF = polyvinyldifluoride binder
2Super P = battery grade carbon black
3SAB = low surface area carbon black
4KS-15 = graphitic carbon
The positive electrode for each cathode active slurry formulation was prepared by coating the slurries on aluminum foil with an Adjustable Micron Film Applicator from Gardco (gap 12 mil), drying first in open air on an electric plate at 110° C. for 2 hours, and then in a vacuum oven at 110° C. for 40 hours. The dried materials were calendered to 104-108 μm (ref. DR28), 100-105 μm (ref. DR29), 108-110 μm (ref. DR30), and 89-95 μm (ref. DR31), respectively, of thickness that corresponded to ca, 75% of its original value. Electrodes of 0.5 inch diameter were punched and weighed, and weight loading was calculated (108-110 mg/in2). Lithium metal ½-inch coin cells were made (batch of 3 for each reference material) as follows. Separator Setela (polyethylene film, 20 μm thickness) and Ferro electrolyte: 1M LiPF6 in EC/DMC/DEC 1:1:1 (vol.) were used.
The coin cells were tested on a Maccor cycling instrument according to the following schedule within the voltage interval of 3V-4.2V: charge C/20 with taper at 4.2V to current C/200, discharge C/20, charge C/10 with taper at 4.2V to current C/100, discharge C/10, charge C/10 with taper at 4.2V to current C/100, stand for 18 hours.
The coin cells were tested to measure specific capacity (mAh/g) and cycle coulombic efficiency using the data from the cycling profiles. The results are tabulated in Table 2, where the following abbreviations apply for charge (Ch.), discharge (Dch.), and efficiency (Eff.).
As shown in Table 2, the cells prepared using active cathode material blends (DR29 cell and DR30 cell) provided excellent specific capacities and efficiencies comparable to cells having cathodes made with LNCO-1 alone (DR31 cell). It was found that for the cells prepared using active cathode material blends (DR29 cell and DR30 cell) the discharge capacities are a linear combination of the discharge capacity of each material in the blend in proportion to the weight percent employed. Thus, the overall energy output of the DR29 and DR30 cathode blend cells was found to be high, while thermal stability was improved, as shown in Example 5.
The coin cells prepared in Example 2, after the 18 hour charge stand of Example 3, were dismantled in a glove box. The charged cathodes were washed with solvent to remove electrolyte and binder, and then each cathode was mixed with electrolyte at a constant cathode/electrolyte weight ratio. These preparations were subjected to DSC using a TA Instruments calorimeter Model 2010 (New Castle, Del.).
Thus, as stated above, the overall energy output of the DR29 and DR30 cathode blend cells was found to be high, as shown in Example 4, while thermal stability was unexpectedly improved.
Further, in addition to the disclosed coin type battery, it is expected that a similar technical advantage can be obtained with any of the cylindrical or rectangular batteries.
As can be appreciated from the description of certain embodiments according to the present invention, it is possible to provide a non-aqueous electrolyte secondary battery having a high specific capacity, thus high energy density, high cycling efficiency, and good thermal stability.
All references, including publications, patent applications, and patents, cited herein are hereby incorporated by reference to the same extent as if each reference were individually and specifically indicated to be incorporated by reference and were set forth in its entirety herein.
The use of the terms “a” and “an” and “the” and similar references in the context of describing the invention (especially in the context of the following claims) are to be construed to cover both the singular and the plural, unless otherwise indicated herein or clearly contradicted by context. Recitation of ranges of values herein are merely intended to serve as a shorthand method of referring individually to each separate value falling within the range, unless otherwise indicated herein, and each separate value is incorporated into the specification as if it were individually recited herein. All methods described herein can be performed in any suitable order unless otherwise indicated herein or otherwise clearly contradicted by context. The use of any and all examples, or exemplary language (e.g., “such as”) provided herein, is intended merely to better illuminate the invention and does not pose a limitation on the scope of the invention unless otherwise claimed. No language in the specification should be construed as indicating any non-claimed element as essential to the practice of the invention.
Preferred embodiments of this invention are described herein, including the best mode known to the inventors for carrying out the invention. It should be understood that the illustrated embodiments are exemplary only, and should not be taken as limiting the scope of the invention.
| Filing Document | Filing Date | Country | Kind | 371c Date |
|---|---|---|---|---|
| PCT/US09/60462 | 10/13/2009 | WO | 00 | 6/29/2011 |
| Number | Date | Country | |
|---|---|---|---|
| 61104837 | Oct 2008 | US |
