Patent Application
20230130440
The present invention relates to improved particulate lithium nickel oxide materials which are useful as cathode materials in lithium secondary batteries. The present invention also provides processes for preparing such lithium nickel oxide materials, and electrodes and cells comprising the materials.
Lithium transition metal oxide materials having the formula LiMO2, where M typically includes one or more transition metals, find utility as cathode materials in lithium ion batteries. Examples include LiNiO2 and LiCoO2.
U.S. Pat. No. 6,921,609 B2 describes a composition suitable for use as a cathode material of a lithium battery which includes a core composition having an empirical formula LixM′zNi1-yM″yO2 and a coating on the core which has a greater ratio of Co to Ni than the core.
WO 2013/025328 A1 describes a particle including a plurality of crystallites including a first composition having a layered α-NaFeO2-type structure. The particles include a grain boundary between adjacent crystallites, and the concentration of cobalt in the grain boundaries is greater than the concentration of cobalt in the crystallites. Cobalt enrichment is achieved by treatment of the particles with a solution of LiNO3 and Co(NO3)2, followed by spray drying and calcining.
Studies of LiNO2 and similar materials have shown that there is a phase transition from one hexagonal phase (H2) to another hexagonal phase (H3) during delithiation which occurs at high voltages (around 4.2 V vs Li+/Li) i.e. when the material has a significantly reduced lithium content. This phase transition is accompanied by a large and sudden reduction in volume of the unit cell caused by c-axis contraction. This c-axis contraction results in permanent structural damage to the material which has been linked to capacity fade upon cycling.
With demand increasing for lithium-ion batteries in high-end applications such as electric vehicles (EVs), it is imperative to use cathode materials which provide not only acceptable specific capacity but also excellent retention of that capacity over a large number of charging cycles, so that the range of the vehicle after each charge over its lifetime is as consistent as possible. Capacity retention is also commonly referred to simply as the “cyclability” of the battery.
There therefore remains a need for improved lithium transition metal oxide materials and processes for their manufacture. In particular, there remains a need for improvements in the capacity retention of lithium transition metal oxide materials when used as cathode materials in lithium secondary batteries.
The present inventors have found that including relatively high levels of magnesium in surface-modified lithium nickel oxide materials results in excellent capacity retention, even where the lithium nickel oxide material contains low levels of cobalt. Cobalt has been used previously in surface enrichment of lithium nickel oxide materials to enhance capacity retention, and the present inventors have found in particular that including relatively high levels of magnesium in the materials enables a reduction in the amount of cobalt in a surface enriched layer applied to the materials while maintaining excellent capacity retention.
Without wishing to be bound by theory, the present inventors believe that the doping of a certain level of magnesium into the LiNiO2-type material imparts structural stability to the material which reduces the amount of c-axis contraction during the H2→H3 phase transition. It is believed that a tetrahedral site at an intermediate position between the MO2 layer and the Li layer within the crystal is occupied by the magnesium ions when the Li content of the material becomes low, creating a “pillaring effect” which stabilises the structure and reduces the contraction of the c-axis which occurs during the H2→H3 phase transition, thereby mitigating the c-axis contraction and contributing to the observed increased capacity retention as a result.
Reducing the amount of cobalt in cathode materials is highly desirable in the industry, since cobalt can be a significant contribution to the cost of the materials (due to its high relative cost and historic price volatility), and because it may be preferable to reduce cobalt content for ethical reasons. Typically, reduction in cobalt content results in a reduction in capacity retention, and therefore providing battery materials with acceptable performance characteristics and low cobalt levels has been challenging.
Accordingly, a first aspect of the invention is a surface-modified particulate lithium nickel oxide material having Formula I
LiaNixCoyMgzAlpMqO2+b Formula I
in which:
0.8≤a≤1.2
0.8≤x<1
0<y≤0.080
0.025≤z≤0.10
0.004≤p≤0.01
0≤q≤0.2, and
−0.2≤b≤0.2;
wherein M is selected from Mn, V, Ti, B, Zr, Sr, Ca, Cu, Sn, Cr, Fe, Ga, Si, W, Mo, Ta, Y, Sc, Nb, Pb, Ru, Rh and Zn and combinations thereof; and
wherein the particulate lithium nickel oxide material comprises an enriched surface layer comprising aluminium and/or cobalt, wherein the surface enriched layer includes less than 1 wt % cobalt.
These particulate lithium nickel oxide materials provide excellent capacity retention when used as an electrode material in a lithium secondary cell or battery. Furthermore, they may provide other important benefits such as a low % increase in direct current internal resistance (DCIR) over time and/or an acceptably high level of specific capacity. The materials may therefore be used to provide cells or batteries of improved performance and enhanced usable lifetime, providing particular advantages in high-end applications such as electric vehicles, while achieving low cobalt content.
A second aspect of the invention is a process for preparing a surface-modified particulate lithium nickel oxide material having Formula I
LiaNixCoyMgzAlpMqO2+b Formula I
in which:
0.8≤a≤1.2
0.8≤x<1
0<y≤0.080
0.025≤z≤0.10
0.004≤p≤0.01
0≤q≤0.2, and
−0.2≤b≤0.2;
wherein M is selected from Mn, V, Ti, B, Zr, Sr, Ca, Cu, Sn, Cr, Fe, Ga, Si, W, Mo, Ta, Y, Sc, Nb, Pb, Ru, Rh and Zn and combinations thereof;
the process comprising the steps of:
A third aspect of the invention provides particulate lithium nickel oxide obtained or obtainable by a process described herein.
A fourth aspect of the invention provides a cathode material for a lithium secondary battery comprising the particulate lithium nickel oxide material according to the first aspect.
A fifth aspect of the invention provides a cathode comprising the particulate lithium nickel oxide material according to the first aspect.
A sixth aspect of the invention provides a lithium secondary cell or battery (e.g. a secondary lithium ion battery) comprising the cathode according to the fifth aspect. The battery typically further comprises an anode and an electrolyte.
A seventh aspect of the invention provides use of the particulate lithium nickel oxide according to the first aspect for the preparation of a cathode of a secondary lithium battery (e.g. a secondary lithium ion battery).
An eighth aspect of the invention provides the use of the particulate lithium nickel oxide according to the first aspect as a cathode material to improve the capacity retention or cyclability of a lithium secondary cell or battery.
A ninth aspect is a method of improving the capacity retention or cyclability of a lithium secondary cell or battery, comprising the use of a cathode material in the cell or battery, wherein the cathode material comprises the particulate lithium nickel oxide material according to the first aspect.
Preferred and/or optional features of the invention will now be set out. Any aspect of the invention may be combined with any other aspect of the invention unless the context demands otherwise. Any of the preferred and/or optional features of any aspect may be combined, either singly or in combination, with any aspect of the invention unless the context demands otherwise.
The particulate lithium nickel oxide material has a composition according to Formula I defined above. The compositions recited herein may be determined by Inductively Coupled Plasma (ICP) analysis as described in the Examples section below. It may be preferred that the compositions recited herein are ICP compositions. Similarly, the wt % content of elements in the particulate lithium nickel oxide materials may be determined using ICP analysis. The wt % values recited herein are determined by ICP and are with respect to the total weight of the particle analysed (except wt % lithium carbonate which is defined separately below).
In Formula I, 0.8≤a≤1.2. In some embodiments a is greater than or equal to 0.9, 0.95, 0.99 or 1.0. In some embodiments, a is less than or equal to 1.1, or less than or equal to 1.05. In some embodiments, 0.90≤a≤1.10, for example 0.95≤a≤1.05. In some embodiments, 0.99≤a≤1.05 or 1.0≤a≤1.05. It may be particularly preferred that 0.95≤a≤1.05.
In Formula I, 0.8≤x<1. In some embodiments, 0.85≤x<1 or 0.9≤x<1. In some embodiments, x is less than or equal to 0.99, 0.98, 0.97, 0.96 or 0.95. In some embodiments, x is great than or equal to 0.85, 0.9 or 0.95. In some embodiments, 0.8≤x≤0.99, for example 0.85≤x≤0.98, 0.85≤x≤0.98, 0.85≤x≤0.97, 0.85≤x≤0.96 or 0.90≤x≤0.95. It may be particularly preferred that 0.85≤x≤0.98.
In Formula I, 0<y≤0.080. In some embodiments y is greater than or equal to 0.005, 0.010, 0.015, 0.020, 0.025, 0.030 or 0.035. In some embodiments y is less than or equal to 0.075, 0.070, 0.065, 0.060, 0.055 or 0.050.
In some embodiments, 0.01≤y≤0.080. In some embodiments, 0.02≤y≤0.080. In some embodiments, 0.03≤y≤0.080. In some embodiments, 0.01≤y≤0.0.065. In some embodiments, 0.01≤y≤0.0.060. In some embodiments, 0.01≤y≤0.55. In some embodiments, 0.01≤y≤0.05. In some embodiments, 0.03≤y≤0.05.
In Formula I, 0.025≤z≤0.10. In some embodiments z is greater than or equal to 0.030, 0.035, 0.040 or 0.045. In some embodiments z is less than or equal to 0.09, 0.08, 0.07, 0.065, 0.06 or 0.055.
In some embodiments, 0.025≤z≤0.095, 0.025≤z≤0.090, 0.025≤z≤0.085, 0.025≤z≤0.080, 0.025≤z≤0.075, 0.025≤z≤0.070, 0.025≤z≤0.065, 0.025≤z≤0.060, 0.025≤z≤0.055, 0.030≤z≤0.055, 0.035≤z≤0.055, 0.040≤z≤0.055 or 0.045≤z≤0.055
In some embodiments, the particulate lithium nickel oxide material comprises relatively high levels of both nickel and magnesium. In some embodiments, 0.035≤z≤0.060 and 0.85≤x<1. In some embodiments, 0.035≤z≤0.060 and 0.90≤x<1. In some embodiments, 0.035≤z≤0.060 and 0.90≤x<1.
The combination of high levels of nickel and high levels of magnesium has been found to lead to significant improvements in capacity retention of the materials.
In some embodiments, the particulate lithium nickel oxide material comprises relatively high levels of both nickel and magnesium, and relatively low levels of cobalt. In some embodiments, 0.035≤z≤0.060, 0.85≤x<1 and 0.01≤y≤0.0.067. In some embodiments, 0.035≤z≤0.060, 0.90≤x<1 and 0.01≤y≤0.0.067. In some embodiments, 0.035≤z≤0.055, 0.90≤x<1 and 0.01≤y≤0.0.067.
In Formula I, 0.004≤p≤0.01. In some embodiments, p is less than or equal to 0.0090, 0.0080, 0.0075 or 0.0070. In some embodiments p is greater than or equal to 0.005, 0.0055 or 0.0060. In some embodiments, 0.004≤p≤0.0090, 0.005≤p≤0.008, 0.0055≤p≤0.0075 or 0.006≤p≤0.007. It may be particularly preferred that 0.0055≤p≤0.0075 or 0.0055≤p≤0.0080.
In Formula I, −0.2≤b≤0.2. In some embodiments b is greater than or equal to −0.1. In some embodiments b is less than or equal to 0.1. In some embodiments, −0.1≤b≤0.1. In some embodiments, b is 0 or about 0. In some embodiments, b is 0.
In Formula I, M is one or more selected from Mn, V, Ti, B, Zr, Sr, Ca, Cu, Sn, Cr, Fe, Ga, Si, W, Mo, Ta, Y, Sc, Nb, Pb, Ru, Rh and Zn. In some embodiments, M is one or more selected from Mn, V, Ti, B, Zr, Sr, Ca, Cu, Sn, Cr, Fe, Ga, Si and Zn. In some embodiments, M is one or more selected from Mn, V, Ti, B, Zr, Sr, Ca, Cu, Sn, Cr, Fe, Ga, Si and Zn. In some embodiments, M is Mn. In some embodiments, M represents a dopant which is present within the core of the particle but not within the enriched surface layer.
In Formula I, 0≤q≤0.2. In some embodiments, 0≤q≤0.15. In some embodiments, 0≤q≤0.10. In some embodiments, 0≤q≤0.05. In some embodiments, 0≤q≤0.04. In some embodiments, 0≤q≤0.03. In some embodiments, 0≤q≤0.02. In some embodiments, 0≤q≤0.01. In some embodiments, q is 0.
In some embodiments:
0.8≤a≤1.2
0.8≤x<1
0<y≤0.080
0.025≤z≤0.10
0.004≤p≤0.01
0≤q≤0.2, and
−0.2≤b≤0.2;
wherein M is selected from Mn, V, Ti, B, Zr, Sr, Ca, Cu, Sn, Cr, Fe, Ga, Si, W, Mo, Ta, Y, Sc, Nb, Pb, Ru, Rh and Zn and combinations thereof.
In some embodiments:
0.8≤a≤1.2
0.8≤x<1
0<y≤0.080
0.025≤z≤0.10
0.004≤p≤0.01
−0.2≤b≤0.2, and
q=0.
In some embodiments:
0.8≤a≤1.2
0.9≤x<1
0<y≤0.080
0.025≤z≤0.10
0.004≤p≤0.01
−0.2≤b≤0.2, and
q=0.
In some embodiments:
0.8≤a≤1.2
0.85≤x<1
0<y≤0.080
0.030≤z≤0.10
0.004≤p≤0.01
−0.2≤b≤0.2, and
q=0.
In some embodiments:
0.8≤a≤1.2
0.85≤x<1
0<y≤0.080
0.035≤z≤0.10
0.004≤p≤0.01
−0.2≤b≤0.2, and
q=0.
In some embodiments:
0.8≤a≤1.2
0.85≤x<1
0<y≤0.080
0.040≤z≤0.10
0.004≤p≤0.01
−0.2≤b≤0.2, and
q=0.
In some embodiments:
0.8≤a≤1.2
0.85≤x<1
0<y≤0.080
0.025≤z≤0.10
0.006≤p≤0.007
−0.2≤b≤0.2, and
q=0.
In some embodiments:
0.8≤a≤1.2
0.85≤x<1
0.02≤y≤0.070
0.030≤z≤0.10
0.006≤p≤0.007
−0.2≤b≤0.2, and
q=0.
In some embodiments:
0.8≤a≤1.2
0.85≤x<1
0.02≤y≤0.070
0.035≤z≤0.10
0.006≤p≤0.007
−0.2≤b≤0.2, and
q=0.
In some embodiments:
0.8≤a≤1.2
0.85≤x<1
0<y≤0.070
0.025≤z≤0.07
0.006≤p≤0.007
−0.2≤b≤0.2, and
q=0.
In some embodiments:
0.8≤a≤1.2
0.85≤x<1
0.02≤y≤0.070
0.025≤z≤0.70
0.006≤p≤0.007
−0.2≤b≤0.2, and
q=0.
In some embodiments:
0.8≤a≤1.2
0.85≤x<1
0.02≤y≤0.070
0.04≤z≤0.1
0.006≤p≤0.007
−0.2≤b≤0.2, and
q=0.
In some embodiments:
0.8≤a≤1.2
0.85≤x<1
0<y≤0.065
0.025≤z≤0.060
0.004≤p≤0.01
−0.2≤b≤0.2, and
q=0.
In some embodiments:
0.8≤a≤1.2
0.8≤x<1
0.02≤y≤0.065
0.025≤z≤0.060
0.004≤p≤0.01
−0.2≤b≤0.2, and
q=0.
In some embodiments:
0.8≤a≤1.2
0.8≤x<1
0<y≤0.065
0.030≤z≤0.060
0.004≤p≤0.01
−0.2≤b≤0.2, and
q=0.
In some embodiments:
0.8≤a≤1.2
0.8≤x<1
0.02≤y≤0.065
0.030≤z≤0.060
0.004≤p≤0.01
−0.2≤b≤0.2, and
q=0.
In some embodiments:
0.8≤a≤1.2
0.8≤x<1
0<y≤0.065
0.030≤z≤0.055
0.004≤p≤0.01
−0.2≤b≤0.2, and
q=0.
In some embodiments:
0.8≤a≤1.2
0.8≤x<1
0.02≤y≤0.065
0.030≤z≤0.055
0.004≤p≤0.01
−0.2≤b≤0.2, and
q=0.
In some embodiments:
0.8≤a≤1.2
0.8≤x<1
0.02≤y≤0.065
0.035≤z≤0.055
0.006≤p≤0.007
−0.2≤b≤0.2, and
q=0.
In some embodiments, the particulate lithium nickel oxide material is a crystalline (or substantially crystalline) material. It may have the α-NaFeO2-type structure. It may be a polycrystalline material, meaning that each particle of lithium nickel oxide material is made up of multiple crystallites (also known as crystal grains or primary particles) which are agglomerated together. The crystal grains are typically separated by grain boundaries. Where the particulate lithium nickel oxide is polycrystalline, it will be understood that the particles of lithium nickel oxide comprising multiple crystals are secondary particles.
The particulate lithium nickel oxide material of Formula I comprises an enriched surface, i.e. comprises a core material which has been surface modified (subjected to a surface modification process) to form an enriched surface layer. In some embodiments the surface modification results from contacting the core material with one or more further metal-containing compounds, and then optionally carrying out calcination of the material. The compounds may be in solution, and in such context herein the term “compound” refers to the corresponding dissolved species. For clarity, the discussions of the composition according to Formula I herein when in the context of surface-modified particles relate to the overall particle, i.e. the particle including the enriched surface layer.
Herein, the terms “surface modified”, “enriched surface” and “enriched surface layer” refer to a particulate material which comprises a core material which has undergone a surface modification or surface enrichment process to increase the concentration of aluminium and/or cobalt at or near to the surface of the particles. The term “enriched surface layer” therefore refers to a layer of material at or near to the surface of the particles which contains a greater concentration of aluminium and/or cobalt than the remaining material of the particle, i.e. the core of the particle.
In some embodiments, the particle comprises a greater concentration of Al in the enriched surface layer than in the core. In some embodiments, all or substantially all of the Al in the particle is in the enriched surface layer. In some embodiments, the core does not contain Al or contains substantially no Al, for example less than 0.01 wt % Al based on the total particle weight. As used herein, the content of a given element in the surface enriched layer is calculated by determining the wt % of that element in the particulate lithium nickel oxide material prior to surface enrichment (sometimes referred to herein as the first calcined material or the core material) by ICP to give value A, determining the wt % of that element in the final particulate lithium nickel oxide material after surface enrichment (and optional further calcination) by ICP to give value B, and subtracting value A from value B. Similarly, the content of a given element in the core may be determined by determining the wt % of that element in the particulate lithium nickel oxide material prior to surface enrichment (sometimes referred to herein as the first calcined material or the core material) by ICP.
As the skilled person will understand, elements may migrate between the core and the surface layer during preparation, storage or use of the material. Herein, where an element is stated to be present in (or absent from, or present in certain quantities in) the core, this is to be understood to refer to that element being intentionally added to, (or excluded from, or added in a particular quantity to) the core, and is not intended to exclude from the scope of protection materials where the distribution of elements is altered by migration during preparation, storage or use. Similarly, where an element is stated to be present in (or absent from, or present in certain quantities in) the surface enriched layer, this is to be understood to refer to that element being intentionally added to, (or excluded from, or added in a particular quantity to) the surface enriched layer, and is not intended to exclude from the scope of protection materials where the distribution of elements is altered by migration during preparation, storage or use. For example, where all or substantially all of the Al in the particle is in the enriched surface layer, this means that all or substantially all of the Al is added in the surface enrichment step, but does not preclude materials where some of the Al added in the surface enrichment step has migrated into the core.
In some embodiments, the enriched surface layer comprises Al and optionally comprises one or more of Li and Co. In some embodiments, the enriched surface layer comprises Al and Li but does not contain Co or contains substantially no Co, for example less than 0.01 wt % Co based on the total particle weight. In some embodiments, the enriched surface layer comprises Al but does not contain Li or Co, or contains substantially no Li or Co, for example less than 0.01 wt % each of Li and Co, based on the total particle weight. In some embodiments, the enriched surface layer does not contain any magnesium or nickel, for example contains less than about 0.01 wt % each of magnesium and nickel. In some embodiments, the enriched surface layer contains aluminium and optionally cobalt and/or lithium, but does not contain any magnesium or nickel, for example contains less than about 0.01 wt % each of magnesium and nickel.
In some embodiments, the particulate lithium nickel oxide material contains magnesium in an amount of from about 0.60 wt % to about 1.50 wt %, based on the total weight of the particle. In some embodiments, all or substantially all of the magnesium is in the core of the particle. In some embodiments the enriched surface layer contains no magnesium or substantially no magnesium, for example less than 0.01 wt % Mg based on the total particle weight.
In some embodiments, the particulate lithium nickel oxide material contains cobalt in an amount of from about 1 wt % to about 5 wt %, based on the total weight of the particle, for example about 2.5 wt % to about 4 wt %.
In some embodiments, the particulate lithium nickel oxide material contains aluminium in an amount of from about 0.10 wt % to about 0.50 wt %, based on the total weight of the particle, for example from about 0.10 wt % to about 0.45 wt %, from about 0.10 wt % to about 0.40 wt %, from about 0.10 wt % to about 0.35 wt %, from about 0.10 wt % to about 0.30 wt %, from about 0.10 wt % to about 0.25 wt %, from about 0.10 wt % to about 0.20 wt %, from about 0.11 wt % to about 0.20 wt %, from about 0.12 wt % to about 0.20 wt %, from about 0.13 wt % to about 0.20 wt %, from about 0.13 wt % to about 0.19 wt %, from about 0.13 wt % to about 0.18 wt %, from about 0.14 wt % to about 0.18 wt % or from about 0.15 wt % to about 0.18 wt %. In some embodiments, the enriched surface layer of the particulate lithium nickel oxide material contains aluminium in such an amount. Materials containing aluminium in such quantities have been found to have good electrochemical properties including good capacity retention. The aluminium content in the surface enriched layer is determined as described above.
The particulate lithium nickel oxide material of Formula I comprises a surface-modified structure comprising a core and an enriched surface layer at the surface of the core, wherein the enriched surface layer of the material contains less than about 1.0 wt % cobalt. The inventors have found that at the relatively high Mg levels specified in Formula I, the material is stabilised resulting in an improvement of capacity retention even when the amount of cobalt at the surface is reduced. In some embodiments, the magnesium is in the core of the material, i.e. the enriched surface layer does not include magnesium (or includes less than about 0.01 wt % magnesium). In some embodiments, the core of the particulate lithium nickel oxide material comprises at least about 0.55 wt % magnesium, for example at least about 0.60 wt %, 0.65 wt %, 0.70 wt %, 0.75 wt %, 0.80 wt %, 0.85 wt % or 0.90 wt % and the enriched surface layer of the particulate lithium nickel oxide material contains less than about 1.0 wt % cobalt, for example less than about 0.9 wt %, 0.8 wt %, 0.75 wt %, 0.7 wt % or 0.6 wt %. In some embodiments at such levels of magnesium, the enriched surface layer of the particulate lithium nickel oxide material contains no cobalt or substantially no cobalt, for example less than 0.01 wt % cobalt. In some embodiments, 0.03≤z≤0.06 and the amount of cobalt in the enriched surface layer is less than about 1.0 wt %, for example less than about 0.9 wt %, 0.8 wt %, 0.75 wt %, 0.7 wt % or 0.6 wt %. The amount of cobalt in the surface enriched layer may be 0 wt %, greater than 0 wt %, or at least 0.1 wt %.
The cobalt content in the surface enriched layer is determined as described above.
The inventors have surprisingly found that a reduced amount of cobalt at the surface of the material can be provided without detrimental effects on the properties of the material. The inventors have also found that including cobalt in the enriched surface layer may provide some benefits including reducing the level of Li2CO3 on the surface of the material, for example to provide from 0 wt % to about 1.5 wt % Li2CO3.
In some embodiments, the ratio of the mass of material in the enriched surface layer to the mass of material in the core is from 0.01 to 0.04, for example from 0.01 to 0.03, from 0.01 to 0.025 or from 0.014 to 0.022.
In some embodiments, the surface-modified particulate lithium nickel oxide material has a composition according to Formula I as defined herein, e.g.
LiaNixCoyMgzAlpMqO2+b Formula I
in which:
0.8≤a≤1.2
0.8≤x<1
0≤y≤0.080
0.025≤z≤0.10
0.004≤p≤0.01
0≤q≤0.2, and
−0.2≤b≤0.2;
wherein M is selected from Mn, V, Ti, B, Zr, Sr, Ca, Cu, Sn, Cr, Fe, Ga, Si, W, Mo, Ta, Y, Sc, Nb, Pb, Ru, Rh and Zn and combinations thereof;
wherein the surface-modified particulate lithium nickel oxide material comprises a core material which has been subjected to a surface modification, wherein the core material has a composition according to Formula II:
Lia1Nix1Coy1Mgz1Alp1Mq1O2+b1 Formula II
in which:
0.8≤a1≤1.2
0.8≤x1<1
0≤y1≤0.080
0.025≤z1≤0.10
0≤p1≤0.01
0≤q1≤0.2, and
−0.2≤b1≤0.2;
wherein M is selected from Mn, V, Ti, B, Zr, Sr, Ca, Cu, Sn, Cr, Fe, Ga, Si, W, Mo, Ta, Y, Sc, Nb, Pb, Ru, Rh and Zn and combinations thereof.
In some embodiments, p1=0, such that the core material has the following formula:
Lia1Nix1Coy1Mgz1Mq1O2+b1
In some embodiments the surface modification comprises immersion in a solution comprising aluminium species and/or cobalt species (for example in the form of an aluminium-containing compound and/or a cobalt-containing compound), followed by drying of the surface-modified material and optionally calcination. The solution may additionally contain lithium species (for example in the form of a lithium-containing compound). In some embodiments, the solution is heated, for example to a temperature of at least 50° C., for example at least 55° C. or at least 60° C. In some embodiments, the surface-modified material is spray-dried after being contacted with the solution. In some embodiments, the surface-modified material is calcined after spray drying.
The particulate lithium nickel oxide material typically has a D50 particle size of at least 4 μm, e.g. at least 5 μm, at least 5.5 μm, at least 6.0 μm or at least 6.5 μm. The particles of lithium nickel oxide (e.g. secondary particles) typically have a D50 particle size of 20 μm or less, e.g. 15 μm or less or 12 μm or less. In some embodiments, the D50 particle size is from about 5 μm to about 20 μm, for example about 5 μm to about 19 μm, for example about 5 μm to about 18 μm, for example about 5 μm to about 17 μm, for example about 5 μm to about 16 μm, for example about 5 μm to about 15 μm, for example about 5 μm to about 12 μm, for example about 5.5 μm to about 12 μm, for example about 6 μm to about 12 μm, for example about 6.5 μm to about 12 μm, for example about 7 μm to about 12 μm, for example about 7.5 μm to about 12 μm. Unless otherwise specified herein, the D50 particle size refers to Dv50 (volume median diameter) and may be determined by using the method set out in ASTM B822 of 2017 under the Mie scattering approximation, for example using a Malvern Mastersizer 3000.
In some embodiments, the D10 particle size of the material is from about 0.1 μm to about 10 μm, for example about 1 μm to about 10 μm, about 2 μm to about 8 μm, or from about 5 μm to about 7 μm. Unless otherwise specified herein, the D10 particle size refers to Dv10 (10% intercept in the cumulative volume distribution) and may be determined by using the method set out in ASTM B822 of 2017 under the Mie scattering approximation, for example using a Malvern Mastersizer 3000.
In some embodiments, the D90 particle size of the material is from about 10 μm to about 40 μm, for example from about 12 μm to about 35 μm, about 12 μm to about 30 μm, about 15 μm to about 25 μm or from about 16 μm to about 20 μm. Unless otherwise specified herein, the D90 particle size refers to Dv90 (90% intercept in the cumulative volume distribution) and may be determined by using the method set out in ASTM B822 of 2017 under the Mie scattering approximation, for example using a Malvern Mastersizer 3000.
In some embodiments, the tapped density of the particulate lithium nickel oxide is from about 1.9 g/cm3 to about 2.8 g/cm3, e.g. about 1.9 g/cm3 to about 2.4 g/cm3.
The tapped density of the material can suitably be measured by loading a graduated cylinder with 25 mL of powder. The mass of the powder is recorded. The loaded cylinder is transferred to a Copley Tapped Density Tester JV Series. The material is tapped 2000 times and the volume re-measured. The re-measured volume divided by the mass of material is the recorded tap density.
The particulate lithium nickel oxide typically comprises less than 1.5 wt % of surface Li2CO3. It may comprise less than 1.4 wt % of surface Li2CO3, e.g. less than 1.3 wt %, less than 1.2 wt %, less than 1.1 wt %, less than 1.0 wt %, less than 0.9 wt %, less than 0.8 wt %, less than 0.7 wt % or less than 0.6 wt %. It may have 0 wt % surface Li2CO3, but in some embodiments there may be at least 0.01 wt %, 0.02 wt % or 0.04 wt % of surface Li2CO3.
The amount of surface Li2CO3 may be determined by titration with HCl using bromophenol blue indicator. Typically, a first titration step with HCl and phenolphthalein indicator is carried out before titration with bromophenol blue indicator to remove any lithium hydroxide. The titration protocol may include the following steps:
The materials may have a c-axis contraction within the material during the H2→H3 phase transition of less than 4.4%.
In some embodiments, the c-axis contraction is less than 3.8%, for example less than 3.5%, for example less than 3.2%, or example less than 3.0%, for example less than 2.8%, for example less than 2.75%. The c-axis contraction may be at least 1%, at least 1.5% or at least 2%. The c-axis contraction may be measured by the method set out in the Examples.
The particulate lithium nickel oxide of the invention is characterised by an improved capacity retention for cells which incorporate the material as a cathode, in particular a high retention of capacity after 50 cycles. When determined at a temperature of 23° C. in a half cell coin cell vs lithium, under a charge/discharge rate of 1C and voltage window of 3.0-4.3V, with an electrode loading of 9.0 mg/cm2 and an electrode density of 3.0 g/cm3, it has been found that materials according to the invention may provide a capacity retention of greater than 94% after 50 cycles, and in some cases as high as around 98%. The % capacity retention after 50 cycles is defined as the capacity of the cell after the 50th cycle as a percentage of the initial capacity of the cell after its first charge. For clarity, one cycle includes a complete charge and discharge of the cell. For example, 90% capacity retention means that after the 50th cycle the capacity of the cell is 90% of the initial capacity.
An aspect of the invention is a lithium secondary cell or battery wherein the capacity retention of the cell or battery after 50 cycles at 23° C. and a 1C charge/discharge rate and a voltage window of 3.0-4.3V is at least 93%.
The material may have a capacity retention (after 50 cycles in a half cell coin cell vs Li, at an electrode loading of 9.0 mg/cm2 and an electrode density of 3.0 g/cm3, tested at 23° C. and a 1C charge/discharge rate and voltage window of 3.0-4.3V) of at least 93%.
In some embodiments, the capacity retention is at least 94%, for example at least 95%, for example at least 96%, for example at least 97%.
Materials of the invention are also characterised by a surprisingly low direct current internal resistance (DCIR). DCIR tends to increase over time as the secondary cell or battery is cycled. It has been found that materials according to the invention provide a % increase in DCIR of less than 50% after 50 cycles, and in some cases an increase as low as 24%, when tested at a temperature of 23° C. in a half cell coin cell vs lithium, under a charge/discharge rate of 10 and voltage window of 3.0-4.3V, with an electrode loading of 9.0 mg/cm2 and an electrode density of 3.0 g/cm3.
The material may have a % increase in DCIR (after 50 cycles in a half cell coin cell vs Li, at an electrode loading of 9.0 mg/cm2 and an electrode density of 3.0 g/cm3, tested at 23° C. and a 1C charge/discharge rate and voltage window of 3.0-4.3V) of less than 50%.
In some embodiments, the % increase in DCIR is less than 45%, for example less than 40%, for example less than 35%, for example less than 30%, for example less than 25%.
Materials of the invention are also characterised by a high specific capacity. It has been found that materials according to the invention when tested in a cell at 23° C., a 1C discharge rate and a voltage window of 3.0-4.3V, with an electrode loading of 9.0 mg/cm2 and an electrode density of 3.0 g/cm3 in a half call coin cell vs Li metal, provide a specific capacity of at least 160 mAh/g, in some cases as high as 190 mAh/g. This high specific capacity in combination with the high capacity retention on cycling provides a cell or battery of improved performance with an extended usable lifetime which is useful in high performance applications such as in electric vehicles.
The material may have a specific capacity when tested in a cell at 23° C., a 1C discharge rate and a voltage window of 3.0-4.3V, with an electrode loading of 9.0 mg/cm2 and an electrode density of 3.0 g/cm3 in a half call coin cell vs Li metal of at least 180 mAh/g. In some embodiments, the specific capacity is at least 190 mAh/g, for example at least 200 mAh/g.
The process for preparing the particulate lithium nickel oxide typically comprises the steps of:
wherein M is selected from Mn, V, Ti, B, Zr, Sr, Ca, Cu, Sn, Cr, Fe, Ga, Si, W, Mo, Ta, Y, Sc, Nb, Pb, Ru, Rh and Zn and combinations thereof.
In some embodiments, the first calcined material is a core material having Formula II:
Lia1Nix1Coy1Mgz1Alp1Mq1O2+b1 Formula II
in which:
0.8≤a1≤1.2
0.8≤x1<1
0≤y1≤0.080
0.025≤z1≤0.10
0≤p1≤0.01
0≤q1≤0.2, and
−0.2≤b1≤0.2;
wherein M is selected from Mn, V, Ti, B, Zr, Sr, Ca, Cu, Sn, Cr, Fe, Ga, Si, W, Mo, Ta, Y, Sc, Nb, Pb, Ru, Rh and Zn and combinations thereof.
In some embodiments, p1=0, such that the core material has the following formula:
Lia1Nix1Coy1Mgz1Mq1O2+b1
In some embodiments, the process includes a further calcination step after the surface modification step.
In some embodiments q1=0.
The lithium-containing compound may be selected from lithium hydroxide (e.g. LiOH or LiOH.H2O), lithium carbonate (Li2CO3), and hydrated forms thereof. Lithium hydroxide may be particularly preferred.
The nickel-containing compound may be selected from nickel hydroxide (Ni(OH)2), nickel oxide (NiO), nickel oxyhydroxide (NiOOH), nickel sulfate, nickel nitrate, nickel acetate and hydrated forms thereof. Nickel hydroxide may be particularly preferred.
The cobalt-containing compound may be selected from cobalt hydroxide (Co(OH)2), cobalt oxide (CoO, Co2O3, Co3O4), cobalt oxyhydroxide (CoOOH), cobalt sulfate, cobalt nitrate, cobalt acetate and hydrated forms thereof. Cobalt hydroxide may be particularly preferred.
The magnesium-containing compound may be selected from magnesium hydroxide (Mg(OH)2), magnesium oxide (MgO), magnesium sulfate, magnesium nitrate, magnesium acetate and hydrated forms thereof. Magnesium hydroxide may be particularly preferred.
The M-containing compound may be selected from M hydroxide, M oxide, M nitrate, M sulfate, M carbonate or M acetate and hydrated forms thereof. M hydroxide may be particularly preferred.
Alternatively, two or more of nickel, cobalt, magnesium and optionally M may be provided as a mixed metal hydroxide, e.g. a mixed nickel cobalt hydroxide or a mixed nickel cobalt M hydroxide. The mixed metal hydroxide may be a coprecipitated hydroxide. It may be polycrystalline.
The mixed metal hydroxide may have a composition according to Formula III:
NixCoyMgzMq(OH)2+b Formula III
in which x, y, z, q and b are each independently as defined herein. If a cobalt enrichment step is carried out (as described below), it may be preferred that the value for y in Formula III is less than the value for y in Formula I.
Such mixed metal hydroxides may be prepared by co-precipitation methods well-known to the person skilled in the art. These methods may involve the co-precipitation of the mixed metal hydroxide from a solution of metal salts, such as metal sulfates, for example in the presence of ammonia and a base, such as NaOH. In some cases suitable mixed metal hydroxides may be obtainable from commercial suppliers known to the skilled person.
The calcination step may be carried out at a temperature of at least 400° C., at least 500° C., at least 600° C. or at least 650° C. The calcination step may be carried out at a temperature of 1000° C. or less, 900° C. or less, 800° C. or less or 750° C. or less. The material to be calcined may be at a temperature of 400° C., at least 500° C., at least 600° C. or at least 650° C. for a period of at least 2 hours, at least 5 hours, at least 7 hours or at least 10 hours. The period may be less than 24 hours.
The calcination step may be carried out under a CO2-free atmosphere. For example, CO2-free air may be flowed over the materials to be calcined during calcination and optionally during cooling. The CO2-free air may, for example, be a mix of oxygen and nitrogen. The CO2-free atmosphere may be oxygen (e.g. pure oxygen). Preferably, the atmosphere is an oxidising atmosphere. As used herein, the term “CO2-free” is intended to include atmospheres including less than 100 ppm CO2, e.g. less than 50 ppm CO2, less than 20 ppm CO2 or less than 10 ppm CO2. These CO2 levels may be achieved by using a CO2 scrubber to remove CO2.
In some embodiments, the CO2-free atmosphere comprises a mixture of O2 and N2. In some embodiments, the mixture comprises a greater amount of N2 than O2. In some embodiments, the mixture comprises N2 and O2 in a ratio of from 50:50 to 90:10, for example from 60:40 to 90:10, for example about 80:20.
In some embodiments, the particulate lithium nickel oxide material of Formula I comprises a surface-modified structure comprising a core and an enriched surface layer at the surface of the core, resulting from performing a surface-modification step on a core material having Formula II:
Lia1Nix1Coy1Mgz1Alp1Mq1O2+b1 Formula II
in which:
0.8≤a1≤1.2
0.8≤x1<1
0≤y1≤0.080
0.025≤z1≤0.10
0≤p1≤0.01
0≤q1≤0.2, and
−0.2≤b1≤0.2;
wherein M is selected from Mn, V, Ti, B, Zr, Sr, Ca, Cu, Sn, Cr, Fe, Ga, Si, W, Mo, Ta, Y, Sc, Nb, Pb, Ru, Rh and Zn and combinations thereof.
The surface modification step may comprise contacting the core material with an aluminium-containing compound and/or a cobalt-containing compound, and optional one or more of a lithium-containing compound and an M-containing compound. The aluminium-containing compound, cobalt-containing compound, and optional lithium-containing compound and M-containing compound may be provided in solution, for example in aqueous solution.
In some embodiments, p1=0, such that the core material has the following formula:
Lia1Nix1Coy1Mgz1Mq1O2+b1
In some embodiments q1=0.
The surface-modification step of the processes of the invention (also referred to herein as a surface enrichment step) comprises contacting the core material with aluminium and/or cobalt, to increase the concentration of aluminium and/or cobalt in the grain boundaries and/or at or near to the surface of the particles. In some embodiments, the surface-modification step (also referred to herein as a surface enrichment step) comprises contacting the core material with additional metal selected from one or more of lithium and M, to increase the concentration of such metal in the grain boundaries and/or at or near to the surface of the particles. The surface modification may be carried out by contacting a core material with an aluminium-containing compound and/or a cobalt-containing compound, and optionally one or more further metal-containing compounds. For example, the compounds may be independently selected from nitrates, sulfates or acetates. Nitrates may be particularly preferred. The compounds may be provided in solution (e.g. aqueous solution). The compounds may be soluble in water.
The mixture of the core material with the aluminium-containing compound and/or cobalt containing compound, and optionally one or more further metal-containing compounds may be heated, for example to a temperature of at least 40° C., e.g. at least 50° C. The temperature may be less than 100° C. or less than 80° C. Where the compound(s) are provided in solution, the mixture of the solution with the intermediate may be dried, e.g. by evaporation of the solvent or by spray drying.
The aluminium-containing compound and/or cobalt-containing compound, and optional one or more further metal-containing compounds may be provided as a composition, referred to herein as a “surface modification composition”. The surface modification composition may comprise a solution of the aluminium-containing compound and/or cobalt-containing compound, and optional one or more further metal-containing compounds (e.g. aqueous solution).
The surface modification composition may comprise an aluminium-containing compound and optionally one or more of a lithium-containing compound, a cobalt-containing compound and an M-containing compound. The surface modification composition may comprise a cobalt-containing compound and optionally one or more of a lithium-containing compound, an aluminium-containing compound and an M-containing compound. The surface modification composition may comprise an aluminium-containing compound and optionally one or more of a lithium-containing compound and a cobalt-containing compound. The surface modification composition may comprise a cobalt-containing compound and optionally one or more of a lithium-containing compound and an aluminium-containing compound. The surface modification composition may comprise an aluminium-containing compound, a cobalt-containing compound and optionally a lithium-containing compound. The surface modification composition may comprise an aluminium-containing compound as the sole metal-containing compound (i.e. thereby lacking a lithium-containing compound, a cobalt-containing compound and an M-containing compound). The surface modification composition may comprise a cobalt-containing compound as the sole metal-containing compound (i.e. thereby lacking a lithium-containing compound, an aluminium-containing compound and an M-containing compound).
The cobalt-containing compound, the aluminium-containing compound, lithium-containing compound and M-containing compound used in the surface modification step may be as defined above with reference to the cobalt-containing compound, the aluminium-containing compound, the lithium-containing compound and the M-containing compound used in the formation of the intermediate (core) material. It may be particularly preferred that the aluminium-containing compound and each of the one or more further metal-containing compounds is a metal-containing nitrate. It may be particularly preferred that the aluminium-containing compound is aluminium nitrate. It may be particularly preferred that the lithium-containing compound is lithium nitrate. It may be particularly preferred that the cobalt-containing compound is cobalt nitrate. It may be preferred that the cobalt-containing compound, the further aluminium-containing compound and the further lithium-containing compound are soluble in water.
In some embodiments, the surface modification step comprises contacting the core material with additional metal-containing compounds in an aqueous solution. The core material may be added to the aqueous solution to form a slurry or suspension. In some embodiments the slurry is agitated or stirred. In some embodiments, the weight ratio of core material to water in the slurry after addition of the core material to the aqueous solution is from about 1.5:1 to about 1:1.5, for example from about 1.4:1 to about 1:1.4, about 1.3:1 to about 1:1.3, about 1.2:1 to about 1:1.2 or about 1.1:1 to about 1:1.1. The weight ratio may be about 1:1.
Typically, the surface modification step is carried out after the first calcination step described above.
The surface modification step may be followed by a second calcination step. The second calcination step may be carried out at a temperature of at least 400° C., at least 500° C., at least 600° C. or at least 650° C. The second calcination step may be carried out at a temperature of 1000° C. or less, 900° C. or less, 800° C. or less or 750° C. or less. The material to be calcined may be at a temperature of 400° C., at least 500° C., at least 600° C. or at least 650° C. for a period of at least 30 minutes, at least 1 hour or at least 2 hours. The period may be less than 24 hours. The second calcination step may be shorter than the first calcination step.
The second calcination step may be carried out under a CO2-free atmosphere as described above with reference to the first calcination step.
The process may include one or more milling steps, which may be carried out after the first and/or second calcination steps. The nature of the milling equipment is not particularly limited. For example, it may be a ball mill, a planetary ball mill or a rolling bed mill. The milling may be carried out until the particles (e.g. secondary particles) reach the desired size. For example, the particles of lithium nickel oxide (e.g. secondary particles) are typically milled until they have a D50 particle size of at least 5 μm, e.g. at least 5.5 μm, at least 6 μm or at least 6.5 μm. The particles of lithium nickel oxide (e.g. secondary particles) are typically milled until they have a D50 particle size of 15 μm or less, e.g. 14 μm or less or 13 μm or less.
The process of the present invention may further comprise the step of forming an electrode (typically a cathode) comprising the lithium nickel oxide material. Typically, this is carried out by forming a slurry of the particulate lithium nickel oxide, applying the slurry to the surface of a current collector (e.g. an aluminium current collector), and optionally processing (e.g. calendaring) to increase the density of the electrode. The slurry may comprise one or more of a solvent, a binder, carbon material and further additives.
Typically, the electrode of the present invention will have an electrode density of at least 2.5 g/cm3, at least 2.8 g/cm3 or at least 3 g/cm3. It may have an electrode density of 4.5 g/cm3 or less, or 4 g/cm3 or less. The electrode density is the electrode density (mass/volume) of the electrode, not including the current collector the electrode is formed on. It therefore includes contributions from the active material, any additives, any additional carbon material, and any remaining binder.
The process of the present invention may further comprise constructing a battery or electrochemical cell including the electrode comprising the lithium nickel oxide. The battery or cell typically further comprises an anode and an electrolyte. The battery or cell may typically be a secondary (rechargeable) lithium (e.g. lithium ion) battery.
The present invention will now be described with reference to the following examples, which are provided to assist with understanding the present invention, and are not intended to limit its scope.
100 g Ni0.960Co0.031Mg0.099(OH)2 and 26.36 g LiOH were dry mixed in a poly-propylene bottle for 30 mins. The LiOH was pre-dried at 200° C. under vacuum for 24 hours and kept dry in a purged glovebox filled with dry N2.
The powder mixture was loaded into 99%+ alumina crucibles and calcined under an artificial CO2-free air mix which was 80:20 N2:O2. Calcination was performed as follows: to 450° C. (5° C./min) with 2 hours hold, ramp to 700° C. (2° C./min) with a 6 hour hold and cooled naturally to 130° C. The artificial air mix was flowing over the powder bed throughout the calcination and cooling. The title compound was thereby obtained.
The samples were then removed from the furnace at 130° C. and transferred to a high-alumina lined mill pot and milled on a rolling bed mill until D50 was between 12.0 and 12.5 μm.
D50 was measured according to ASTM B822 of 2017 using a Malvern Mastersizer 3000 under the Mie scattering approximation and was found to be 9.5 μm. The chemical formula of the material was determined by ICP analysis to be Ni0.953Co0.030Mg0.010O2.
The procedure according to Comparative Example 1A was repeated except that 26.21 g of LiOH were dry mixed with 100 g Ni0.948Co0.031Mg0.021(OH)2. The title compound was thereby obtained. D50 was found to be 10.2 μm. The chemical formula of the material was determined by ICP analysis to be Li1.019Ni0.949Co0.031Mg0.020O2.
The procedure according to Comparative Example 1A was repeated except that 24.8 g of LiOH were dry mixed with 100 g Ni0.917Co0.050Mg0.033(OH)2. The title compound was thereby obtained. D50 was found to be 9.65 μm. The chemical formula of the material was determined by ICP analysis to be Li1.027Ni0.923Co0.049Mg0.029O2.
The procedure according to Comparative Example 1A was repeated except that 25.92 g of LiOH were dry mixed with 100 g Ni0.915Co0.049Mg0.036(OH)2. The title compound was thereby obtained. D50 was found to be 12.2 μm. The chemical formula of the material was determined by ICP analysis to be Li1.007Ni0.923Co0.049Mg0.038O2.
The procedure according to Comparative Example 1A was repeated except that 25.75 g of LiOH were dry mixed with 100 g Ni0.903Co0.048Mg0.049(OH)2. The title compound was thereby obtained. The chemical formula of the material was determined by ICP analysis to be Li0.998Ni0.917Co0.049Mg0.052O2.
The procedure according to Comparative Example 1A was repeated except that 25.94 g of LiOH were dry mixed with 100 g Ni0.918Co0.045Mg0.037(OH)2. The title compound was thereby obtained. D50 was found to be 9.0 μm. The chemical formula of the material was determined by ICP analysis to be Li1.024Ni0.926Co0.045Mg0.037O2.
The procedure according to Comparative Example 1A was repeated except that 26.20 g of LiOH were dry mixed with 100 g Ni0.952Co0.029Mg0.019(OH)2. The title compound was thereby obtained. D50 was found to be 9.6 μm. The chemical formula of the material was determined by ICP analysis to be Li1.003Ni0.956Co0.030Mg0.020O2.
The procedure according to Comparative Example 1A was repeated except that 26.29 g of LiOH were dry mixed with 100 g Ni0.957Co0.029Mg0.014(OH)2. The title compound was thereby obtained. D50 was found to be 9.3 μm. The chemical formula of the material was determined by ICP analysis to be Li1.009Ni0.957Co0.030Mg0.015O2.
The procedure according to Comparative Example 1A was repeated except that 25.96 g of LiOH were dry mixed with 100 g Ni0.935Co0.029Mg0.037(OH)2. The title compound was thereby obtained. D50 was found to be 10.7 μm. The chemical formula of the material was determined by ICP analysis to be Li1.005Ni0.944Co0.029Mg0.038O2.
The procedure according to Comparative Example 1A was repeated except that 25.75 g of LiOH were dry mixed with 100 g Ni0.900Co0.053Mg0.048(OH)2. The title compound was thereby obtained. D50 was found to be 9.49 μm. The chemical formula of the material was determined by ICP analysis to be Li0.996Ni0.914Co0.053Mg0.051O2.
Bases 12 to 20, listed in Table 4 below, were made by an analogous process to Bases 1 to 10.
The product of Comparative Example 1A was sieved through a 53 μm sieve and transferred to a N2-purged glovebox. An aqueous solution containing 5.91 g Co(NO3)2·6H2O, 0.47 g LiNO3 and 2.44 g Al(NO3)3·9H2O in 100 mL water was heated to between 60 and 65° C. 100 g of the sieved powder was added rapidly while stirring vigorously. The slurry was stirred at a temperature between 60 and 65° C. until the supernatant was colourless. The slurry was then spray-dried.
After spray-drying powders were loaded into 99%+ alumina crucibles and calcined under an artificial CO2-free air mix which was 80:20 N2:O2. Calcination was performed as follows: ramp to 130° C. (5° C./min) with 5.5 hours hold, ramp to 450° C. (5° C./min) with 1 hour hold, ramp to 700° C. (2° C./min) with a 2 hours hold and cooled naturally to 130° C. The artificial air mix was flowing over the powder bed through the calcination and cooling. The title compound was thereby obtained.
The samples were then removed from the furnace at 130° C. and transferred to a purged N2-filled glove-box.
The sample was milled in a high-alumina lined mill pot on a rolling bed mill. The target end point of the milling was when D50 was between 10 and 11 μm; D50 was measured after milling and found to be 9.5 μm. The sample was passed through a 53 μm sieve and stored in a purged N2 filled glove-box. The water content of the material was 0.18 wt %. The chemical formula of the material was determined by ICP analysis to be Li1.018Ni0.930Co0.049Mg0.010Al0.006O2.
The product of Comparative Example 1B was subjected to the procedure set out under Comparative Example 2A, except that the aqueous solution contained 5.90 g Co(NO3)2·6H2O, 0.47 g LiNO3 and 2.43 g Al(NO3)3·9H2O in 100 mL water. The title compound was thereby obtained. D50 was found to be 8.5 μm. The water content of the material was 0.28 wt %. The chemical formula of the material was determined by ICP analysis to be Li1.002Ni0.927Co0.053Mg0.020Al0.0065O2.
The product of Comparative Example 10 was subjected to the procedure set out under Comparative Example 2A, except that the aqueous solution contained 5.89 g Co(NO3)2·6H2O, 0.46 g LiNO3 and 2.43 g Al(NO3)3·9H2O in 100 mL water. The title compound was thereby obtained. D50 was found to be 7.61 μm. The water content of the material was 0.2 wt %. The chemical formula of the material was determined by ICP analysis to be Li0.995Ni0.909Co0.068Mg0.027Al0.0065O2.
The product of Comparative Example 1D was subjected to the procedure set out under Example 1A, except that the aqueous solution contained 3.94 g Co(NO3)2·6H2O and 2.43 g Al(NO3)3·9H2O in 100 mL water, but did not contain any LiNO3. The title compound was thereby obtained. D50 was found to be 11.7 μm. The water content of the material was 0.26 wt %. The chemical formula of the material was determined by ICP analysis to be Li0.985Ni0.913Co0.061Mg0.037Al0.0069O2.
The product of Comparative Example 1E was subjected to the procedure set out under Example 1A, except that the aqueous solution contained 3.93 g Co(NO3)2·6H2O and 2.42 g Al(NO3)3·9H2O in 100 mL water, but did not contain any LiNO3. The title compound was thereby obtained. D50 was found to be 10.7 μm. The water content of the material was 0.09 wt %. The chemical formula of the material was determined by ICP analysis to be Li0.980Ni0.905Co0.061Mg0.051Al0.0065O2.
The product of Comparative Example 1F was subjected to the procedure set out under Example 1A, except that the aqueous solution contained 2.43 g Al(NO3)3·9H2O in 100 mL water, but did not contain any Co(NO3)2·6H2O or LiNO3. The title compound was thereby obtained. D50 was found to be 7.5 μm. The water content of the material was 0.18 wt %. The chemical formula of the material was determined by ICP analysis to be Li1.003Ni0.923Co0.045Mg0.038Al0.0062O2.
The product of Comparative Example 1G was subjected to the procedure set out under Comparative Example 2A, except that the aqueous solution contained 2.44 g Al(NO3)3·9H2O in 100 mL water, but did not contain any Co(NO3)2·6H2O or LiNO3. The title compound was thereby obtained. D50 was found to be 7.9 μm. The water content of the material was 0.29 wt %. The chemical formula of the material was determined by ICP analysis to be Li0.997Ni0.952Co0.029Mg0.019Al0.0065O2. Comparative Example 1H—Comparative Compound 8 (Li1.002Ni0.919Co0.064Mg0.014Al0.0062O2)
The product of Comparative Example 1H was subjected to the procedure set out under Comparative Example 2A, except that the aqueous solution contained 11.82 g Co(NO3)2·6H2O, 1.88 g LiNO3 and 2.44 g Al(NO3)3·9H2O in 100 mL water. The title compound was thereby obtained. D50 was found to be 8.2 μm. The water content of the material was 0.29 wt %. The chemical formula of the material was determined by ICP analysis to be Li1.002Ni0.919Co0.064Mg0.014Al0.0062O2.
The product of Comparative Example 1J was subjected to the procedure set out under Comparative Example 2A, except that the aqueous solution contained 11.77 g Co(NO3)2·6H2O, 1.87 g LiNO3 and 2.44 g Al(NO3)3·9H2O in 100 mL water. The title compound was thereby obtained. D50 was found to be 10.0 μm. The water content of the material was 0.08 wt %. The chemical formula of the material was determined by ICP analysis to be Li0.980Ni0.909Co0.066Mg0.037Al0.0066O2.
The product of Comparative Example 1J was subjected to the procedure set out under Comparative Example 2A, except that the aqueous solution contained 3.93 g Co(NO3)2·6H2O and 2.42 g Al(NO3)3·9H2O in 100 mL water, but did not contain any LiNO3. The title compound was thereby obtained. D50 was found to be 9.4 μm. The water content of the material was 0.17 wt %. The chemical formula of the material was determined by ICP analysis to be Li0.987Ni0.900Co0.064Mg0.051Al0.0065O2.
100 g Ni0.905Co0.084Mg0.010(OH)2 and 26.33 g LiOH were dry mixed in a poly-propylene bottle for 1 hour. The LiOH was pre-dried at 200° C. under vacuum for 24 hours and kept dry in a glovebox purged with dry N2.
The powder mixture was loaded into 99%+ alumina crucibles and calcined under an artificial CO2 free air mix which was 80:20 N2:O2. Calcination was performed as follows: to 450° C. (5° C./min) with 2 hours hold, ramp to 700° C. (2° C./min) with a 6 hour hold and cooled naturally to 130° C. The artificial air mix was flowing over the powder bed throughout the calcination and cooling.
The samples were then removed from the furnace at 130° C. and transferred to a purged N2 filled glove-box. The sample was transferred to a high-alumina lined mill pot and milled on a rolling bed mill until D50 was between 12.0-12.5 μm.
After milling, the product was sieved through a 53 μm sieve and transferred to a purged N2 filled glovebox. An aqueous solution containing 11.83 g Co(NO3)2·6H2O, 1.88 g LiNO3 and 2.44 g Al(NO3)3·9H2O in 100 mL water was heated to between 60 and 65° C. 100 g of the sieved powder was added rapidly while stirring vigorously. The slurry was stirred at a temperature between 60 and 65° C. until the supernatant was colourless. The slurry was then spray-dried.
After spray-drying powders were loaded into 99%+ alumina crucibles and calcined under an artificial CO2 free air mix which was 80:20 N2:O2. Calcination was performed as follows: ramp to 130° C. (5° C./min) with 5.5 hours hold, ramp to 450° C. (5° C./min) with 1 hour hold, ramp to 700° C. (2° C./min) with a 2 hours hold and cooled naturally to 130° C. The artificial air mix was flowing over the powder bed through the calcination and cooling. The title compound was thereby obtained.
The samples were then removed from the furnace at 130° C. and transferred to a N2 filled glove-box.
The sample was milled in a high-alumina lined mill pot on a rolling bed mill. The end point of the milling was when D50 was between 10 and 11 μm; D50 was measured after milling and found to be 8.8 μm. The sample was passed through a 53 μm sieve and stored in a purged N2 filled glove-box.
The water content of the material was 0.4 wt %. The chemical formula of the material was determined by ICP analysis to be Li0.984Ni0.877Co0.115Mg0.010Al0.0066O2.
Comparative Compounds 12, 14, 15, 17a, 17b, 18a and 19, listed in Table 3 below, were made by an analogous process to Comparative Compounds 1-3 and 7-9, using the following bases:
Compounds 13, 18b and 20, listed in Table 3 below, were made by an analogous process to Compounds 4, 5, 6 and 10, using the following bases:
Li2CO3 Content
Surface Li2CO3 content in samples was determined using a two-stage titration with phenolphthalein and bromophenol blue. For the titration, surface lithium carbonate was extracted from a sample of each material by agitating in deionised water for 5 minutes to provide an extractate solution, the extractate solution was separated from residual solid. Phenolphthalein indictor was added to the extractate solution, and the extracted solution was titrated using HCl solution until the extractate solution became clear (indicating the removal of any LiOH). Bromophenol blue indictor was added to the extractate solution, and the extracted solution titrated using HCl solution until the extractate solution turned yellow. The amount of lithium carbonate in the extractate solution was be calculated from this bromophenol titration step, the wt % of surface lithium carbonate in each sample was calculated assuming 100% extraction of surface lithium carbonate into the extractate solution.
The results for the materials tested were as set out in Table 3:
Compositional Analysis
The total magnesium and cobalt contents (weight % based on the total particle weight) in the Comparative and Inventive materials was determined by ICP and is given in Table 4 below.
The surface cobalt content was calculated by subtracting the ICP wt % Co in the base material from the ICP wt % Co in the final material. The core cobalt content is taken as the ICP wt % Co in the base material.
ICP (Inductively Coupled Plasma)
The elemental composition of the compounds was measured by ICP-OES. For that, 0.1 g of material are digested with aqua regia (3:1 ratio of hydrochloric acid and nitric acid) at ˜130° C. and made up to 100 mL. The ICP-OES analysis was carried out on an Agilent 5110 using matrix matched calibration standards and yttrium as an internal standard. The lines and calibration standards used were instrument-recommended.
Electrochemical Testing
Electrodes were made in a 94:3:3 active:carbon:binder formulation with an ink at 65% solids. 0.6 g of SuperC65 carbon was mixed with 5.25 g of N-methyl pyrrolidone (NMP) on a Thinky® mixer. 18.80 g of active material was added and further mixed using the Thinky® mixer. Finally, 6.00 g of Solef® 5130 binder solution (10 wt % in NMP) was added and mixed in the Thinky mixer. The resulting ink was cast onto aluminium foils using a 125 μm fixed blade coater and dried at 120° C. for 60 minutes. Once dry, the electrode sheet was calendared in an MTI calendar to achieve a density of 3 g/cm3. Individual electrodes were cut and dried under vacuum overnight before transferring to an argon filled glovebox.
Coin cells were built using a lithium anode and 1M LiPF6 in 1:1:1 EC (ethylene carbonate):EMC (ethyl methyl carbonate):DMC (dimethyl carbonate)+1 wt % VC (vinylene carbonate) electrolyte. Electrodes selected had a loading of 9.0 mg/cm2 and a density of 3 g/cm3. Electrochemical measurements were taken from averages of three cells measured at 23° C., and a voltage window of 3.0-4.3V.
Electrochemical characteristics evaluated include first cycle efficiency (FCE), 0.1C specific capacity, 1.0C specific capacity, capacity retention and DCIR growth using a 10 s pulse. Capacity retention and DCIR growth were determined based on performance after 50 cycles at 1C.
Table 4 below includes details of the materials tested.
Design of Experiments Approach
Traditionally experiments are planned varying one factor at a time whilst keeping the other factors constant. An alternative approach is “Design of Experiments”, where multiple variables are changed at once, allowing a large experimental space to be covered using relatively few experimental points. A computer-based statistical analysis is then applied to ascertain the key interactions.
The compounds made in the Examples and Comparative Examples above were prepared and analysed according to a Design of Experiments approach. Statistical analysis determined that increasing capacity retention was most strongly related to increasing Mg content, and to a lesser extent with increasing Co content in the surface enriched layer. The correlations had the following p-values:
Mg content: <0.0001
Co in surface layer: 0.0086
with the p-value indicating the statistical significance of the results and a p-value of <0.05 signifying a statistically significant result. The stronger dependence of capacity retention on Mg content than surface Co content indicates that excellent capacity retention may be achieved by increasing Mg while decreasing Co content in the surface modified layer.
Analysis of c-Axis Contraction
The particulate lithium nickel oxide of the invention is characterised by a measurably reduced contraction of the c-axis during the H2→H3 phase transition which occurs at around 4.2 V vs Li+/Li. The length of the c-axis can be measured by ex-situ X-ray powder diffraction (XRPD) on cycled electrodes. This can be measured for the material in the H2 phase and the H3 phase, and a comparison of these can be used to determine the c-axis contraction. In order to understand the effect of the Mg dopant on the LiNi(1-x-y)CoxMgyO2 structure, site disorder defect structures were computed at several low lithiation states. Site exchange defects were built by swapping the position of two cations (or a cation and a site vacancy). The defect energies show that at low lithium loading, a site disordered structure is preferred where the Mg cation moves from its normal octahedral site (transition metal site) to a tetrahedral site midway between the transition metal oxide layer and the Li layer. Calculations also show that Li may have a tendency to move to an equivalent tetrahedral site on the other side of the transition metal oxide layer. This disordered structure is significantly more stable than the undefective structure and reduces the lattice contraction observed at low Li loadings by a pillaring effect.
Table 5 below shows the c-axis changes for some materials of the invention based on ex situ XRPD measurements of electrodes cycled to 4 V and 4.3 V, respectively.
| Number | Date | Country | Kind |
|---|---|---|---|
| 2004511.8 | Mar 2020 | GB | national |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/GB2021/050726 | 3/25/2021 | WO |
