Positive electrode materials having a superior hardness strength

Abstract

A powderous positive electrode material for a lithium secondary battery, the material having the general formula Li1+x[Ni1−a−b−cMaM′bM″c]1−xO2−z; M being either one or more elements of the group Mn, Zr and Ti, M′ being either one or more elements of the group Al, B and Co, M″ being a dopant different from M and M′, x, a, b and c being expressed in mol with −0.02≤x≤0.02, 0≤c≤0.05, 0.10≤(a+b)≤0.65 and 0≤z≤0.05; and wherein the powderous material is characterized by having a BET value ≤0.37 m2/g, a Dmax<50 μm, and a hardness strength index ΔΓ(P) of no more than 100%+(1−2a−b)×160% for P=200 MPa, wherein (Formula I) (I) with D 10p=0 being the D10 value of the unconstrained powder (P=0 M Pa), r°(D 10p=0) being the cumulative volume particle size distribution of the unconstrained powder at D 10p=0, and Γp(D 10p=0) being the cumulative volume particle size distribution at D10p=0 of the pressed samples with P being expressed in M Pa.

Description

This application is a National Stage application of International Application No. PCT/IB2015/054146, filed Jun. 1, 2015. This application also claims priority under 35 U.S.C. § 119 to European Application No. 14171694.4, filed Jun. 10, 2014.

TECHNICAL FIELD AND BACKGROUND

This invention relates to metal oxide compounds and to preparation methods thereof. More specifically, this invention relates to doped metal oxide insertion compounds for use in lithium and lithium-ion batteries.

In recent years, secondary lithium ion batteries superseded other battery systems due to their relatively high gravimetric and volumetric energy density. These features are particularly desirable to accompany the miniaturization of portable electronics (such as laptops, smartphones or cameras . . . ) and foreseen as suitable for electrical vehicles (HEV or EV) with long operational range. The latter application requires batteries able to sustain good charge-discharge cycle life under real operating conditions, namely several thousand of cycles at over an extended temperature range and high rate of discharge. The majority of rechargeable lithium ion batteries use anode materials which do not contain lithium metal, for example carbon and/or metal alloy (such as silicon alloys, tin alloys . . . ) containing materials. The cathode must then contain lithium which can be reversibly extracted during charge and inserted during discharge in order to deliver good cycle life.

Most promising materials as cathodes for rechargeable lithium ion batteries are lithium transition metal oxides with a layered structure derived from α-NaFeO₂ (space group R-3m). Since the introduction of the first Li-ion battery in 1990 by Sony into consumer electronics; LiCoO₂ is still the most commonly used cathode materials thanks to its good cycle life, very high pressed density—commonly exceeding 3.7 g/cm³—and large specific capacity of about 140 mAh/g at 4.2V against graphite anodes. LiCoO₂ is however less favored by its very high and fluctuating price and relative scarcity of cobalt, which limits its use for the emerging EV mass-market. Alternative cathode active materials such as LiNiO₂ have been investigated due to larger availability and lower price of nickel. LiNiO₂ also features a higher specific capacity when compared to LiCoO₂; typically exceeding 200 mAh/g at 4.2V, due to the lower potential of the transition metal oxide redox-couple. LiNiO₂ has two shortcomings:

• • (i) LiNiO₂ raises safety concerns because it has a sharper exothermic reaction with electrolyte at a lower temperature than LiCoO₂, as evidenced by DSC (see Dahn et al, Solid State Ionics, 69, 265 (1994)), ultimately leading to thermal runaway and catastrophic failure of the battery. Accordingly, pure LiNiO₂ is generally not selected for use in commercial lithium-ion batteries.
  • (ii) Higher specific capacity at a given cell voltage means that larger amounts of Li can be reversibly de-intercalated per unit of LiNiO₂, leading to significant changes of the crystal volume upon charge and discharge cycling. Such repeated large variations of the crystal volume can lead to cathode materials' primary and secondary particles not being able to sustain such stress. Particle fracture and loss of electrical contact may occur within the electrode and this ultimately impairs the cycle life of the Li-ion battery.

For improving the abovementioned issues, especially the ones related to safety for LiNiO₂, various doping elements have been introduced, for example electrochemically inactive ions such as Mg²⁺, Ti⁴⁺ and Al³⁺ (see for example U.S. Pat. No. 6,794,085 B2). Such a doping strategy however frequently results in a decrease of specific capacity and lower power in real cells, and is not preferred for the end application.

A more promising route is Co and Mn substitution of Ni (as disclosed in US 2003/0022063 A1) leading to a so called NMC-type composition with the idealized general formula Li_1+x[Ni_1−a−bMn_aCo_b]_1−xO₂. This idealized formula doesn't expressly take into account cation mixing, which is the ability of a metal, generally nickel in divalent state, to occupy sites in the lithium layers. It is generally admitted that Mn is tetravalent, Co trivalent and Ni bears a 2+/3+ charge. It is trivial to show that the fraction of nickel ions being effectively Ni³⁺ is:

$\frac{\left(\frac{1+x}{1-x}-2a-b\right)}{1-a-b}\mathrm{where}\frac{1+x}{1-x}$ is referred to as the lithium to metal molar ratio.

The Ni³⁺ molar content is therefore equal to:

$\left(\frac{1+x}{1-x}-2a-b\right)\times \left(1-x\right).$

When Li:M is close to 1, meaning that for x˜0 (or −0.05≤x≤0.05), the Ni³⁺ molar content approximates 1−2a−b. This last expression will be considered to calculate the effective Ni³⁺ content in the following examples with the convention that “a” represents tetravalent metal cations (examples include—but are not limited to—Mn⁴⁺, Zr⁴⁺ or Ti⁴⁺), and b represents trivalent metal cations (examples include—but are not limited to—Co³⁺ and Al³⁺). Likewise, the calculation of effective Ni³⁺ fraction can be extended to take into account divalent metal cation doping such as Mg²⁺ and Ca²⁺; one can show that the content is given by (1−2a−b)/(1−a−b−c) where c represents the molar content of divalent cations.

In these NMC materials, the specific capacity, hence the amount of Li reversibly de-intercalating from the materials, increases when the effective Ni³⁺ content increases. For example, popular compositions such as 111 (111 standing for the molar ratio of Ni:Mn:Co, with ˜0.1 mole Ni³⁺ per mole of product), 532 (˜0.2 mole Ni³⁺), 622 (˜0.4 mole Ni³⁺) and 811 (˜0.7 mole Ni³⁺) typically have a specific discharge capacity of 150, 160, 170 and 190 mAh/g, respectively, when cycled between 4.2 and 2.7V against a graphite anode.

More lithium ions are then reversibly extracted from the materials, resulting in a higher particle strain when the effective Ni³⁺ content is increased. Strain ultimately will lead to particle fracture and electrode degradation, hence accelerating the rate of capacity fading and impairing the cycle life of the cell. In addition, such particle fracture creates new exposed surfaces which will eventually accelerate side reactions on the cathode, namely electrolyte oxidation, and further reduce the cycle life of the battery. Such issues become more critical for systems requiring a higher power output: typically modern EV applications require operating C-rates superior to 1 C and even up to 5 C (1 C=1 h and 5 C=12 mins to complete full battery charging or discharging). Cathode materials must be able to accommodate strain generated by volume change of the unit cell due to insertion and extraction of Li ions in a short amount of time. Clearly, it is difficult to design materials being both able to deliver a large specific capacity (i.e. having high effective Ni³⁺) and able to accommodate larger strain, especially at higher power. It is the object of the present invention to provide such materials.

The volumetric energy density (in Wh/L) of the Li-ion battery is not only influenced by the specific discharge capacity (in mAh/g) of both the anode and cathode electrodes, but also by the gravimetric density of the electrodes (in g/cm³). On the cathode side, the electrode gravimetric density is determined by:

• • (i) the intrinsic properties of the cathode materials such as tap density (TD) or pressed density, and,
  • (ii) the electrode production process, for example during the calendaring or pressing step to increase electrode density. In such a step, an uniaxial stress is applied to the electrode in order to reach the desired level of density (or porosity) to achieve a high volumetric energy.

The present invention aims at providing a cathode material able to sustain such stress, id est a material with secondary particles that do not break under pressure during the manufacturing process and that are able to sustain repeated charge-discharge cycles without breaking.

In this respect, US 2004/023113 A1 is concerned with the determination of the compressed density and compressive strength of cathode powders; the examples being mostly about LiCoO₂. In the determination of the compressed density, the power is compressed under a pressure of 29.4 MPa. Such pressure is about 10-fold lower in comparison to the present state of the art requirements of electrode making and is not representative of the behavior of cathode materials during such process.

It is known that the particular morphology of LiCoO₂, with very dense, non-agglomerated potato-shaped particles, can sustain very high compression stress without breaking. Composite lithium nickel manganese cobalt oxides (NMC) have a very different morphology of secondary particles made of agglomeration of primary particles. Such secondary particles are more brittle due to the occurrence of inter-particle grain boundaries which are preferred fracture points. Impurities such as un-reacted alkali salts (hydroxides, carbonates, sulfates . . . ) accumulate at the grain boundaries. When the full cell is operated at potentials above 4V, these unreacted salts decompose and dissolve in the electrolyte, leaving the grain boundary opened and unfilled, which dramatically impairs the mechanical resistance of the secondary particles. Materials comprising an excessive amount of such Li-salt impurities demonstrate a lower resistance to mechanical stress resulting from electrode processing, and have an inferior tolerance to accommodate strain resulting for Li insertion and extraction when operated in a battery at high power (=at a high discharge C-rate). It is commonly accepted that the higher the effective Ni³⁺ content, the more impurities, primarily LiOH and Li₂CO₃, accumulate at the grain boundaries, further increasing the propensity of secondary particles to break.

US 2009/0314985 A1 describes the compressive strength of cathode powders and introduces the concept that the D10 value of the particle size distribution should change by no more than 1 μm after compression of the powder under 200 MPa. Such criterion fails to properly describe the behavior of materials having lower D10 values; especially when D10<1 μm. The only example describes the behavior of a D50=10 μm NMC 111 with +/−5 mol % of Ni³⁺. Because of its low effective Ni³⁺ content NMC 111 is one of the less brittle NMC materials. Materials having a larger effective Ni³⁺ content—and a larger specific capacity—while keeping relatively low secondary particle brittleness are desirable for modern applications. In addition, the manufacturing process disclosed in US 2009/0314985 A1 is not realistic for mass production: it is for example described to use oxygen gas streams and multiple step firing resulting in both high cost and low throughput. In addition, no mention is made on the cycle life improvement of cathode materials featuring an improved hardness strength.

SUMMARY

Viewed from a first aspect, the invention can provide a powderous positive electrode material for a lithium secondary battery, the material having the general formula Lii+x[Nii−a−b−cMaM′bM″_c]i−x02−; M being either one or more elements of the group Mn, Zr and Ti,

M′ being either one or more elements of the group Al, B and Co,

M″ being a dopant different from M and M′,

x, a, b and c being expressed in mol with −0.02≤x≤0.02, 0≤c≤0.05, 0.10≤(a+b)≤0.65 and 0≤z≤0.05; and wherein the powderous material is characterized by having a BET value ≤0.37 m²/g, a D_max<50 μm, and wherein the powderous material is characterized by having a hardness strength index (HSI) ΔΓ(P) value of no more than 100%+(1−2a−b)×160% for P=200 MPa, wherein

$\mathrm{\Delta \Gamma }\left(P\right)=\frac{{\Gamma }^P\left(D{10}_{P=0}\right)-{\Gamma }^0\left(D{10}_{P=0}\right)}{{\Gamma }^0\left(D{10}_{P=0}\right)}\times 100\left(\mathrm{in}\%\right)$

with D10_P=0 being the D10 value of the unconstrained powder (P=0 MPa), Γ⁰(D10_P=0) being the cumulative volume particle size distribution of the unconstrained powder at D10_P=0, and Γ^P(D10_P=0) being the cumulative volume particle size distribution at D10_P=0 of the pressed samples with P being expressed in MPa. In an embodiment, M=Mn and M′ is either one of Al and Co. In another embodiment Dmax<45 μm. From the experiments below it is clear that a value for BET of less than 0.20 m²/g is not obtained. In a more particular embodiment, 1−a−b≥0.5 and 1+x<1.000. Also, the material may comprise up to 2 mol % of W, Mo, Nb, Zr, or a rare earth element. In one embodiment, the material comprises a second phase LiN_x′O_y′ with 0<x′<1 and 0<y′<2, where N is either one or more of W, Mo, Nb, Zr and rare earth elements. Authors speculate that materials modified with proper additives or dopants can feature enhanced hardness strength and also an improved cycle life. This is for example the case of additives or dopants T such as W, Mo, Nb, Zr, or rare earth elements. Such T elements have the property to alloy with Li (for example Li₂ZrO₃, (Li₂O)_n(WO₃) with n=1, 2, 3; or Li₃NbO₄) and sometimes also with M=Co, Ni and Mn as in Li₄MWO₆ compounds. Such T-containing alloys are stable and accumulate at the grain boundary of particles; it results in a stabilization of the grain boundary offering better mechanical resistance to stress and during repeated electrochemical cycling.

The material may have a AI2O3 surface coating, resulting in an alumina content greater than 1000 ppm, or even greater than 2000 ppm. The cathode materials according to the invention may have less than 3000 pm F. In one embodiment, the material may have a S wt % content lower than 0.5 wt %, or lower than 0.25 wt %, or even lower than 0.15 wt %.

In various embodiments the following features are provided:

ΔΓ(P)≤150+(1−2a−b)×160% for P=300 MPa, or

ΔΓ(P)≤125%+(1−2a−b)×100% for P=300 MPa, or

ΔΓ(P)≤180% for P=300 MPa, or

ΔΓ(P)≤140% for P=300 MPa, or

ΔΓ(P)≤100% for P=300 MPa.

For the powderous positive electrode material according to the invention

• • they may have a BET value after wash >1 m²/g, or also greater than 1.5 m²/g,
  • they may have a pressed density greater than 3.0 g/cm³, or greater than 3.2 g/cm³, or also greater than 3.4 g/cm³.
  • they may have a soluble base content (Li₂CO₃+LiOH)<0.8 wt %, or Li₂CO₃ wt %+LiOH wt %<0.5 wt %, or also Li₂CO₃ wt %+LiOH wt %<0.3 wt %.
  • they may comprise secondary particles substantially free from porosities larger than 20 nm, or even free from porosities larger than 10 nm, as is illustrated in FIG. 9-10.
  • they may comprise secondary particles comprising less than 20 voids larger than 20 nm or even less than 10 voids larger than 20 nm, as is illustrated in FIG. 9-10.
  • they may have a FWHM value of the (104) peak as defined by the pseudo hexagonal lattice with R-3m space group which is greater than 0.125 2-theta degrees, or greater than 0.140 2-theta degrees, or even greater than 0.150 2-theta degrees.
  • they may have a FWHM value of the (015) peak as defined by the pseudo hexagonal lattice with R-3m space group which is greater than 0.125 2-theta degrees, or greater than 0.140 2-theta degrees, or even greater than 0.150 2-theta degrees.
  • they may have a FWHM value of the (113) peak as defined by the pseudo hexagonal lattice with R-3m space group which is greater than 0.16 2-theta degrees, or greater than 0.18 2-theta degrees, or even greater than 0.20 2-theta degrees.

The cathode materials according to the invention may have a 0.1 C Efad.≤(1−2a−b)×10%, or a 0.1 C Efad.≤(1−2a−b)×5%, or a 1 C Efad.≤(1−2a−b)×20% (see in the detailed description, part a) and c) for the electrochemical testing experiments). The material may cycle for at least 1000 cycles, or even at least 1500 cycles with a retained capacity above 80% at room temperature in a full cell. The material may also cycle for at least 900 cycles, or even at least 1500 cycles with a retained capacity above 80% at 45° C. in a full cell.

It is clear that further product embodiments according to the invention may be provided by combining features that are covered by the different product embodiments described before.

Viewed from a second aspect, the invention may provide a powderous positive electrode material incorporated in an electrode and having an electrode density greater than 3.0+((1−2a−b)/2) g/cm³.

Viewed from a third aspect, the invention may provide a lithium secondary battery comprising a positive electrode active material comprising particles of lithium-transition metal oxide; a Li-free negative electrode, a separator interposed between the positive electrode and the negative electrode; and a non-aqueous electrolyte, wherein the particles of the positive electrode active material have a ΔΓ(P) values which is no more than (1−2a−b)×180% for P=300 MPa, or no more than 2(1−x)(1−a−b)×140% for 300 MPa, or even less than (1−a−b)×100% at 300 MPa. In an embodiment the material has a FWHM of the (104) peak greater than 0.16 2-theta and demonstrates at least 1000 cycles, or even 1500 cycles with a retained capacity above 80% at room temperature. In an embodiment the material has a FWHM of the (104) peak greater than 0.16 2-theta and demonstrates at least 900 cycles with a retained capacity above 80% at 45° C.

Viewed from a fourth aspect, the invention may provide a method for preparing a powderous positive electrode material according to the invention, the material having the general formula Li_1+x[Ni_{1−a−b−c}M_aM′_bM″_c]_1−xO_2−z, and the method comprising the steps of:

• • providing a mixture of one or more precursor materials comprising either one or more of Ni, M, M′ and M″, and a precursor material comprising Li,
  • sintering the mixture at a temperature T expressed in ° C., with (945−(248*(1−2a−b)≤T≤(985−(248*(1−2a−b)), thereby obtaining agglomerated particles, and
  • pulverizing the agglomerated particles whereby a powder is obtained having a BET≤0.37 m²/g and a D_max<50 μm. The D_max or D100 value is the maximum particle size of the obtained powder. In an embodiment D_max<45 μm. From the experiments below it is clear that a value for BET of less than 0.20 m²/g is not obtained.

It should be mentioned here that US2011/193013 describes a powderous lithium transition metal oxide having a layered crystal structure Li_1+aM_1−aO_2±bM′_kS_m with −0.03<a<0.06, b≅0, 0≤m≤0.6, m being expressed in mol %, M being a transition metal compound, consisting of at least 95% of either one or more elements of the group Ni, Mn, Co and Ti; M′ being present on the surface of the powderous oxide, and consisting of either one or more elements of the group Ca, Sr, Y, La, Ce and Zr. The products having a BET value ≤0.37 m²/g have been fired at a too high temperature, causing an increase in porosity that leads to a decrease in hardness.

Also, US2006/233696 describes a powderous lithium transition metal oxide with the composition Li_xM_yO₂ and prepared by solid state reaction in air from a mixed transition metal precursor and Li₂CO₃, the powder being practically free of Li₂CO₃ impurity. In the formula M=M′_1−kA_k, where M′=Ni_1−a−b(Ni_1/2Mn_1/2)_aCo_b on condition of 0.65≤a+b≤0.85 and 0.1≤b≤0.4; A is a dopant; and 0≤k≤0.05; and x+y=2 on condition of 0.95≤x≤1.05. The BET surface area of the prepared products is too high, causing a decrease in hardness.

Finally, in US2010/112447 the positive electrode active material includes a composite oxide containing lithium and Ni, Mn, and Co. The molar ratio of Ni is from 0.45 to 0.65, and the molar ratio of Mn is from 0.15 to 0.35. The positive electrode active material has a pressed density under a compression of 60 MPa of 3.3 g/cm³ or more and 4.3 g/cm³ or less. The positive electrode active material has a volume resistivity under a compression of 60 MPa of 100 Ω-cm or more and less than 1000 Ω-cm. The disclosed material however have a (Ni+Mn+Co):Li ratio of _1:1.03 or more, or 1:0.95. This ratio is either too high or too low to allow to obtain products with the desired hardness.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1: evolution of the cumulative particle size distribution Γ^P as function of uni-axial stress P, for P=0, 100, 200 and 300 MPa for Example 1.

FIG. 2: enlargement of the evolution of the cumulative particle size distribution Γ^P as function of uni-axial stress P, for P=0, 100, 200 and 300 MPa for Example 1 and showing the steps to determine Γ^P(D10_P=0)

FIG. 3: full cell cycle life at room-temperature of EX1, EX2 and CEX1 when cycled between 4.2 and 2.7V. Evolution of the retained capacity (in % of the initial discharge capacity) as a function of the cycle number (#).

FIG. 4: full cell cycle life at 45° C. of EX1, EX2 and CEX1 when cycled between 4.2 and 2.7V. Evolution of the retained capacity (in % of the initial discharge capacity) as a function of the cycle number.

FIG. 5: cross-sectional SEM and SEM of secondary particles of Examples 1 (a), 2 (b) and Counter Example 1 (c).

FIG. 6: full cell cycle life at room-temperature of EX3, EX4 and CEX2 when cycled between 4.2 and 2.7V. Evolution of the retained capacity (in % of the initial discharge capacity) as a function of the cycle number (#).

FIG. 7: full cell cycle life at 45° C. of EX3, EX4 and CEX2 when cycled between 4.2 and 2.7V. Evolution of the retained capacity (in % of the initial discharge capacity) as a function of the cycle number (#).

FIG. 8: SEM of secondary particles of Example 3 (top) and Counter Example 2 (bottom).

FIG. 9: cross-sectional SEM of secondary particles of Examples 3 (top), 4 (middle) and Counter Example 2 (bottom).

FIG. 10: cross-sectional SEM and SEM of secondary particles of Examples 5 (a), 6 (b) and Counter Example 7 (c).

FIG. 11: full cell cycle life at room-temperature of EX8, EX9 and EX10 when cycled between 4.2 and 2.7V. Evolution of the retained capacity (in % of the initial discharge capacity) as a function of the cycle number (#).

FIG. 12: full cell cycle life at 45° C. of EX8, EX9 and EX10 when cycled between 4.2 and 2.7V. Evolution of the retained capacity (in % of the initial discharge capacity) as a function of the cycle number (#).

FIG. 13: SEM of secondary particles of Examples 8 (a), 9 (b) and 10 (c).

FIG. 14: XRD pattern of Example 1 showing the diffracted intensity (counts) as function of 2-theta (degrees). The positions of 003, 104, 015, 018, 110 and 113 reflections of the α-NaFeO₂ cell (space group R-3m) are indicated.

FIG. 15: example of pseudo-Voigt decomposition of 018, 110 and 113 peaks in the 63˜70 2-theta range for Example 1. The open dots are the experimental data I_obs. after KAlpha2 subtraction, the black solid line is the fitted profile I_calc. using 3 pseudo-Voigt functions and the dashed line represents the (I_obs.−I_calc.) quantity.

DETAILED DESCRIPTION

This invention provides a cathode material able to sustain a large mechanical stress during electrode making and electrochemical stress in power-demanding applications. Such cathode material has an improved cycle life at both room temperature and 45° C. in full cells. Hence, the materials according to the invention offer significant advantages such as:

• • a state of the art electrode density that facilitates the electrode production process: the cathode materials secondary particles are able to sustain high uni-axial stress during electrode manufacturing, with a substantially lower fracture and breaking risk,
  • an increase in cycle life: the cathode materials' secondary particles show substantially lower fracturing and breaking after electrode manufacturing and upon electrochemical cycling at high C-rate, and a good contact between the cathode secondary particles, the binder, the conductive agent and the current collector is preserved within the electrode, and,
  • an improved cycle life at elevated temperature. The BET increase of cathode active materials able to sustain higher stress according to the invention is minimized after electrode pressing and due to particle breaking upon cycling, and hence this is limiting the surface exposure where side reactions such as electrolyte oxidation at higher voltage are occurring.

The methods for preparing the materials according to the invention are generally known, but it is by a proper selection of parameters such as sintering temperature and Li/metal ratio in a single step cooking process—depending largely on the content of Ni³⁺ in the compounds—that the superior hardness and other characteristics may be achieved. In practice the sintering temperature of the cooking step is limited to (985−(248*(1−2a−b))° C., and the Li:M ratio (=(1+x)/(1−x)) is between 0.98 and 1.02. A minimum sintering temperature can also be established as (945−(248*(1−2a−b))° C., to ensure that the reaction between the precursors is completed. The reason for limiting the sintering temperature is to be found in the direct influence of that temperature on the internal porosity of the particles. When the Li:M ratio is below 0.98, there is a serious decrease in capacity, since the amount of Ni that is located in Li sites increases considerably. When the Li:M ratio is more than 1.02, the soluble base content increases, leading to problems like serious gas generation in full cells, as is discussed in WO2012/107313.

Also important for the process is that after sintering the agglomerated particles are softly crushed or milled to ensure a proper hardness, and, since the milling increases the BET value, softly milling means that the BET of the milled product may be limited to ≤0.37 m²/g. As crushing and milling may lead to a very high value for D_max (being the maximum particle size), whereby the capacity is seriously hampered, the milling may be controlled to lead to a D_max<50 μm.

General Description of Experiments

a) Evaluation of Electrochemical Properties in Coin Cells

Electrodes are prepared as follows: about 27.27 wt. % of active cathode material, 1.52 wt. % polyvinylidene fluoride polymer (KF polymer L #9305, Kureha America Inc.), 1.52 wt. % conductive carbon black (Super P, Erachem Comilog Inc.) and 69.70 wt. % N-methyl-2-pyrrolidone (NMP) (from Sigma-Aldrich) are intimately mixed by means of high speed homogenizers. The slurry is then spread in a thin layer (typically 100 micrometer thick) on an aluminum foil by a tape-casting method. After evaporating the NMP solvent, the cast film is processed through a roll-press using a 40 micrometer gap. Electrodes are punched from the film using a circular die cutter measuring 14 mm in diameter. The electrodes are then dried overnight at 90° C. The electrodes are subsequently weighed to determine the active material loading. Typically, the electrodes contain 90 wt. % active materials with an active materials loading weight of about 17 mg (˜11 mg/cm²). The electrodes are then put in an argon-filled glove box and assembled within a 2325-type coin cell body. The anode is a lithium foil having a thickness of 500 micrometers (origin: Hosen); the separator is a Tonen 20 MMS microporous polyethylene film. The coin cell is filled with a 1M solution of LiPF₆ dissolved in a mixture of ethylene carbonate and dimethyl carbonate in a 1:2 volume ratio (origin: Techno Semichem Co.).

Each cell is cycled at 25° C. using Toscat-3100 computer-controlled galvanostatic cycling stations (from Toyo). The coin cell testing schedule 1 used to evaluate EX1, EX2, EX3, EX4, CEX1 and CEX2 is detailed in Table 8. Coin cell schedule 2 used to evaluate EX5, EX6, EX7, EX8, EX9 and EX10 is detailed in Table 9. Both schedules use a 1C current definition of 160 mA/g and comprise 3 parts as follows:

(i) Part I is the evaluation of rate performance at 0.1 C, 0.2 C, 0.5 C, 1 C, 2 C and 3 C in the 4.3˜3.0V/Li metal window range. With the exception of the 1^st cycle where the initial charge capacity CQ1 and discharge capacity DQ1 are measured in constant current mode (CC), all subsequent cycles feature a constant current-constant voltage during the charge with an end current criterion of 0.05 C. A rest time of 30 minutes for the first cycle and 10 minutes for all subsequent cycles is allowed between each charge and discharge.

The irreversible capacity Q_irr. is expressed in % as: Q_Irr.=(CQ1−DQ1)/CQ1×100(%) CQ1

The rate performance at 0.2 C, 0.5 C, 1 C, 2 C and 3 C is expressed as the ratio between the retained discharge capacity DQn, with n=2, 3, 4, 5 and 6 for respectively nC=0.2 C, 0.5 C, 1 C, 2 C and 3 C as follows:

$\mathrm{nC}-\mathrm{rate}=\frac{\mathrm{DQn}}{\mathrm{DQ}1}\times 100\%,$ e.g. 3 C-rate (in %)=(DQ₆/DQ₁)×100.

(ii) Part II is the evaluation of cycle life at 1 C. Coin cell schedules 1 and 2 only differ in the charge cutoff voltage, being 4.5V and 4.3V/Li metal for schedules 1 and 2 respectively. The discharge capacity at 4.5V/Li metal is measured at 0.1 C at cycle 7 and 1 C at cycle 8. Capacity fadings at 0.1 C and 1 C are calculated as follows and are expressed in % per 100 cycles:

$0.1C\mathrm{QFad}.=\left(1-\frac{\mathrm{DQ}34}{\mathrm{CQ}7}\right)\times \frac{10000}{27}\mathrm{in}\%/100\mathrm{cycles},1C\mathrm{QFad}.=\left(1-\frac{\mathrm{DQ}35}{\mathrm{CQ}7}\right)\times \frac{10000}{27}\mathrm{in}\%/100\mathrm{cycles}.$

Energy fadings at 0.1 C and 1 C are calculated as follows and are expressed in % per 100 cycles. Vn is the average voltage at cycle n.

$0.1C\mathrm{EFad}.=\left(1-\frac{\mathrm{DQ}34\times \stackrel{\_}{V34}}{\mathrm{CQ}7\times \stackrel{\_}{V7}}\right)\times \frac{10000}{27}\mathrm{in}\%/100\mathrm{cycles},\text{}1C\mathrm{EFad}.=\left(1-\frac{\mathrm{DQ}35\times \stackrel{\_}{V35}}{\mathrm{CQ}7\times \stackrel{\_}{V7}}\right)\times \frac{10000}{27}\mathrm{in}\%/100\mathrm{cycles}.$

(iii) Part III is an accelerated cycle life experiment using 1 C-rate for the charge and 1 C rate for the discharge between 4.5 and 3.0V/Li metal. Capacity and energy fading are calculated as follows:

$1C/1C\mathrm{QFad}.=\left(1-\frac{\mathrm{DQ}60}{\mathrm{CQ}36}\right)\times \frac{10000}{27}\mathrm{in}\%/100\mathrm{cycles},1C/1C\mathrm{EFad}.=\left(1-\frac{\mathrm{DQ}60\times \stackrel{\_}{V60}}{\mathrm{CQ}36\times \stackrel{\_}{V36}}\right)\times \frac{10000}{27}\mathrm{in}\%/100\mathrm{cycles},$

b) Full Cell Manufacturing

650 mAh pouch-type cells are prepared as follows: the positive electrode active material powder is prepared as described above, Super-P (Super-P™ Li commercially available from Timcal), and graphite (KS-6 commercially available from Timcal) as positive electrode conductive agents and polyvinylidene fluoride (PVdF 1710 commercially available from Kureha) as a positive electrode binder are added to NMP (N-methyl-2-pyrrolidone) as a dispersion medium so that the mass ratio of the positive electrode active material powder, the positive electrode conductive agent, and the positive electrode binder is set at 92/3/1/4. Thereafter, the mixture is kneaded to prepare a positive electrode mixture slurry. The resulting positive electrode mixture slurry is then applied onto both sides of a positive electrode current collector, made of a 15 μm thick aluminum foil. The width of the applied area is 43 mm and the length is 450 mm. Typical cathode active material loading weight is 13.9 mg/cm². The electrode is then dried and calendared using a pressure of 100 Kgf. Typical electrode density is 3.2 g/cm³. In addition, an aluminum plate serving as a positive electrode current collector tab is arc-welded to an end portion of the positive electrode.

Commercially available negative electrodes are used. In short, a mixture of graphite, CMC (carboxy-methyl-cellulose-sodium) and SBR (styrene-butadiene-rubber), in a mass ratio of 96/2/2, is applied on both sides of a copper foil. A nickel plate serving as a negative electrode current collector tab is arc-welded to an end portion of the negative electrode. Typical cathode and anode discharge capacity ratio used for cell balancing is 0.75. Non-aqueous electrolyte is obtained by dissolving lithium hexafluorophosphate (LiPF₆) salt at a concentration of 1.0 mol/L in a mixed solvent of EC (ethylene carbonate) and DEC (diethyl carbonate) in a volume ratio of 1:2.

A sheet of the positive electrode, a sheet of the negative electrode, and a sheet of separator made of a 20 μm-thick microporous polymer film (Celgard® 2320 commercially available from Celgard) interposed between them are spirally wound using a winding core rod in order to obtain a spirally-wound electrode assembly. The wounded electrode assembly and the electrolyte are then put in an aluminum laminated pouch in an air-dry room with dew point of −50° C., so that a flat pouch-type lithium secondary battery is prepared. The design capacity of the secondary battery is 650 mAh when charged to 4.20 V. The non-aqueous electrolyte solution is impregnated for 8 hrs at room temperature. The battery is pre-charged at 15% of its theoretical capacity and aged 1 day, also at room temperature. The battery is then degassed using a pressure of −760 mm Hg for 30 sec, and the aluminum pouch is sealed. The battery is prepared for use as follows: the battery is charged using a current of 0.2 C (with 1 C=650 mA) in CC mode (constant current) up to 4.2V then CV mode (constant voltage) until a cut-off current of C/20 is reached, before being discharged in CC mode at 0.5 C rate down to a cut-off voltage of 2.7V.

c) Cycle Life Experiments

The lithium secondary full cell batteries are charged and discharged several times under the following conditions, both at 25° C. and 45° C., to determine their charge-discharge cycle performance:

• • Charge is performed in CC mode under 1 C rate up to 4.2V, then CV mode until C/20 is reached,
  • The cell is then set to rest for 10 min,
  • Discharge is done in CC mode at 1 C rate down to 2.7V,
  • The cell is then set to rest for 10 min,
  • The charge-discharge cycles proceed until the battery reaches 80% retained capacity. Every 100 cycles, the discharge is done at 0.2 C rate in CC mode down to 2.7 V.

The retained capacity at the n^th cycle is calculated as the ratio of the discharge capacity obtained at cycle n to cycle 1.

d) XRD

XRD patterns are recorded on a Rigaku D/MAX 2200 PC X-ray diffractometer in the 17−144 2-theta range in a 0.02 degree scan step. Scan speed is set to 1.0 degree per minute. The goniometer with theta/2 theta Bragg Brentano geometry has a radius of 185 mm. The copper target X-ray tube is operated at KV and 40 mA. The diffracted beam monochromator, based on a curved graphite crystal, is used to remove KBeta Cu radiation. The collected XRD patterns comprise KAlpha Cu radiations with typical wavelengths KAlpha₁=1.5405 Å and KAlpha₂=1.5443 Å in an IAlpha₂/IAlpha₁ intensity ratio of ½ using a conventional scintillation counter detector. The incident beam optic setup comprises a 10 mm divergent height limiting slit (DHLS), a 1-degree divergence slit (DS) and 5 degree vertical Soller slit. The diffracted beam optic setup includes a 1-degree anti-scatter slit (SS), 5 degree vertical Soller slit and 0.3 mm reception slit (RS). Crystallinity of the different materials is calculated from the full width at half maximum (FWHM) of the (003) and (104) peaks where the hkl miller indices correspond to the O3-type hexagonal lattice with R-3m space group as defined by J. J. Braconnier, C. Delmas, C. Fouassier, and P. Hagenmuller, Mat. Res. Bull. 15, 1797 (1980). FWHM is determined by further subtraction of the background contribution using the Sonnevelt-Visser's algorithm and KAlpha2 elimination as implemented in the “Integral analysis v6.0” software from Rigaku between 17 and 20 2-theta and 43 and 43.5 2-theta for (003) and (104) peaks, respectively.

The FWHMs of the 015, 018, 110 and 113 reflections have been calculated by local fitting of the experimental intensities Iobs. after KAlpha2 elimination using pseudo-Voigt functions as follows:

$I_{\mathrm{calc}.}\left(2\theta \right)=I_0+\sum _{i=1}^n{I}_i\left({\mu }_i\left(\frac{2}{\pi }\right)\left(\frac{{\mathrm{FWHM}}_i}{4{\left(2\theta -2{\theta }_{0,i}\right)}^2+{\mathrm{FWHM}}_i^2}\right)+\left(1-{\mu }_i\right)\frac{\sqrt{4\ln \left(2\right)}}{\sqrt{\pi }{\mathrm{FWHM}}_i}{e}^{\left(-\frac{4\ln \left(2\right)}{{\mathrm{FWHM}}_i^2}{\left(2\theta -2{\theta }_{0,i}\right)}^2\right)}\right)$

Where:

• • I₀ is the background level (in counts),
  • n is the number of diffracted peaks considered on the interval,
  • I_i, μ_i, 2θ_0,i and FWHM_i are respectively the height of the pseudo-Voigt distribution (in counts), Lorentzian-Gaussian mixing ratio, 2θ₀ position (in 2-theta degrees) and FWHM (in 2-theta degrees) of peak i with i=1 . . . n.

An example of such pseudo-Voigt fitting with n=3 peaks on the 63˜70 2-theta range is shown on FIG. 15. 018, 110 and 113 peaks are well fitted with square correlation coefficient R² in excess of 99.5%. The authors emphasize that FWHM determination in such conditions is a trivial operation and can be done with a large variety of academic/open/commercial software.

e) Material Hardness Evaluation

Materials hardness is estimated by means of particle size evolution under uniaxial stress as follows:

• • Cathode active material is put in a stainless-steel pellet die and a uni-axial pressure of 100, 200 and 300 MPa is applied. The obtained pellet is then gently unravelled with the finger to obtain a loose powder for laser particle size distribution measurement. The use of strong de-agglomeration methods such as agate mortar is not suitable for this step as the particles would be further broken and the fraction of fine particles would be increased.
  • The laser particle size distribution is measured using a Malvern Mastersizer 2000 with Hydro 2000MU wet dispersion accessory after dispersing the powder in an aqueous medium, sufficient ultrasonic irradiation, typically 1 minute for an ultrasonic displacement of 12, and stirring are applied and an appropriate surfactant is introduced.
  • a Hardness Strength Index (HSI) is defined as follows:

$\mathrm{\Delta \Gamma }\left(P\right)=\frac{{\Gamma }^P\left(D{10}_{P=0}\right)-{\Gamma }^0\left(D{10}_{P=0}\right)}{{\Gamma }^0\left(D{10}_{P=0}\right)}\times 100\left(\mathrm{in}\%\right)$

where:

• • D10_P=0 is the D10 value of the unconstrained powder (P=0 MPa), −r°(D10_P=0) is the cumulative volume particle size distribution of the unconstrained powder at D10_P=0. Note that by definition r°(D10_P=0) always equals 10%.
  • r^p(D10_P=0) is the cumulative volume particle size distribution of the pressed samples with P=100, 200 and 300 MPa at D10_P=0. This value can be determined by direct reading on the plot or by local approximation using fitting functions.

An increase in the r^p(D10p=o) value after the uni-axial compression stress is direct evidence that particles have been broken into smaller particles. ΔΓ(P) is the relative increase of r^p(D10p=o) compared to r°(D10p=0) and is expressed in %. The change in the r^p(D10p=o) and ΔΓ(P) are therefore quantitative measures for determining the HSI of cathode powders according to the invention. Such evolution of the cumulative particle size as function of uniaxial stress is shown on FIG. 1, and more explicitly on FIG. 2 for Example 1 (see also below). In one embodiment, the powderous lithium mixed metal oxides according to the invention have a ΔΓ(P) value which increases by no more than 100%+(1−2a−b)×160% under 200 MPa, in another embodiment 150%+1−2a−b)×160% under 300 MPa and in still another embodiment 125%+(1−2a−b)×100% under 300 MPa; where a and b are the molar contents of Mn and Co resp. in the cathode compound Li_1+x[Ni_{1−a−b−c}M_aM′_bM″_c]_1−xO_2−z.

f) Pressed Density

The pressed density is measured as follows: 3 grams of powder is filled into a pellet die with a diameter “d” of 1.300 cm. A uniaxial load of 2.8 tons, corresponding to a pressure of 207 MPa, is applied for 30 seconds. After relaxing the load, the thickness “t” of the pressed powder is measured. The pellet density is then calculated as follows:3/(π×(d/2)²×t) in g/cm³.

Also, the density of the powder under 300 MPa load is measured and gives information about the pressed density increase due to secondary particles breaking into smaller particles. In particular, smaller particles increase the apparent density by filling the voids of the secondary particles packing. The more the secondary particles break and create fines, the higher the density. This property is listed as density at 300 MPa in the tables and is calculated as follows: 3/(π×(d/2)²×t) in g/cm³; where “d” is the diameter of the die (equal to 1.3 cm) and “t” is the thickness of the pellet under 300 MPa load.

g) BET Specific Surface Area

The specific surface area is measured with the Brunauer-Emmett-Teller (BET) method using a Micromeritics Tristar 3000. 3 g of powder sample is vacuum dried at 300° C. for 1 h prior to the measurement in order to remove adsorbed species. The “true” BET is measured as follows: 10 g of powder sample is immerged in 100 g water and stirred for 10 mins at room temperature. The aqueous solution is then removed using Buchner filtration with suction. The washed powder is collected and dried at 120° C. for 3 h. The true BET is then measured on the washed powder using the same experimental conditions as ditto. The true BET is believed to be representative of the BET seen in the full cell once all Li-salts, such as LiOH, Li₂CO₃, Li₂SO₄, . . . have dissolved in the electrolyte at potentials higher than 4V. In this case, precious qualitative information is given on the microporosity of the particles; it is for example expected that the smaller the pores, the higher the true BET.

h) Residual Li₂CO₃ and LiOH Titration

The base content is a material surface property that can be quantitatively measured by the analysis of reaction products between the surface and water. If powder is immersed into water a surface reaction occurs. During the reaction the pH of the water increases (as basic compounds dissolve) and the base is quantified by a pH titration. The result of the titration is the “soluble base content” (SBC). The content of soluble base can be measured as follows: 100 ml of de-ionized water is added to 20 g of cathode powder when Ni³⁺ content <0.4 and 4 g of cathode powder when Ni³⁺ content ≥0.4, followed by stirring for 10 minutes. The aqueous solution is then removed by using Buchner filtration with suction, thereby achieving >90 g of clear solution which contains the soluble base. The content of soluble base is titrated by logging the pH profile during addition of 0.1 M HCl at a rate of 0.5 ml/min until the pH reaches 3 under stirring. A reference voltage profile is obtained by titrating suitable mixtures of LiOH and Li₂CO₃ dissolved in low concentration in DI water. In almost all cases two distinct plateaus are observed. The upper plateau with endpoint γ1 (in mL) between pH 8˜9 is OH⁻/H₂O followed by CO₃²⁻/HCO³⁻, the lower plateau with endpoint γ2 (in mL) between pH 4˜6 is HCO³⁻/H₂CO₃. The inflection point between the first and second plateau γ1 as well as the inflection point after the second plateau γ2 are obtained from the corresponding minima of the derivative dpH/dVol of the pH profile. The second inflection point generally is near to pH 4.7. Results are then expressed in LiOH and Li₂CO₃ weight percent as follows:

${\mathrm{Li}}_2{\mathrm{CO}}_3\mathrm{wt}\%=\frac{73.8909}{1000}\times \left({\gamma }_2-{\gamma }_1\right);$ $\mathrm{LiOH}\mathrm{wt}\%=\frac{23.9483}{1000}\times \left(2\times {\gamma }_2-{\gamma }_1\right).$

i) ICP for Sulfur Titration

Sulfur content is measured using inductively coupled plasma atomic emission spectroscopy (ICP-OES) using an Agilent 720 series equipment. The analytic results are expressed in weight percent.

The invention is further illustrated in the following examples:

Example 1

The powderous cathode material of Example 1 (EX 1) is prepared by using a conventional high temperature sintering. Li₂CO₃ (Chemetall) and a Umicore mass-produced metal oxy-hydroxide precursor with Ni/Mn/Co molar ratio of 5/3/2 are mixed in a Li:M molar ratio of 1.01, resulting in the general composition of Li_1.005Ni_0.498Mn_0.299Co_0.199O₂ or Li_1.005[Ni_0.5Mn_0.3Co_0.2]_0.995O₂. The mixture is reacted at a temperature of 910° C. for 10 hours using pilot-scale equipment. The sintered cake is then crushed and classified so as to obtain a non-agglomerated powder with a mean particle size D50 of 9.9 μm. Electrochemical and physical properties are shown on Tables 1 to 7.

Example 2

The powderous cathode material of Example 2 (EX 2) is prepared by using a conventional high temperature sintering. Li₂CO₃ (Chemetall) and a Umicore mass-produced metal oxy-hydroxide precursor with Ni/Mn/Co molar ratio of 5/3/2 are mixed in a Li:M molar ratio of 1.01, resulting in the general composition of Li_1.005[Ni_0.5Mn_0.3Co_0.2]_0.995O₂. The mixture is reacted at a temperature of 930° C. for 10 hours using pilot-scale equipment. The sintered cake is then crushed and classified so as to obtain a non-agglomerated powder with a mean particle size D50 of 10 μm.

Electrochemical and physical properties are shown on Tables 1 to 7.

Counter Example 1

The powderous cathode material of Counter Example 1 (CEX 1) is prepared by using a conventional high temperature sintering. Li₂CO₃ (Chemetall) and a Umicore mass-produced metal oxy-hydroxide precursor with Ni/Mn/Co molar ratio of 5/3/2 are mixed in a Li:M molar ratio of 1.01, resulting in the general composition of Li_1.005[Ni_0.5Mn_0.3Co_0.2]_0.995O₂. The mixture is reacted at a temperature of 950° C. for 10 hours using pilot-scale equipment. The sintered cake is then crushed and classified so as to obtain a non-agglomerated powder with a mean particle size D50 of 10 μm.

Electrochemical and physical properties are shown on Tables 1 to 7.

Example 3

The powderous cathode material of Example 3 (EX 3) is prepared by using a conventional high temperature sintering. LiOH.H₂O (SQM) and a Umicore mass-produced metal oxy-hydroxide precursor with Ni/Mn/Co molar ratio of 6/2/2 are mixed in a Li:M molar ratio of 1.01, resulting in the general composition of Li_1.005Ni_0.597Mn_0.199Co_0.199O₂ or Li_1.005[Ni_0.6Mn_0.2Co_0.2]_0.995O₂. The mixture is reacted at a temperature of 860° C. for 10 hours using pilot-scale equipment. The sintered cake is then crushed and classified so as to obtain a non-agglomerated powder with a mean particle size D50 of 11.6 μm. Electrochemical and physical properties are shown on Tables 1 to 7.

Example 4

The powderous cathode material of Example 4 (EX 4) is prepared by using a conventional high temperature sintering. Li₂CO₃ (Chemetall) and a Umicore mass-produced metal oxy-hydroxide precursor with Ni/Mn/Co molar ratio of 6/2/2 are mixed in a Li:M molar ratio of 1.01, resulting in the general composition of Li_1.005[Ni_0.6Mn_0.2Co_0.2]_0.995O₂. The mixture is reacted at a temperature of 870° C. for 10 hours using pilot-scale equipment. The sintered cake is then crushed and classified so as to obtain a non-agglomerated powder with a mean particle size D50 of 12.8 μm.

Electrochemical and physical properties are shown on Tables 1 to 7.

Counter Example 2

The powderous cathode material of Counter Example 2 (CEX 2) is prepared by using a conventional high temperature sintering. Li₂CO₃ (Chemetall) and a Umicore mass-produced metal oxy-hydroxide precursor with Ni/Mn/Co molar ratio of 6/2/2 are mixed in a Li:M molar ratio of 1.01, resulting in the general composition of Li_1.005[Ni_0.6Mn_0.2Co_0.2]_0.995O₂. The mixture is reacted at a temperature of 890° C. for 10 hours using pilot-scale equipment. The sintered cake is then crushed and classified so as to obtain a non-agglomerated powder with a mean particle size D50 of 12.8 μm.

Electrochemical and physical properties are shown on Tables 1 to 7.

Examples 5, 6 and 7

These examples will demonstrate that the particle brittleness and cycle life can be affected by modifying the Li:M composition. The powderous cathode material of Example 5, 6 and 7 (EX 5, 6 and 7) is prepared by using a conventional high temperature sintering. A1203 powder, LiOH.H₂O (SQM) and a Umicore mass-produced Ni, Co oxy-hydroxide precursor with a Ni/Co molar ratio of 84.2/15.8 are mixed in order to achieve a Ni/Co/Al molar ratio of 81.7/15.3/3.0 and Li:M equal to 0.98, 1.00 and 1.02 for EX5, EX6 and EX7, respectively. Heat treatment is conducted at a temperature of 775° C. for 10 hours under O₂ flow (4 m³/Kg) using laboratory-scale equipment. The sintered cakes are then crushed and classified so as to obtain non-agglomerated powders with a mean particle size D50 of approximately 12 to 13 μm. Electrochemical and physical properties are shown on Tables 1 to 7. Cross-sectional SEM and particle SEM are shown on FIG. 8.

Examples 8, 9 and 10

These examples will demonstrate that the particle brittleness and cycle life can be affected by modifying the Li:M composition and dopant concentration. The powderous cathode material of Example 8, 9 and 10 (EX 8, 9 and 10) is prepared by using a conventional high temperature sintering. A1203 powder, LiOH.H₂O (SQM) and an Umicore mass-produced Ni—Co oxy-hydroxide precursor with a Ni/Co molar ratio of 84.2/15.8 are mixed in order to achieve a Ni/Co/Al molar ratio of 81.7/15.3/3.0 and Li:M equal to 0.98 and 1.00 for respectively EX8 and EX9 and a Ni/Co/Al molar ratio of 82.8/15.5/1.7 and Li:M equal to 1.00 for EX10. Heat treatment is conducted at a temperature of 775° C. for 10 hours under 02 flow (4 m³/Kg) using pilot-scale equipment. The sintered cakes are then crushed and classified so as to obtain non-agglomerated powders with a mean particle size D50 of approximately 12 to 13 μm. Electrochemical and physical properties are shown on Tables 17. Room temperature and 45° C. full cell performances are shown on FIGS. 11 and 12, respectively. Particle SEM's are shown on FIG. 13.

Examples 11, 12, 13, 14 and 15

200 g of cathode materials is prepared by mixing Li₂CO₃ (Chemetall) and a Umicore mass-produced metal oxy-hydroxide precursor with Ni/Mn/Co molar ratio of 5/3/2 in a Li:M molar ratio of 1.01 and reacting the mixture at 910° C. for 10 hours using muffle furnace. The general composition is Li_1.010Ni_0.495Mn_0.297Co_0.198O₂ or Li_1.010[Ni_0.5Mn_0.3Co_0.2]_0.990O₂.

The sintered cake is then crushed and 20 g of crushed product is sieved using 270 mesh size sieve (53 μm opening) resulting in Example 11 (EX11). The Dmax=D100 is 799.5 μm and the oversize fraction; determined as the weight fraction of materials not going through the sieve is 60.7%. The BET is 0.250 m²/g.

20 g of crushed product is grounded using a Cremania CG-01 150 W mill for 15 seconds resulting in Example 12 (EX12). The Dmax is 38.7 μm and the oversize fraction; determined as the weight fraction of materials not going through the sieve is 9.0%. The BET is 0.299 m²/g.

20 g of crushed product is grounded using a Cremania CG-01 150 W mill for 30 seconds resulting in Example 13 (RX13). The Dmax is 38.2 μm and the oversize fraction; determined as the weight fraction of materials not going through the sieve is 6.2%. The BET is 0.294 m²/g.

20 g of crushed product is grounded using a Cremania CG-01 150W mill for 30 seconds resulting in Example 13 (EX13). The Dmax is 38.2 μm and the oversize fraction; determined as the weight fraction of materials not going through the sieve is 6.2%. The BET is 0.294 m²/g.

20 g of crushed product is grounded using a Cremania CG-01 150 W mill for 300 seconds resulting in Example 15 (EX15). The Dmax is 32.0 μm and the oversize fraction; determined as the weight fraction of materials not going through the sieve is 0.0%. The BET is 0.821 m²/g.

The physical properties of EX11 to EX15 are shown on Table 10. The crushed product EX11 has the lowest BET and the largest oversize fraction and largest Dmax value due to agglomerated particles. EX11 has the problem of offering low production throughput because of the large oversize fraction and poor ability to make homogeneous electrodes because of large size agglomerates. EX11 is therefore unsuitable for application as lithium battery cathode materials and appropriate de-agglomeration is required.

EX12 to EX15 are prepared by increasing the milling time from 15 to 300 seconds with the result that the oversize fraction and Dmax continuously decrease and the BET continuously increases. A decrease in oversize fraction is a positive effect as the production throughput is increased. The BET increase is however not desirable because the rate of parasite reactions with electrolyte increases. In particular, the authors expect that the side reaction in EX15 will proceed about 2.4 times faster than in EX14 because of the BET surface increase. Therefore, only a special selection of milling conditions allow to control the Dmax, BET and oversize fraction within the embodiments of the present invention.

Discussion:

EX1, EX2 and CEX1

EX1, EX2 and CEX1 are in particular characterized by having different ΔΓ(P=300 MPa) values increasing from 83.7% for EX1, 116.4% for EX2 to 266.4% for CEX1 (data in Table 3 that are derived from FIGS. 1 and 2 in the case of EX1, for EX2 and CEX1 similar figures are obtained). This evolution of ΔΓ(P) indicates that more particles are broken into smaller particles when applying a uniaxial stress of 200 MPa and 300 MPa in CEX1 compared to EX1 and EX2.

Coin cell cycle life shows (in Table 1) that both the capacity fading and energy fading at 4.5V are increasing from EX1, EX2 to CEX1. In particular, the improvement in cycle stability is more noticeable at higher charge/discharge 1 C and 1 C/1 C rates.

Full cell batteries using EX1, EX2 and CEX1 are fabricated as described in the general description of experiments. Electrode densities of about 3.20 g/cm³ are achieved for EX1, EX2 and CEX1, which is very close to the density value of the powders when pressed under 208 MPa. Evolutions of the retained capacity as function of cycle number are shown on FIG. 3 at room temperature, and, on FIG. 4 at 45° C. (for each the top dotted line is for Ex1, the middle is for EX 2 and the bottom line is for CEX1). EX1 shows the best retention capacity with a retained capacity superior to 80% after 2000 cycles at room temperature and a retained capacity superior to 80% after 816 cycles at 45° C. (Table 5). Such a high retention capacity is particularly well-suited in the case of applications where long cycle life is required, such as electrical vehicles or grid storage. Comparatively, CEX1 demonstrates poor full cell cycling performances.

Conclusion: the decrease of ΔΓ(P) at P=200 and 300 MPa fits very well with the decrease in coin cell fading at 4.5V and improvements of full cell retention capacity upon cycling at both room temperature and 45° C.

Careful observation of SEM images (FIG. 5) shows that:

• • (i) The size of the primary particles is more developed in the case of CEX1 (FIG. 5c) compared to EX1 (FIG. 5a). This is consistent with the increase in the FWHM of the 003, 104, 015, 018, 110 and 118 which is attributed the smaller size of coherent domains hence smaller size of primary particles (Table 7 & FIG. 14-15).
  • (ii) The density of nanometric voids and pores, typically 10˜100 nm in size, is higher inside particles of CEX1 compared to EX1 and EX2. EX1, EX2 and CEX1 have similar BET values near 0.30 m²/g (Table 4). Their true BET are however very different and substantially higher for EX1 and EX2 by about 0.50 m²/g compared to CEX1. Presence of nanometric pores is then also expected in EX1 and EX2 but with a much smaller characteristic size than in CEX1 materials.

It is the author's opinion that the larger crystallinity and the presence of internal porosity and voids with large concentration and large characteristic size, typically exceeding 10 nm in size, are factors enhancing particle fracture and therefore making the particles less resistant to uni-axial stress and more brittle upon electrochemical cycling for CEX1 compared to EX1 and EX2. It is shown in the present invention that internal porosity of the particle can be controlled by process conditions and in this case by lowering the sintering temperature. As shown later in other examples, other suitable parameters include different Li:M ratio and different impurity content such as lithium salt based species that affect the stability of grain boundaries and therefore increase brittleness. For example, excessive amounts of LiOH, Li₂CO₃ and Li₂SO₄ lead to accumulation of these species at the grain boundaries, destabilization of the grain boundary and eventually increased brittleness. In conclusion, EX1 and EX2 are embodiments of the present invention; CEX1 is a counter example.

EX3, EX4 and CEX2

Likewise, EX3, EX4 and CEX2 follow the same relationship between cycle stability and particle brittleness as EX1, EX2 and CEX1: the lower the ΔΓ(P), the better the coin cell and full cell cycle life. In particular, EX3 is superior over 1400 cycles and over 1000 cycles at room temperature and 45° C., respectively (FIG. 6-7). The same inclusion of voids and grain boundary cracks within the particles are observed when the heat treatment temperature increases (FIG. 8-9). EX3, EX4 and CEX2 however differentiate from EX1, EX2 and CEX1 in the larger amount of effective Ni³⁺, being 0.2 in EX1, EX2 and CEX1 and 0.4 in EX3, EX4 and CEX2. This higher Ni³⁺ content results in about 10 mAh/g higher CQ1 and DQ1 values compared to EX1, EX2 and CEX1. Residual LiOH and Li₂CO₃ contents are also much increased. In particular, EX1 and EX3 have similar crystallinity as shown by the XRD FWHMs values but particles of EX3 have a propensity to break more than EX1. As a result, coin cell and full cell electrochemical properties of EX3 are inferior to EX1 especially at room temperature. The better cycle life at 45° C. of EX3 compared to EX1 might be explained by different surface chemistry regarding electrolyte oxidation due to the different Ni/Mn/Co composition and is not well understood by the authors; though the improvements over EX4 and CEX2 are believed to be in relation with lower brittleness.

EX5, EX6 and EX7

EX5, EX6 and EX7 differ in their increasing Li:M ratio and as a result differ in many properties. Strictly and as explained in the introduction, the effective Ni³⁺ content increases with Li:M but in the present case the Ni³⁺ content will be considered constant and equal to 0.817. Coin cell evaluation shown that DQ1 increases constantly with Li:M ratio but in the meantime both 0.1 C and 1 C Qfad and Efad are degrading. Note that the 1 C/1 C cycle life at 4.5V does not allow to discriminate products; the depth of charge and discharge, meaning the amount of Li reversibly extracted from the cathode materials being too high, which levels out differences. Residual LiOH and Li₂CO₃ contents are also increasing with Li:M. Cross-sectional SEM (FIG. 10) shown that the density and the size of voids within the particles increases with Li:M. XRD FWHM values (Table 7) are also increasing with decreasing Li:M, meaning that crystallinity is decreasing with Li:M.

ΔΓ(P) hardness properties (Table 3) show a more complex behavior: as expected from SEM and XRD, EX5 has the lowest ΔΓ(P) and the best coin cell properties. EX6 and EX7 have larger ΔΓ(P) values than EX5, though being identical. A careful examination of the particle size distribution of EX7 reveals that the <3 μm volume fraction is circa 2% and higher than EX5 and EX6. In fact though all the samples have close D50 between 10˜14 μm, EX7 is the only example of this study to feature such high value of <3 μm fraction. The authors believe that these fine particles are created during the post-treatment step of the powder and are evidence of a more brittle character of EX7 over EX6. As a conclusion, the increasing residual base content and the increasing crystallinity with Li:M are resulting in larger particle brittleness for EX5, EX6 and EX7.

EX8, EX9 and EX10

EX8 and EX9 were an attempt to reproduce EX5 and EX6 at pilot scale, respectively, in order to measure full cell properties. Although there exists a systematic offset in properties between EX8 and EX5 and EX9 and EX6, the differences between EX8 and EX9 are in line with the one reported for EX5 and EX6. EX8 shows significant improvements of 0.1 C and 1 C Qfad and Efad coin cell fading compared to EX9 and there again align well with the decrease of ΔΓ(P). Full cell cycle life is similar at room temperature but improved at 45° C. by about 10% more cycles demonstrated for EX8. See FIG. 11-12. Cross-sectional SEM is shown on FIG. 13.

EX10 has a lower Al and Co content compared to EX9 resulting in a higher Ni³⁺ content. The ΔΓ(P) of EX10 is strongly increased over EX9 and the 0.1 C and 1 C Qfad and Efad coin cell and the full cell room temperature and 45° C. cycle stabilities are lowered.

TABLE 1
coin cell evaluation using schedule 1 (4.3-4.5-4.5 V/Li metal).
	Capacity and rate at 4.3 V	Capacity and fading rate at 4.5 V (per 100 cycles)
	Rate (per 0.1 C)	QD7	QD8
	QC1	QD1	Qirr	1 C	2 C	3 C	0.1 C	1 C	Capacity fading (%)	Energy fading (%)
Sample	mAh/g	mAh/g	%	(%)	(%)	(%)	mAh/g	mAh/g	0.1 C	1 C	1 C/1 C	0.1 C	1 C	1 C/1 C
Ex1	190.4	166.5	12.5	91.5	87.5	84.7	192.5	177.1	−2.4	1.1	18.1	−0.9	4.5	24.2
Ex2	191.3	170.6	10.8	92.0	88.4	86.0	195.2	180.9	1.0	5.2	20.1	2.3	9.2	26.6
CEX1	193.5	170.4	11.9	91.7	88.0	85.6	195.2	180.0	4.8	9.5	24.1	6.3	13.9	31.3
EX3	198.6	179.6	9.6	91.4	88.0	85.8	201.1	185.0	−0.5	2.8	14.5	0.5	5.0	18.7
EX4	200.9	178.2	11.3	92.5	89.5	87.4	199.9	185.1	4.5	9.1	20.2	5.5	11.7	25.1
CEX2	200.0	178.2	10.9	92.0	88.9	86.8	200.4	185.6	3.9	9.8	21.4	5.1	12.8	26.7

TABLE 2
coin cell evaluation using schedule 2 (4.3-4.3-4.5 V/Li metal).
	Capacity and rate at 4.3 V	Capacity and fading rate at 4.3 V and 4.5 V (per 100 cycles)
	Rate (per 0.1 C)	Capacity fading (%)	Energy fading (%)
	QC1	QD1	Qirr	1 C	2 C	3 C			1 C/1 C			1 C/1 C
Sample	mAh/g	mAh/g	%	(%)	(%)	(%)	0.1 C	1 C	(4.5 V)	0.1 C	1 C	(4.5 V)
EX5	221.1	188.1	14.9	92.5	89.4	86.8	2.6	7.6	22.3	3.6	9.0	27.7
EX6	221.3	194.7	12.0	91.7	88.9	87.4	6.3	8.8	23.6	6.5	9.4	28.6
EX7	221.3	195.8	11.5	92.7	89.9	88.5	9.8	12.9	23.4	10.0	13.7	27.7
EX8	220.7	190.1	13.9	91.7	88.4	85.6	−3.6	2.0	21.4	−2.5	3.2	26.7
EX9	222.5	194.7	12.5	80.2	89.6	87.6	0.7	5.9	17.8	1.5	6.8	22.4
EX10	223.1	201.4	9.7	91.0	88.4	86.9	11.8	12.2	21.3	11.6	12.7	26.2

TABLE 3
brittleness properties.
	Li:M			Ni3+	ΔΓ(P)	ΔΓ(P)
	(1 + x)/			1-2a-b	P = 200 MPa	P = 300 MPa	(1)	(2)	(3)
Sample	(1 − x)	a	b	(mol %)	(%)	(%)	(%)	(%)	(%)
EX1	1.010	0.3	0.2	0.200	56.4	83.7	132	182	145
EX2	1.010	0.3	0.2	0.200	83.8	116.4	132	182	145
CEX1	1.010	0.3	0.2	0.200	223.4	266.4	132	182	145
EX3	1.010	0.2	0.2	0.400	78.5	112.9	164	214	165
EX4	1.010	0.2	0.2	0.400	122.8	184.2	164	214	165
CEX2	1.010	0.2	0.2	0.400	218.6	242.8	164	214	165
EX5	0.980	0	0.183	0.817	68.4	97.4	230.72	280.72	206.7
EX6	1.000	0	0.183	0.817	98.0	137.0	230.72	280.72	206.7
EX7	1.020	0	0.183	0.817	91.2	135.5	230.72	280.72	206.7
EX8	0.985	0	0.183	0.817	77.9	109.4	230.72	280.72	206.7
EX9	1.000	0	0.183	0.817	130.3	168.2	230.72	280.72	206.7
EX10	1.000	0	0.172	0.828	174.0	219.3	232.48	282.48	207.8
(1) 100% + (1-2a-b) × 160% for P = 200 MPa
(2) 150% + (1-2a-b) × 160% for P = 300 MPa
(3) 125% + (1-2a-b) × 100% for P = 300 Mpa

TABLE 4
physical properties.
					True	Pressed	Electrode	Density at
	LiOH	Li2CO3	S	BET	BET	density	density	300 MPa
Sample	wt %	wt %	wt %	(m2/g)	(m2/g)	(g/cm3)	(g/cm3)	(g/cm3)
EX1	0.12	0.06	0.1149	0.30	1.29	3.21	3.19	3.35
EX2	0.12	0.09	0.1129	0.37	1.49	—	3.21	3.44
CEX1	0.08	0.06	0.1123	0.28	0.93	3.28	3.19	3.61
EX3	0.33	0.16	0.1188	0.25	—	3.28	3.36	3.45
EX4	0.20	0.17	0.1179	0.32	—	3.40	3.30	3.50
CEX2	0.22	0.17	0.1497	—	—	3.25	3.28	3.57
EX5	0.38	0.21	0.0517	0.28	2.15	—	—	3.50
EX6	0.46	0.30	0.0499	0.30	2.21	—	—	3.58
EX7	0.52	0.44	0.0491	0.34	2.51	—	—	3.56
EX8	0.35	0.24	0.0508	0.24	1.76	3.40	3.41	3.49
EX9	0.37	0.24	0.0497	0.23	1.93	3.40	3.47	3.50
EX10	0.25	0.20	0.0503	0.28	—	3.46	3.51	3.84

TABLE 5
number of cycles to reach 80% retained capacity
in full cell at room temperature and 45° C.
	Sample	RT cycle number	45° C. cycle number
	EX1	>2000	816
	EX2	1075	735
	CEX1	938	614
	EX3	1450	>1000
	EX4	1230	567
	CEX2	1139	567
	EX5	—	—
	EX6	—	—
	EX7	—	—
	EX8	1658	453
	EX9	1681	409
	EX10	1024	329

TABLE 6
Particle size distribution.
	Volume	Volume
	fraction <1	fraction <3	D10	D50	D90	D99	D100
Sample	μm (%)	μm (%)	(μm)	(μm)	(μm)	(μm)	(μm)
EX1	0.0	0.0	5.6	9.9	17.4	24.6	32.3
EX2	0.0	0.0	5.6	10.0	17.6	25.2	33.3
CEX1	0.0	0.0	7.1	12.4	21.5	30.3	38.2
EX3	0.0	0.0	6.4	11.7	20.6	29.2	38.5
EX4	0.0	0.0	7.3	12.8	21.9	30.6	38.1
CEX2	0.0	0.0	8.1	14.4	24.9	34.8	45.1
EX5	0.0	0.0	6.9	12.4	22.0	31.4	38.7
EX6	0.0	0.0	7.2	13.0	22.9	32.8	42.7
EX7	0.6	2.0	6.9	12.8	22.6	32.2	38.8
EX8	0.0	0.0	7.1	12.9	22.7	32.4	39.6
EX9	0.0	0.0	7.6	13.2	22.9	32.4	39.7
EX10	0.0	0.0	7.7	13.6	23.7	33.4	42.7

TABLE 7
FWHM and 2-theta position of 003, 104, 015, 018, 110 and 113 peaks. Units are 2-theta degrees.
	2θ	FWHM	2θ	FWHM	2θ	FWHM	2θ	FWHM	2θ	FWHM	2θ	FWHM
Sample	003	003	104	104	015	015	018	018	110	110	113	113
EX1	18.63	0.146	44.38	0.175	48.53	0.173	64.26	0.209	64.89	0.183	68.18	0.206
EX2	18.65	0.140	44.40	0.165	48.55	0.162	64.28	0.206	64.92	0.174	68.21	0.196
CEX1	18.65	0.134	44.39	0.148	48.55	0.141	64.28	0.178	64.90	0.161	68.19	0.171
EX3	18.69	0.192	44.45	0.180	48.62	0.171	64.39	0.212	64.98	0.198	68.28	0.217
EX4	18.67	0.140	44.44	0.163	48.61	0.154	64.38	0.196	64.98	0.174	68.27	0.190
CEX2	18.68	0.136	44.44	0.155	48.61	0.150	64.38	0.191	64.97	0.170	68.26	0.186
EX5	18.72	0.140	44.49	0.158	48.67	0.142	64.51	0.190	64.99	0.186	68.30	0.188
EX6	18.73	0.136	44.50	0.149	48.69	0.137	64.53	0.164	65.00	0.165	68.32	0.175
EX7	18.73	0.136	44.51	0.144	48.69	0.132	64.54	0.155	65.02	0.156	68.34	0.162
EX8	18.71	0.141	44.49	0.160	48.67	0.150	64.50	0.191	65.00	0.189	68.31	0.195
EX9	18.73	0.138	44.51	0.156	48.69	0.146	64.53	0.181	65.03	0.174	68.34	0.184
EX10	18.71	0.131	44.47	0.154	48.66	0.143	64.50	0.179	64.96	0.170	68.28	0.172

TABLE 8
coin cell schedule 1 used to evaluate EX1, EX2, EX3,
EX4, CEX1 and CEX2. 1 C definition is 160 mA/g.
	Cycle	Charge	Discharge
	number		End	Rest	V/Li metal		End	Rest	V/Li metal
Type	“n”	C Rate	Current	(min)	(V)	C Rate	Current	(min)	(V)
Part I:	1	0.10	—	30	4.3	0.10	—	30	3.0
Rate	2	0.25	0.05 C	10	4.3	0.20	—	10	3.0
performance	3	0.25	0.05 C	10	4.3	0.50	—	10	3.0
	4	0.25	0.05 C	10	4.3	1.00	—	10	3.0
	5	0.25	0.05 C	10	4.3	2.00	—	10	3.0
	6	0.25	0.05 C	10	4.3	3.00	—	10	3.0
Part II:	7	0.25	0.1 C	10	4.5	0.10	—	10	3.0
1 C cycle life	8	0.25	0.1 C	10	4.5	1.00	—	10	3.0
	9~33	0.50	0.1 C	10	4.5	1.00	—	10	3.0
	34	0.25	0.1 C	10	4.5	0.10	—	10	3.0
	35	0.25	0.1 C	10	4.5	1.00	—	10	3.0
Part III:	36~60	1.00	—	10	4.5	1.00	—	10	3.0
1 C/1 C cycle
life

TABLE 9
coin cell schedule 2 used to evaluate EX5, EX6, EX7,
EX8, EX9 and EX10. 1 C definition is 160 mA/g.
	Cycle	Charge	Discharge
	number		End	Rest	V/Li metal		End	Rest	V/Li metal
Type	“n”	C Rate	Current	(min)	(V)	C Rate	Current	(min)	(V)
Part I:	1	0.10	—	30	4.3	0.10	—	30	3.0
Rate	2	0.25	0.05 C	10	4.3	0.20	—	10	3.0
performance	3	0.25	0.05 C	10	4.3	0.50	—	10	3.0
	4	0.25	0.05 C	10	4.3	1.00	—	10	3.0
	5	0.25	0.05 C	10	4.3	2.00	—	10	3.0
	6	0.25	0.05 C	10	4.3	3.00	—	10	3.0
Part II:	7	0.25	0.1 C	10	4.3	0.10	—	10	3.0
1 C cycle life	8	0.25	0.1 C	10	4.3	1.00	—	10	3.0
	9~33	0.50	0.1 C	10	4.3	1.00	—	10	3.0
	34	0.25	0.1 C	10	4.3	0.10	—	10	3.0
	35	0.25	0.1 C	10	4.3	1.00	—	10	3.0
Part III:	36~60	1.00	—	10	4.5	1.00	—	10	3.0
1 C/1 C cycle
life

TABLE 10
physical properties of EX11 to EX15.
	D50	D99	D100	wt % oversize	BET
Sample	(μm)	(μm)	(μm)	(wt %)	(m2/g)
EX11	18.1	544.2	799.5	60.7%	0.250
EX12	12.4	31.2	38.7	9.0%	0.299
EX13	12.1	30.0	38.2	6.2%	0.294
EX14	10.9	26.5	33.1	4.4%	0.343
EX15	10.2	23.9	32.0	0.0%	0.821

Claims

1. A powderous positive electrode material for a lithium secondary battery, the material having the general formula Li1+x[Ni1−a−b−cMaM′bM″c]1−xO2−z; M being either one or more elements selected from the group consisting of Mn, Zr and Ti,M′ being either one or more elements selected from the group consisting of Al, B and Co,M″ being a dopant different from M and M′,

2. The powderous positive electrode material of claim 1, wherein M=Mn and M′comprises either one of Al or Co.

3. The powderous positive electrode material of claim 1, wherein ΓP(D10P=0) is no more than 41%-16%(2a+b) for P=300 MPa.

4. The powderous positive electrode material of claim 1, wherein ΓP(D10P=0) is no more than 32.5%-10%(2a+b) for P=300 MPa.

5. The powderous positive electrode material of claim 1, wherein ΓP(D10P=0) is no more than 28% for P=300 MPa.

6. The powderous positive electrode material of claim 1, wherein 1-a−b≥0.5 and 1+x<1.

7. The powderous positive electrode material of claim 1, having a BET value after wash >1 m2/g.

8. The powderous positive electrode material of claim 1, having a pressed density greater than 3.0 g/cm3.

9. The powderous positive electrode material of claim 1, comprising up to 2 mol % of W, Mo, Nb, Zr, or a rare earth element.

10. The powderous positive electrode material of claim 1, having a soluble base content (Li2CO3+LiOH)<0.8 wt %.

11. The powderous positive electrode material of claim 1, comprising secondary particles substantially free from porosities larger than 20 nm.

12. The powderous positive electrode material of claim 1, comprising secondary particles containing less than 20 voids larger than 20 nm.

13. The powderous positive electrode material of claim 1, having a FWHM value of the (104) peak as defined by a pseudo hexagonal lattice with R-3m space group which is greater than 0.125 2-theta degrees.

14. The powderous positive electrode material of claim 1, having a FWHM value of the (015) peak as defined by a pseudo hexagonal lattice with R-3m space group which is greater than 0.125 2-theta degrees.

15. The powderous positive electrode material of claim 1, having a FWHM value of the (113) peak as defined by a pseudo hexagonal lattice with R-3m space group which is greater than 0.16 2-theta degrees.

16. The powderous positive electrode material of claim 1, having a second phase LiNx′Oy′ with 0<x′<1 and 0<y′<2, where N is selected from the group consisting of either one or more of W, Mo, Nb, Zr and rare earth elements.

17. A method for preparing the powderous positive electrode material according to claim 1, the material having the general formula Li1+x[Ni1−a−b−cMaM′bM″c]1−xO2−z, the method comprising: providing a mixture of one or more precursor materials comprising either one or more of Ni, M, M′ or M″, and a precursor material comprising Li,sintering the mixture at a temperature T expressed in ° C., with (945 (248*(1−2a−b)≤T≤(985−(248*(1−2a−b)), thereby obtaining agglomerated particles, andpulverizing the agglomerated particles whereby a powder is obtained having the BET≤0.37 m2/g and the Dmax<50 μm.

18. The powderous positive electrode material of claim 1, wherein ΓP(D10P=0) is no more than 24% for P=300 MPa.

19. The powderous positive electrode material of claim 1, wherein ΓP(D10P=0) is no more than 20% for P=300 MPa.