The present invention relates to a positive electrode active material having ultra-fine grains and highly oriented primary particles, and a lithium secondary battery including the same, and more particularly, to a positive electrode active material having ultra-fine grains and highly oriented primary particles have a heteroatom at the grain boundary between them, and the concentration of the heteroatom is higher at the grain boundary than in the central portion of the primary particle, and a lithium secondary battery including the same.
With the development of portable mobile electronic devices such as smart phones, MP3 players, and tablet PCs, the demand for secondary batteries capable of storing electrical energy has increased explosively. In particular, with the advent of electric vehicles, medium and large energy storage systems, and portable devices requiring high energy density, the demand for lithium secondary batteries has increased.
With an increasing demand for such lithium secondary batteries, research and development for positive electrode active materials for use in lithium secondary batteries has been conducted. For example, Korean Patent Application Publication No. 10-2014-0119621 (Korean Patent Application No. 10-2013-0150315) discloses a secondary battery having high-voltage capacity and long cycle life characteristics as a result of controlling the kinds and composition of metals substituted in a precursor for preparing a lithium-rich positive electrode active material and controlling the kinds and amounts of metals added.
An object of the present invention is to provide a positive electrode active material including primary particles having ultra-fine grains, and a lithium secondary battery including the same.
Another object of the present invention is to provide a positive electrode active material which has ultra-fine grains and highly oriented particles, and has high capacity and improved cycle life characteristics by having a high content of nickel, and a lithium secondary battery including the same.
Still another object of the present invention is to provide a positive electrode active material containing a heteroatom inside primary particles and at the grain boundary between the primary particles, wherein the concentration of the heteroatom is higher at the grain boundary than inside the primary particles, and a lithium secondary battery including the same.
Objects to be achieved by the present invention are not limited to the above-described objects.
To achieve the above objects, the present invention provides a positive electrode active material and a positive electrode.
One embodiment of the present invention includes a positive electrode active material for a lithium secondary battery including a secondary particle composed of a plurality of primary particles, wherein the primary particles include oriented particles provided in the surface portion of the secondary particle and having a short axis and a long axis, the oriented particles include ultra-fine grain grains having a grain size of 0.1 µm to 0.5 µm, and the grain size is obtained by calculating the square root of the average cross-sectional area of the oriented particles.
Another embodiment of the present invention includes a positive electrode active material for a lithium secondary battery including a secondary particle composed of a plurality of primary particles, wherein the primary particles include oriented particles provided in the surface portion of the secondary particle and having a short axis and a long axis, the oriented particles include those in which the average absolute value of acute angles among angles between long-axis-direction extension lines passing through the centers of the oriented particles and angle baselines connecting between the central points of the extension lines and the central point of the secondary particle is 20 or less, and the central point of each of the extension lines is the center of a line connecting one end to the other end of the oriented particle.
Still another embodiment of the present invention includes a positive electrode active material for a lithium secondary battery including a secondary particle composed of a plurality of primary particles, wherein the primary particles include oriented particles provided in the surface portion of the secondary particle and having a short axis and a long axis, and the oriented particles include those in which the distance between a long-axis-direction extension line passing through the centers of the oriented particles and a central baseline passing through the central point of the secondary particle in parallel with the extension line is 1.5 µm or less.
Other embodiments of the present invention include a positive electrode active material for a lithium secondary battery including a secondary particle composed of a plurality of primary particles, wherein the primary particles include oriented particles provided in the surface portion of the secondary particle and having a short axis and a long axis, wherein the primary particles contain a heteroatom, wherein the heteroatom is provided at the grain boundary between the primary particles and inside the primary particles, and the concentration of the heteroatom is higher at the grain boundary between the primary particles than inside the primary particles, so that the heteroatom reduces the degree of agglomeration of the oriented particles when the positive electrode active material is calcined at a high temperature of 700° C. or higher.
In one embodiment, 70% or more of the primary particles distributed in a thickness (T) region ranging from the outermost surface of the secondary particle to a portion corresponding to 40% of the diameter (L) of the secondary particle in a direction toward the center of the secondary particle may be oriented particles.
In one embodiment, the thickness (T) ranging from the outermost surface of the secondary particle to a portion corresponding to 40% of the diameter (L) of the secondary particle in a direction toward the center of the secondary particle may be 1.5 µm to 4 µm.
In one embodiment, the long-axis direction of the oriented particles may correspond to a lithium ion diffusion path.
In one embodiment, the average aspect ratio of the oriented particles, which is the ratio of the length of the long axis to the length of the short axis, may be 2.5 to 15.
In one embodiment, the average diameter of the secondary particles may be 5 µm to 20 µm.
In one embodiment, the heteroatom may be composed of any one or more of antimony (Sb), molybdenum (Mo), tungsten (W), niobium (Nb), tellurium (Te), tantalum (Ta), zirconium (Zr), titanium (Ti), tin (Sn), yttrium (Y), indium (In), vanadium (V), and chromium (Cr).
In one embodiment, the average concentration of the heteroatom in the positive electrode active material may be 0.01 mol% to 2 mol%.
In one embodiment, the positive electrode active material may include one prepared by calcining a lithium compound together with a composite metal hydroxide including any one or more of nickel (Ni), cobalt (Co), manganese (Mn), and aluminum (Al), wherein the heteroatom is added together with any one or more of nickel (Ni), cobalt (Co), manganese (Mn), and aluminum (Al), or added together with the lithium compound, before calcination.
In one embodiment, the positive electrode active material may include lithium, a transition metal and oxygen, the primary particles may include a layered crystal structure in which a lithium (Li) layer including only lithium and a transition metal layer including only a transition metal are alternately and regularly arranged, the doping region may include a cation-ordered structure, the cation-ordered structure may include a first mixed layer and a second mixed layer, each containing lithium and the transition metal, together with the lithium layer and the transition metal layer, the content of lithium in the first mixed layer may be higher than the content of the transition metal therein, the content of the transition metal in the second mixed layer may be higher than the content of lithium therein, the first mixed layer and the second mixed layer may be stacked together, and a unit cell formed by the first mixed layer and second mixed layer stacked together may include a long-range ordered lattice with an increased a-axis lattice constant.
In one embodiment, the positive electrode active material may include one prepared by calcining a lithium compound together with a composite metal hydroxide containing any one or more of nickel (Ni), cobalt (Co), manganese (Mn), and aluminum (Al), and the positive electrode active material may be any one or more of NC-based, NCM-based, NCA-based, LNO-based, and NCMA-based positive electrode active materials.
In one embodiment, the composite metal hydroxide may be produced by a co-precipitation reaction such that any one or more of nickel (Ni), cobalt (Co), manganese (Mn), and aluminum (Al), which are contained in the composite metal hydroxide, have a concentration gradient in at least a portion of the composite metal hydroxide.
Embodiments according to another aspect of the present invention include a lithium secondary battery including: a positive electrode including the above-described positive electrode active material; a negative electrode facing the positive electrode and comprising graphite or lithium metal; a separator interposed between the positive electrode and the negative electrode; and an electrolyte solution or solid electrolyte containing a lithium salt.
Embodiments according to still another aspect of the present invention a composite metal hydroxide for a lithium secondary battery including at least one of nickel (Ni), cobalt (Co), manganese (Mn), and aluminum (Al) and including a preliminary secondary particle composed of a plurality of preliminary primary particles, wherein the preliminary primary particles include oriented particles provided in the surface portion of the preliminary secondary particle and provided in a rod shape having a short axis and a long axis, the oriented particles include those in which the average absolute value of acute angles between long-axis-direction extension lines passing through the centers of the oriented particles and angle baselines connecting between the central points of the extension lines and the central point of the secondary particle is 20 or less, the central point of each of the extension lines is the center of a line connecting one end to the other end of the oriented particle, and the oriented particles include those in which the distance between the long-axis-direction extension line passing through the centers of the oriented particles and a central baseline passing through the central point of the secondary particle in parallel with the extension line is 1.5 µm or less.
In one embodiment, the composite metal hydroxide may be produced by a co-precipitation reaction such that any one or more of nickel (Ni), cobalt (Co), manganese (Mn), and aluminum (Al), which are contained in the composite metal hydroxide, have a concentration gradient in at least a portion of the composite metal hydroxide.
According to the present invention as described above, it is possible to provide a positive electrode active material having improved cycle life characteristics and charge-discharge rate capability by having a high content of nickel and suppressing the formation of microcracks in the charged state of the nickel-rich positive electrode active material while maintaining a high discharge capacity, and a lithium secondary battery including the same.
In addition, according to the present invention, it is possible to provide a positive electrode active material in which at least a portion of primary particles are rod-shaped primary particles having a long axis and a short axis, and the primary particles include a heteroatom at the grain boundary between the primary particles at a higher concentration than in the central positions of the primary particles, and thus the positive electrode active material has a high content of nickel (Ni-rich), and at the same time, the crystal structure and the morphology of the primary particles are maintained during long-term cycling, thereby reducing the formation of microcracks, and a lithium secondary battery including the same.
Hereinafter, preferred embodiments of the present invention will be described in detail with reference to the accompanying drawings. However, the technical spirit of the present invention is not limited to the embodiments disclosed herein and may be embodied in other forms. Rather, the embodiments disclosed herein are provided so that this disclosure will be thorough and complete, and will fully convey the spirit of the present invention to those skilled in the art.
Throughout the present specification, when any component is referred to as being “on” another component, it not only refers to a case where the component is directly on the other but also a case where a third component exists between them. In addition, in the drawings, the thicknesses of the film and the region are exaggerated for effective description of the technical contents.
Furthermore, terms such as first, second, third and the like are used in various embodiments of the present specification in order to describe various components, but these components should not be limited by these terms. These terms are only used to distinguish any component from another component. Thus, a component referred to as a first component in any one embodiment may also be referred to as a second component in other embodiments. Each embodiment described and illustrated herein includes its complementary embodiment as well. Moreover, as used herein, the term “and/or,” includes at least one of the associated listed items.
In the specification, singular expressions include plural expressions unless specified otherwise in the context thereof. The terms “include”, “comprise”, “have”, etc., are intended to denote the existence of mentioned characteristics, numbers, steps, components, or combinations thereof, but do not exclude the probability of existence or addition of one or more other characteristics, numbers, steps, components, or combinations thereof.
In the following description, the detailed description of related known functions or configurations will be omitted when it may obscure the subject matter of the present invention.
In addition, in the present specification, “the expression “the proportion of the first crystal structure in a specific portion is higher than the proportion of the second crystal structure” means that the specific portion includes both the first crystal structure and the second crystal structure, and means not only that the proportion of the first crystal structure in the specific portion is higher than the proportion of the second crystal structure, but also that the specific portion has only the first crystal structure.
In addition, in the present specification, the crystal system may consist of seven crystal systems: triclinic, monoclinic, orthorhombic, tetragonal, trigonal or rhombohedral, hexagonal, and cubic crystal systems.
In addition, in the present application, “mol%” is interpreted as meaning the content of any metal in a positive electrode active material or a positive electrode active material precursor, based on 100% of the sum of metals other than lithium and oxygen in the positive electrode active material or the positive electrode active material precursor.
Referring to
In the secondary particle 100, the primary particles 30 constituting the central portion 10 and the primary particles 30 constituting the surface portion 20 may have the same or different sizes, and the primary particles 30 constituting the surface portion 20 may be provided in a shape having a long axis and a short axis, and at least a portion of the primary particles 30 constituting the surface portion 20 may be oriented toward the central portion 10 of the secondary particle 100. At least a portion of the primary particles 30 constituting the surface portion 20 may be provided in a radial form.
The secondary particle 100 may be composed of one or more metals including lithium, and at least a portion of the one or more metals may have a concentration gradient in the central portion 10 and the surface portion 20. Alternatively, in the secondary particle 100, a gap may be formed between the central portion 10 and the surface portion 20, or the crystal form may be different between the central portion 10 and the surface portion 20, or a difference in image between the central portion 10 and the surface portion 20 may be created by making the central portion 10 and then making the surface portion 20 to surround the central portion 10. Thus, the secondary particle may be provided in a core-shell form.
The primary particles 30 may extend radially from one region in the second particle toward the surface portion 20 of the secondary particle. The one region in the secondary particle may be the central portion 10 of the secondary particle. In other words, the primary particle 30 may be formed in a flake shape, and the cross-section of the primary particles 30 may be of a rod shape extending from one region inside the secondary particle toward the surface 20 of the secondary particle.
Between the primary particles 30 having a rod shape, that is, between the primary particles 30 extending in a direction D from the central portion 10 of the secondary particle to the surface portion 20 thereof, a path for movement of metal ions (e.g., lithium ions) and an electrolyte may be provided. Accordingly, the positive electrode active material according to an embodiment of the present invention may improve the charging and discharging efficiency of a secondary battery.
According to one embodiment, in the direction from the center 10 of the secondary particle toward the surface 20 of the secondary particle, the primary particles 30 relatively adjacent to the surface portion 20 of the secondary particle may have a longer length than the primary particles 30 relatively adjacent to the central portion 10 of the secondary particle. In other words, in at least a portion of the secondary particle extending from the central portion 10 of the secondary particle to the surface portion 20, the length of the primary particles 30 may increase toward the surface portion 20.
For example, at least a portion of the primary particles 30 may have a short axis length and a long axis length, wherein the long axis length is longer than the short axis length. Thus, at least a portion of the primary particles 30 may be provided in a rod shape having an aspect ratio of 1 or more.
According to one embodiment of the present invention, in a positive electrode material including a secondary particle composed of a plurality of primary particles, at least one of the primary particles may contain a heteroatom. The hetero element may be an element other than lithium (Li), nickel (Ni), cobalt (Co), manganese (Mn) and aluminum (Al), and the heteroatom may comprise any one or more of antimony (Sb), molybdenum (Mo), tungsten (W), niobium (Nb), tellurium (Te), tantalum (Ta), zirconium (Zr), titanium (Ti), tin (Sn), yttrium (Y), indium (In), vanadium (V), and chromium (Cr).
Referring to
On the other hand, the positive electrode active material according to this embodiment contains a heteroatom. As the heteroatom, a compound containing an excess of the heteroatom is provided at the grain boundary between the primary particles, and thus can prevent a phenomenon in which the plurality of primary particles are agglomerated during high-temperature calcination. Accordingly, the composite metal oxide in the positive electrode active material containing the heteroatom has a rod shape approximately similar to that before calcination, and thus microcracks may be inhibited from being formed in the secondary particle during a charging/discharging process, thereby improving electrochemical properties.
The heteroatom may be provided in a doping region formed by diffusion into the primary particle, and an excess of the heteroatom may also be provided and remain at the grain boundary between the primary particles. The concentration of the heteroatom may be higher at the grain boundary between the primary particles than inside the primary particles, so that agglomeration of the oriented particles during calcination of the positive electrode active material at a high temperature of 700° C. or higher may be reduced. The primary particles may include oriented particles provided on the surface portion of the secondary particle and having a short axis and a long axis.
For example, at the grain boundary between the primary particles, a compound (Li—HA—O) composed of the heteroatom (HA), lithium and oxygen may be provided and an excess of the heteroatom may remain. The heteroatom may be disposed between the plurality of primary particles or may be provided by accumulation of a compound containing the heteroatom at the grain boundary between the primary particles in an island form. Here, the island shape refers to a shape provided to cover the primary particles at the grain boundary between the primary particles while exposing at least a portion of the primary particle. The concentration of the heteroatom included in the island form may be higher than the concentration of the heteroatom inside the primary particle. For example, the thickness of the compound (containing an excess of the heteroatom) at the grain boundary between the primary particles (the average thickness of the islands) may be about 2 nm to 15 nm, or 2 nm to 13 nm, or 2 nm to 10 nm, or 2 nm to 8 nm, or 2 nm to 5 nm, or 5 nm to 15 nm, or 7 nm to 15 nm, or 10 nm to 15 nm.
Specifically, when the heteroatom is tantalum (Ta), the compound may comprise any one or more of Ta2O5, LiTaO3, Li2TaO3, Li2TaO4 and Li3TaO4; when the heteroatom is antimony (Sb), the compound may comprise any one or more of Sb2O3, Sb2O5, LiSbO3, Li2SbO3, Li2SbO4 and Li3SbO4; and when the heteroatom is niobium (Nb), the compound may comprise any one or more of Nb2O5, LiNbO3, LiNb3O8, Li2NbO3, Li2NbO4 and Li3NbO4. In addition, when the heteroatom is tungsten (W), the compound may comprise any one or more of WO3, LiWO3, Li2WO3, Li2WO4 and Li3WO4, and when the heteroatom is molybdenum (Mo), the compound may comprise any one or more of MoO3, LiMoO3, Li2MoO3, Li2MoO4, and Li3MoO4.
The doping region may be formed by uniform diffusion of the same heteroatom as the heteroatom provided at the grain boundary into the primary particle. The heteroatom-containing compound provided on the grain boundary between the primary particles may interact with the elements constituting the primary particles, whereby the compound may function as a sintering inhibitor that reduces the extent to which pristine particles constituting the composite metal hydroxide are agglomerated together, even when the composite metal hydroxide is calcined at high temperature.
The heteroatom provided in excess at the grain boundary between the primary particles may prevent preliminary primary particles constituting the composite metal hydroxide, which is a precursor of the positive electrode active material, from being converted into equiaxed grains due to agglomeration of the particles during calcination at a high temperature of 700° C. or higher, so that the primary particles of the positive electrode active material after calcination may have a rod shape approximately similar to the rod shape of the preliminary primary particles of the composite metal hydroxide.
The average concentration of the heteroatom in the positive electrode active material may be 0.01 mol% to 2 mol%, specifically 0.05 mol% to 2 mol%, or 0.1 mol% to 2 mol%, or 0.5 mol% to 2 mol%. The average concentration of the heteroatom at the grain boundary between the primary particles may be 0.5 mol% to 12 mol%, specifically 2 mol% to 12 mol%.
If the average concentration of the heteroatom throughout the positive electrode active material is less than 0.01 mo%l, a problem may arise in that the heteroatom is not uniformly distributed throughout the primary particles constituting the secondary particle, and if the average concentration is more than 2 mol%, a problem may arise in that the heteroatom may degrade capacity. In addition, if the average concentration of the heteroatom at the grain boundary between the primary particles is less than 2 mol%, a problem may arise in that the heteroatom cannot prevent agglomeration of the primary particles during high-temperature calcination, and if the average concentration is more than 12 mol%, a problem may arise in that the heteroatom is excessively accumulated at the grain boundary between the primary particles, so that the movement of lithium ions through the primary particles is not easy.
The positive electrode active material may contain lithium, a transition metal and oxygen, and the primary particles may include a layered crystal structure in which a lithium layer containing only lithium and a transition metal layer containing only a transition metal are alternately and regularly arranged. Here, the primary particles may further include a cation-ordered structure in a doping region formed by diffusion of the heteroatom.
The cation-ordered structure, together with the lithium layer and the transition metal layer, may further include a first mixed layer and a second mixed layer, each containing both lithium and a transition metal, wherein the content of lithium in the first mixed layer may be higher than the content of the transition metal, and the content of the transition metal in the second mixed layer may be higher than the content of lithium.
The first mixed layer and the second mixed layer are stacked together, and a unit cell formed by the first mixed layer and second mixed layer stacked together may include a long-range ordered lattice with an increased a-axis lattice constant. A lattice formed by the first and second mixed layers stacked adjacent to each other may include a superlattice whose a-axis is twice as long as that of a lattice formed by the lithium layer and the transition metal layer.
Specifically, the first mixed layer and the second mixed layer may be stacked adjacent to each other and alternately and regularly repeated to form a layered structure, and the first and second mixed layers stacked adjacent to each other may be configured such that the transition metal of the first mixed layer and the lithium of the second mixed layer may correspond to each other.
For example, the first and second mixed layer may be configured such that the lithium of the lithium layer and the transition metal of the transition metal layer are substituted with each other.
One example of the cation-ordered structure may include an ordered lattice structure formed by 1:1 site exchange between the lithium and transition metal provided at the positions corresponding to each other in the lithium layer and transition metal layer facing each other, although only lithium is present in the lithium layer and only the transition metal is present in the transition metal layer.
Another example of the cation-ordered structure may include a structure in which a lithium-transition metal layer and a transition metal-lithium layer are alternately and regularly formed, wherein a layer formed by exchange of the lithium of the lithium layer with the transition metal is referred to as the lithium-transition metal layer (first mixed layer), and a layer formed by site exchange of the transition metal of the transition metal layer with the lithium of the lithium layer is referred to as the transition metal-lithium layer (second mixed layer).
The positive electrode active material according to this embodiment may be composed of primary particles having a layered structure, and the cation-ordered structure may be formed adjacent to the grain boundary in the primary particles.
A lattice formed by the lithium-transition metal layer and the transition metal-lithium layer may include a long-range ordered lattice whose a-axis is longer than that of a lattice formed by the lithium layer and the transition metal layer.
The positive electrode active material may be prepared by calcining a lithium compound and a composite metal hydroxide including at least one of nickel (Ni), cobalt (Co), manganese (Mn) and aluminum (Al). In this case, the heteroatom may be added together with at least one of nickel (Ni), cobalt (Co), manganese (Mn) and aluminum (Al) in a wet process, or may be added together with the lithium compound in a dry process and calcined. As the composite metal hydroxide is calcined together with the lithium compound at high temperature, a spherical positive electrode active material formed by calcination may be produced. The heteroatom may be calcined together with the lithium compound after already included in the composite metal hydroxide, or may be added together with the lithium compound. In the positive electrode active material produced by calcination, the heteroatom may form a doping region inside the primary particle, and may be provided in excess in the form of a compound at the grain boundary between the primary particles.
The primary particles may include oriented particles provided on the surface of the secondary particle and having a long axis and a short axis, and the oriented particles may include those in which the average absolute value (orientation angle) of acute angles among angles between long-axis-direction extension lines passing through the centers of the oriented particles and angle baselines connecting between the central points of the extension lines and the central point of the secondary particle is 20 or less, wherein the central point of each of the extension lines may be the center of a line connecting one end to the other end of the oriented particle. The distance (orientation distance) between the long-axis-direction extension line passing through the centers of the primary particles and the central baseline passing through the central point of the secondary particle in parallel with the extension line may be 1.5 µm or less.
The secondary particles may have an average diameter of 5 µm to 20 µm. The secondary particles may have an approximately spherical shape, and specifically, the secondary particles have an average diameter of 6 µm to 20 µm, or 9 µm to 20 µm, or 12 µm to 20 µm, or 15 µm to 20 µm, or 5 µm to 18 µm, or 5 µm to 15 µm, 5 µm to 10 µm.
When the compound containing an excess of a heteroatom is provided at the grain boundary between the primary particles according to this embodiment, the primary particles constituting the positive electrode active material after calcination may have a rod shape approximately similar to that of preliminary primary particles constituting the composite metal hydroxide.
For example, the composite metal hydroxide may contain any one or more of nickel, cobalt, magnesium and aluminum, and may include an approximately sphere-shaped preliminary secondary particle prepared by a co-precipitation method and formed by agglomeration of a plurality of preliminary primary particles. Among the preliminary primary particles, the preliminary primary particles provided on the surface of the preliminary secondary particle may include oriented particles having a rod shape.
The oriented particles may include highly oriented particles provided on the surface of the preliminary secondary particle, among the preliminary primary particles constituting the composite metal hydroxide, and may include those in which the average absolute value of acute angles (e.g., orientation angles) among angles between long-axis-direction extension lines passing through the centers of the oriented particles and angle baselines connecting between the central points of the extension lines and the central point of the secondary particle is 20 or less, wherein the central point of each of the extension lines may be the center of a line connecting one end to the other end of the oriented particle.
The oriented particles may include those in which the distance (e.g., orientation distance) between the long-axis-direction extension line passing through the centers of the oriented particles and the central baseline passing through the central point of the secondary particle in parallel with the extension line may be 1.5 µm or less.
The orientation angle and orientation distance of the oriented particles in the composite metal hydroxide may affect the orientation angle and orientation distance of the primary particles of the positive electrode active material provided after high-temperature calcination, and even when the oriented particles of the composite metal hydroxide have an orientation angle and an orientation distance within the above-described ranges, the positive electrode active material produced by calcination at high temperature may have a structure with improved stability.
In addition, the composite metal hydroxide is produced by a co-precipitation reaction, and at least any one or more of nickel (Ni), cobalt (Co), manganese (Mn) and aluminum (Al) constituting the composite metal hydroxide may have a concentration gradient in at least a portion of the composite metal hydroxide.
The composite metal hydroxide may be mixed with a lithium compound and then calcined at high temperature to produce a positive electrode active material. Here, the extent to which the preliminary primary particles constituting the composite metal oxide are agglomerated during the calcination process may be reduced, and thus the primary particles constituting the positive electrode active material which is a calcined body may have a shape similar to the rod shape of the preliminary primary particles.
In the positive electrode active material according to this embodiment, 70% or more of the primary particles distributed in a thickness (T) region ranging from the outermost surface of the secondary particle to a portion corresponding to 40% of the diameter (L) of the secondary particle in a direction toward the center may be oriented particles. Specifically, the proportion of oriented particles among the primary particles distributed in a thickness (T) region ranging from the outermost surface of the secondary particle to a portion corresponding to 40% of the diameter (L) of the secondary particle in a direction toward the center may be about 75% or more, or 80% or more, or 85% or more.
For example, the orientation of the primary particles provided in a thickness (or depth, T) region ranging from the outermost surface to a portion corresponding to 40% of the diameter (L) of the secondary particle in a direct toward the inside may be particularly high, and the number of the primary particles provided in the surface portion of the secondary particle, which is the thickness (T) region of the secondary particle, may be similar to the number of preliminary primary particles in the composite metal hydroxide which is a precursor before high-temperature calcination.
In general, the thickness (T) region of the secondary particle is a portion that is particularly affected by heat during the calcination process. Thus, a problem arises in that, when the composite metal hydroxide is calcined, the orientation of the primary particles in the thickness (T) region of the secondary particle is reduced due to agglomeration of the primary particles.
On the other hand, in the positive electrode active material according to this embodiment, the heteroatom provided in excess at the grain boundary between the primary particles can prevent agglomeration of the primary particles in the thickness (T) region of the secondary particle so as to have high orientation. Accordingly, even after the positive electrode active material according to this embodiment is calcined at high temperature, the structure and orientation of the preliminary primary particles in the precursor stage can be maintained similar to those of the primary particles in the calcined body, and thus the overall structural stability of the positive electrode active material may be ensured and movement of lithium ions through the positive electrode active material may be easy even after multiple charging/discharging cycles.
In the positive electrode active material according to this embodiment, 80% or more of the primary particles distributed in a thickness (T) region ranging from the outermost surface of the secondary particle to a portion corresponding to 40% of the diameter (L) of the secondary particle in a direction toward the center may be oriented particles. The long-axis direction of the oriented particles may correspond to a lithium ion diffusion path.
The primary particles may further include oriented particles, and the oriented particles may be provided approximately in the surface portion of the secondary particle. Specifically, the secondary particle may have a spherical shape having a central portion and a surface portion, and the oriented particles may be provided in the surface portion of the secondary particle, that is, a portion that comes into contact with an electrolyte.
Referring to
As the average of the orientation angles in the positive electrode active material according to this embodiment is 20 or less, the primary particles are aligned from the outermost surface of the secondary particle toward the center of the secondary particle, and thus may provide a movement path to facilitate lithium ion diffusion. As shown in the left drawing of
When the average of the orientation angles of the oriented particles provided at the outer surface of the secondary particle is 20 or less, the oriented particles are structurally aligned in the secondary particle, the change in the volume of the primary particles during charging/discharging may occur reversibly, thereby preventing the occurrence of microcracks and changes in the morphology of the particles. In addition, the positive electrode active material may relieve micro strain in the positive electrode active material even under hard conditions such as high voltage and/or high-rate charge and discharge after long-term cycling, and prevent stress accumulation, thereby further improving the performance characteristics of a secondary battery, such as electrochemical properties, safety, and reliability. Here, the morphology of the particles may be expressed by the orientation angle, orientation distance, grain size, aspect ratio, and width of the primary particles.
Specifically, in the oriented particles, the average of acute angles among angles between long-axis-direction extension lines passing through the oriented particles and angle baselines connecting the central points of the extension lines may be 2 to 20, or 3 to 20, or 4 to 20, or 2 to 18, or 2 to 15, or 2 to 12, or 2 to 10, or 4 to 10.
The oriented particles may include those in which the distance (orientation distance) between the long-axis-direction extension line (A) passing through the centers of the oriented particles and the central baseline (C2) passing through the central point of the secondary particle in parallel with the extension line (A) is 1.5 µm or less.
The orientation distance refers to an orientation angle (n) which is a distance between the line connecting the long axes of the primary particles provided in the surface portion of the secondary particle, for example, the long axes of the primary particles provided in a region at a distance of 2 µm or more from the center with respect to the radius of the secondary particle, and the central baseline (C2) passing through the central point of the secondary particle in parallel with the long axes of the oriented particles. This means that the number of primary particles aligned toward the center of the secondary particle increases as the orientation distance (n) decreases. The orientation distance n may indicate the degree of agglomeration of the primary particles provided in the surface portion of the secondary particle, together with the level at which the primary particles are aligned toward the center of the secondary particle. For example, as the orientation distance (n) decreases, the primary particles provided in the surface portion of the secondary particle may be aligned toward the center of the secondary particle to exhibit excellent orientation, and the degree of aggregation of the primary particles may decrease even after calcination.
As the orientation distance, which is a vertical distance or spacing between the extension line (A) of the oriented particles and the central baseline (C2), is maintained at 1.5 µm or less, the overall orientation of the secondary particles may be further improved. Specifically, the distance between the extension line of the oriented particles and the central baseline may be 0.1 µm to 1.5 µm, or 0.1 µm to 1.2 µm, or 0.1 µm to 1 µm, or 0.1 µm to 0.9 µm, or 0.2 µm to 1.5 µm, or 0.2 µm to 1.2 µm, or 0.1 µm to 1 µm, or 0.1 µm to 0.9 µm, or 0.2 µm to 0.9 µm.
As the positive electrode active material according to an embodiment of the present invention contains a heteroatom and the heteroatom is provided at high concentration at the grain boundary between the primary particles, the heteroatom may reduce the degree of agglomeration of the primary particles in the surface portion of the secondary particle during the calcination process, thereby maintaining the aspect ratio of the primary particles at a higher ratio, and improving the orientation of the primary particles provided in the outermost surface of the secondary particle so that the primary particles are aligned toward the center of the secondary particle.
In addition, the spacing between adjacent particles among the oriented particles, which are primary particles provided in the surface portion of the secondary particle with improved orientation, may be maintained at an approximately constant level, and the occurrence of microcracks and morphological changes of the particles by volumetric changes due to shrinkage and expansion of the primary particles during the charging/discharging process may be prevented. In addition, the positive electrode active material may relieve micro strain in the positive electrode active material even under hard conditions such as high voltage and/or high rate charge and discharge after long-term cycling, and prevent stress accumulation, thereby further improving the performance characteristics of a secondary battery, such as electrochemical properties, safety, and reliability. Here, the morphology of the particles may be expressed by the orientation angle, orientation distance, grain size, aspect ratio, and width of the primary particles.
Specifically, 80% or more of the primary particles distributed in a thickness (T) region ranging from the outermost surface of the secondary particle to a portion corresponding to 40% of the diameter (L) of the secondary particle in a direction toward the center may be oriented particles.
In addition, the thickness (T) ranging from the outermost surface of the secondary particle to a portion corresponding to 40% of the diameter (L) of the secondary particle in a direction toward the center may be 1.5 µm to 4 µm. Specifically, the thickness may be 1.2 µm to 4 µm, or 1.1 µm to 4 µm, or 1 µm to 4 µm, or 1.5 µm to 3.5 µm, or 1.5 µm to 3 µm, or 1.5 µm to 2.5 µm. Alternatively, when the average radius of the secondary particle is 5 µm, the thickness (T) may be 1.25 µm from the outermost surface of the secondary particle.
The oriented particles have a short axis and a long axis, and may include those in which an average aspect ratio which is the ratio of the length of the long axis to the length of the short axis is 2.5 to 15. Specifically, the average aspect ratio of the oriented particles may be 2.5 to 14, or 2.5 to 13, or 2.5 to 12, or 2.7 to 15, or 3 to 15, or 3 to 12.
The average grain size of the oriented particles may be obtained by calculating the square root of the average cross-sectional area of the oriented particles. Specifically, the average grain size may be 0.15 µm to 0.5 µm, or 0.18 µm to 0.5 µm, or 0.2 µm to 0.5 µm.
In general, in the process of preparing the positive electrode active material, it is not easy to make the average grain size of the primary particles 0.5 µm or less, except for a rapid heating method such as the SPS method. When the cathode active material is prepared by the co-precipitation method, the grain size inevitably increases in the process of synthesizing and heat-treating the composite metal hydroxide. In particular, when the composite metal hydroxide is heat-treated at 700° C. or higher, a problem arises in that the average grain size of the primary particles in the prepared cathode active material increases to more than 0.5 µm.
On the other hand, as the positive electrode active material according to this embodiment contains a heteroatom such that the heteroatom is not only simply doped into the primary particle, but also provided in excess at the grain boundary between the primary particles, it is possible to control the grain size of the positive electrode active material to an ultra-fine grain size of 0.5 µm or less even after heat treatment at 700° C. or higher, and accordingly, it is possible to prevent the occurrence of micro-cracks in a nickel-rich positive electrode active material.
For example, the average grain size of the oriented particles is a value obtained by calculating the cross-sectional area based on a TEM image of the positive electrode active material and taking the square root of the calculated value, and indicates the overall shape of the oriented particles. Here, the grain size can be obtained by measuring the cross-sectional area of the oriented particles to be measured using a size measuring program (e.g., ImageJ), and taking the square root of the measured cross-sectional area.
The positive electrode active material according to this embodiment may be prepared by calcining a lithium compound together with a composite metal hydroxide containing at least any one of nickel (Ni), cobalt (Co), manganese (Mn) and aluminum (Al), and the positive electrode active material may be any one or more of NC-based, NCM-based, NCA-based, LNO-based, and NCMA-based positive electrode active materials. For example, the NC-based, NCM-based, NCA-based, and NCMA-based positive electrode active materials are determined by the types of metal elements other than lithium and a heteroatom added as a dopant in the positive electrode active materials, wherein N denotes nickel (Ni), C denotes cobalt (Co), M denotes manganese (Mn), and A denotes aluminum (Al). The NC-based may refer to a positive electrode active material composed of nickel and cobalt without lithium and a heteroatom added as a dopant, the NCM-based may refer to a positive electrode active material composed of nickel, cobalt and manganese, the NCA-based may refer to a positive electrode active material composed of nickel, cobalt and aluminum, and the NCMA-based may refer to a positive electrode active material composed of nickel, cobalt, manganese and aluminum. In addition, the positive electrode active material according to this embodiment may further include an LNO-based positive electrode active material. The LNO-based may refer to a positive electrode active material composed of lithium (Li) and nickel (Ni).
The secondary particles include bulk type particles in which a concentration gradient does not appear throughout the secondary particles, and gradient type particles in which at least one of nickel (Ni), cobalt (Co), manganese (Mn) and aluminum (Al) has a concentration gradient. In addition, the secondary particle may comprise: a core portion which is provided in the central portion of the secondary particle; and a shell portion which is provided to cover the core portion and in which at least one of nickel (Ni), cobalt (Co), manganese (Mn) and aluminum (Al) has a concentration gradient. Specifically, the core portion in the secondary particle may be of bulk type, and the shell portion may be of gradient type.
The positive electrode active material according to this embodiment may be nickel (Ni)-rich, and for example, may contain 60 mol% or more, or 65 mol% or more, or 70 mol% or more, or 75 mol% or more, or 90 mol% or more of nickel. In at least one or more of the primary particles, a compound containing an excess of a heteroatom may be provided at the grain boundary between the primary particles, thereby suppressing the formation of microcracks during charging and discharging of the nickel-rich positive electrode active material.
In the positive electrode active material, the oriented particles may be provided in a rod shape, wherein the rod shape has a long axis and a short axis, the average length of the short axis may be 1.0 µm or less, and the average length of the long axis may be 1.0 µm or more.
Another aspect of the present invention includes a lithium secondary battery including: a positive electrode including the above-described positive electrode active material; a negative electrode facing the positive electrode and comprising graphite or lithium metal; a separator interposed between the positive electrode and the negative electrode; and an electrolyte solution or solid electrolyte containing a lithium salt.
Hereinafter, examples and comparative examples of the present invention will be described. However, the following examples are only preferred examples of the present invention, and the scope of the present invention is not limited by the following examples.
10 liters of distilled water was placed in a co-precipitation reactor (volume: 40 L; rotary motor output: 750 W or more) , and then N2 gas was supplied into the reactor at a rate of 6 liters/minute and stirring was performed at 350 rpm while the temperature of the reactor was maintained at 45° C. Nickel sulfate aqueous solution (NiSO4·6H2O, Samchun Chemicals) and cobalt sulfate aqueous solution (CoSO4·7H2O, Samchun Chemicals) were mixed together in amounts such that the molar ratio between nickel (Ni) and cobalt (Co) was 96:4, thus preparing a 2 M metal solution. The prepared metal solution, a 16 M ammonia solution (NH4OH, JUNSEI) and a 4 M sodium hydroxide solution (NaOH, Samchun Chemicals) were continuously introduced into the reactor at rates of 0.561 liters/hour, 0.11 liters/hour and 0.60 liters/hour, respectively, for 24 hours. While the pH in the reactor was maintained in the range of 10 to 12, a co-precipitation reaction was performed to produce a Ni0.96Co0.04 (OH) 2 composite metal hydroxide.
The produced composite metal hydroxide was filtered, washed several times with distilled water, and then dried in a dry oven at 110° C. for 12 hours to obtain powder. The obtained composite metal hydroxide powder, aluminum hydroxide (Al(OH)3) as a heteroatom, and lithium hydroxide (LiOH) were mixed at the molar ratio shown in Table 1 below, and then pre-calcined by heating at a rate of 2° C./min and then keeping at 450° C. for 5 hours. Next, the mixture was calcined at 700° C. for 10 hours, thus preparing NC-based positive electrode active material powder.
NC-based positive electrode active material powders were prepared in the same manner as in Preparation Example 1, except that the calcination temperatures were 750° C. and 800° C., respectively, as shown in Table 1 below.
NC-based positive electrode active material powder was prepared in the same manner as in Preparation Example 1, except that the Ni0.96Co0.04 (OH) 2 composite metal hydroxide powder produced in Preparation Example 1, titanium oxide (TiO2) as a heteroatom, and lithium hydroxide (LiOH) were mixed together at the molar ratio shown in Table 1 below.
NC-based positive electrode active material powders were prepared in the same manner as in Preparation Example 1, except that the calcination temperatures were 750° C. and 800° C., respectively, as shown in Table 1 below.
NC-based positive electrode active material powder was prepared in the same manner as in Preparation Example 1, except that the Ni0.96Co0.04 (OH) 2 composite metal hydroxide powder produced in Preparation Example 1, tantalum oxide (Ta2O5) as a heteroatom, and lithium hydroxide (LiOH) were mixed together at the molar ratio shown in Table 1 below.
NC-based positive electrode active material powders were prepared in the same manner as in Preparation Example 7, except that the calcination temperatures were 750° C. and 800° C., respectively, as shown in Table 1 below.
NC-based positive electrode active material powder was prepared in the same manner as in Preparation Example 1, except that the Ni0.96Co0.04 (OH) 2 composite metal hydroxide powder produced in Preparation Example 1, antimony trioxide (Sb2O3, [3+]) as a heteroatom, and lithium hydroxide (LiOH) were mixed together at the molar ratio shown in Table 1 below.
NC-based positive electrode active material powders were prepared in the same manner as in Preparation Example 10, except that the calcination temperatures were 750° C. and 800° C., respectively, as shown in Table 1 below.
NC-based positive electrode active material powder was prepared in the same manner as in Preparation Example 1, except that the Ni0.96Co0.04 (OH) 2 composite metal hydroxide powder produced in Preparation Example 1, niobium pentoxide (Nb2O5) as a heteroatom, and lithium hydroxide (LiOH) were mixed together at the molar ratio shown in Table 1 below.
NC-based positive electrode active material powders were prepared in the same manner as in Preparation Example 13, except that the calcination temperatures were 750° C. and 800° C., respectively, as shown in Table 1 below.
NC-based positive electrode active material powder was prepared in the same manner as in Preparation Example 1, except that the Ni0.96Co0.04 (OH) 2 composite metal hydroxide powder produced in Preparation Example 1, tungsten trioxide (WO3) as a heteroatom, and lithium hydroxide (LiOH) were mixed together at the molar ratio shown in Table 1 below.
NC-based positive electrode active material powders were prepared in the same manner as in Preparation Example 17, except that the calcination temperatures were 750° C. and 800° C., respectively, as shown in Table 1 below.
NC-based positive electrode active material powder was prepared in the same manner as in Preparation Example 1, except that the Ni0.96Co0.04 (OH) 2 composite metal hydroxide powder produced in Preparation Example 1, molybdenum trioxide (MoO3) as a heteroatom, and lithium hydroxide (LiOH) were mixed together at the molar ratio shown in Table 1 below.
NC-based positive electrode active material powders were prepared in the same manner as in Preparation Example 19, except that the calcination temperatures were 750° C. and 800° C., respectively, as shown in Table 1 below.
10 liters of distilled water was placed in a co-precipitation reactor (volume: 47 L; rotary motor output: 750 W or more) , and then N2 gas was supplied into the reactor at a rate of 6 liters/minute and stirring was performed at 350 rpm while the temperature of the reactor was maintained at 45° C. A nickel sulfate aqueous solution (NiSO4·6H2O, Samchun Chemicals) and a cobalt sulfate aqueous solution (CoSO4·7H2O, Samchun Chemicals) were mixed together in amounts such that the molar ratio between nickel (Ni) and cobalt (Co) was 90:10, thus preparing a 2 M metal solution. The prepared metal solution, a 16 M ammonia solution (NH4OH, JUNSEI) and a 4 M sodium hydroxide solution (NaOH, Samchun Chemicals) were continuously introduced into the reactor at rates of 0.561 liters/hour, 0.11 liters/hour and 0.60 liters/hour, respectively, for 24 hours. While the pH in the reactor was maintained in the range of 10 to 12, a co-precipitation reaction was performed to produce a Ni0.9Co0.1 (OH) 2 composite metal hydroxide.
The produced composite metal hydroxide was filtered, washed several times with distilled water, and then dried in a dry oven at 110° C. for 12 hours to obtain powder. The obtained composite metal hydroxide powder and lithium hydroxide (LiOH) were mixed at a molar ratio of 1:1.01, and then pre-calcined by heating at a rate of 2° C./min and then keeping at 450° C. for 5 hours. Next, the mixture was calcined at 730° C. for 10 hours, thus preparing NC-based positive electrode active material powder. Conditions for preparing the NC-based positive electrode active material powder are shown in Table 2 below.
NC-based positive electrode active material powder was prepared in the same manner as in Preparation Example 22, except that the Ni0.9Co0.1 (OH) 2 composite metal hydroxide powder prepared in Preparation Example 22, magnesium oxide (MgO) as a heteroatom, and lithium hydroxide (LiOH) were mixed together at the molar ratio shown in Table 2 below.
NC-based positive electrode active material powder was prepared in the same manner as in Preparation Example 22, except that the Ni0.9Co0.1 (OH) 2 composite metal hydroxide powder prepared in Preparation Example 22, aluminum hydroxide (Al(OH)3) as a heteroatom, and lithium hydroxide (LiOH) were mixed together at the molar ratio shown in Table 2 below.
NC-based positive electrode active material powder was prepared in the same manner as in Preparation Example 22, except that the Ni0.9Co0.1 (OH) 2 composite metal hydroxide powder prepared in Preparation Example 22, titanium oxide (TiO2) as a heteroatom, and lithium hydroxide (LiOH) were mixed together at the molar ratio shown in Table 2 below.
NC-based positive electrode active material powder was prepared in the same manner as in Preparation Example 22, except that the Ni0.9Co0.1 (OH) 2 composite metal hydroxide powder prepared in Preparation Example 22, tantalum oxide (Ta2O5) as a heteroatom, and lithium hydroxide (LiOH) were mixed together at the molar ratio shown in Table 2 below.
NC-based positive electrode active material powder was prepared in the same manner as in Preparation Example 22, except that the Ni0.9Co0.1 (OH) 2 composite metal hydroxide powder prepared in Preparation Example 22, antimony trioxide (Sb2O3, [3+]) as a heteroatom, and lithium hydroxide (LiOH) were mixed together at the molar ratio shown in Table 2 below.
NC-based positive electrode active material powder was prepared in the same manner as in Preparation Example 22, except that the Ni0.9Co0.1 (OH) 2 composite metal hydroxide powder prepared in Preparation Example 22, molybdenum trioxide (MoO3) as a heteroatom, and lithium hydroxide (LiOH) were mixed together at the molar ratio shown in Table 2 below.
NC-based positive electrode active material powder was prepared in the same manner as in Preparation Example 22, except that the Ni0.9Co0.1 (OH) 2 composite metal hydroxide powder prepared in Preparation Example 22, boron oxide (B2O3) and aluminum hydroxide (Al(OH)3) as heteroatoms, and lithium hydroxide (LiOH) were mixed together at the molar ratio shown in Table 2 below.
10 liters of distilled water was placed in a co-precipitation reactor (volume: 40 L; rotary motor output: 750 W or more) , and then N2 gas was supplied into the reactor at a rate of 6 liters/minute and stirring was performed at 350 rpm while the temperature of the reactor was maintained at 45° C. A nickel sulfate aqueous solution (NiSO4·6H2O, Samchun Chemicals), a cobalt sulfate aqueous solution (CoSO4·7H2O, Samchun Chemicals) and a manganese sulfate aqueous solution (MnSO4·H2O, Samchun Chemicals) were mixed together in amounts such that the molar ratio between nickel (Ni), cobalt (Co) and manganese (Mn) was 100:0:0, thus preparing a first 2 M metal solution. In addition, these solutions were mixed together in amounts such that the molar ratio between nickel (Ni), cobalt (Co) and manganese (Mn) was 80:10:10, thus preparing a second 2 M metal solution. The prepared first metal solution, a 16 M ammonia solution (NH4OH, JUNSEI) and a 4 M sodium hydroxide solution (NaOH, Samchun Chemicals) were continuously introduced into the reactor at rates of 0.561 liters/hour, 0.08 liters/hour and 0.60 liters/hour, respectively, for 14 hours, thus forming a first constant-concentration portion. Next, the second metal solution was continuously introduced into the first metal solution chamber at a rate of 0.561 liters/hour for 10 hours while constantly changing the concentration of the metal solution introduced into the reactor, thus forming a second concentration gradient portion on the outside of the first constant-concentration portion. Next, addition of the second metal solution to the first metal solution was stopped, and then only the first metal solution having a changed concentration was introduced into the reactor at a rate of 0.561 liters/hour to form a third constant-concentration portion on the outside of the second concentration gradient portion. While the pH in the reactor was maintained in the range of 10 to 12, a co-precipitation reaction was performed to produce a concentration gradient-type composite metal hydroxide having an average composition of Ni0.90CoMn0.05 (OH) 2.
The produced concentration gradient-type Ni0.90Co0.05Mn0.05 (OH) 2 composite metal hydroxide was filtered, washed several times with distilled water, and then dried in a vacuum dryer at 110° C. for 12 hour to obtain powder. The obtained composite metal hydroxide powder and lithium hydroxide (LiOH) were mixed at the molar ratio shown in Table 3 below, and then pre-calcined by heating at a rate of 2° C./min and then keeping at 450° C. for 5 hours. Next, the mixture was calcined at 730° C. for 10 hours, thus preparing NCM-based (gradient NCM type) positive electrode active material powder.
NCM-based positive electrode active material powders were prepared in the same manner as in Preparation Example 30, except that the calcination temperatures were 750° C. and 770° C., respectively, as shown in Table 3 below.
NCM-based positive electrode active material powder was prepared in the same manner as in Preparation Example 30, except that the concentration gradient-type Ni0.90Co0.05Mn0.05 (OH) 2 composite metal hydroxide prepared in Preparation Example 22, antimony trioxide (Sb2O3, [3+]) as a heteroatom, and lithium hydroxide (LiOH) were mixed together at the molar ratio shown in Table 3 below.
NCM-based positive electrode active material powders were prepared in the same manner as in Preparation Example 33, except that the calcination temperatures were 750° C. and 770° C., respectively, as shown in Table 3 below.
NCM-based positive electrode active material powder was prepared in the same manner as in Preparation Example 30, except that the concentration gradient-type composite metal hydroxide powder Ni0.90Co0.05Mn0.05 (OH) 2 prepared in Preparation Example 30, molybdenum trioxide (MoO3) as a heteroatom, and lithium hydroxide (LiOH) were mixed together at the molar ratio shown in Table 3 below.
NCM-based positive electrode active material powders were prepared in the same manner as in Preparation Example 36, except that the calcination temperatures were 750° C. and 770° C., respectively, as shown in Table 3 below.
NCM-based positive electrode active material powder was prepared in the same manner as in Preparation Example 30, except that the concentration gradient-type composite metal hydroxide powder Ni0.90Co0.05Mn0.05 (OH) 2 prepared in Preparation Example 30, tantalum oxide (Ta2O5) as a heteroatom, and lithium hydroxide (LiOH) were mixed together at the molar ratio shown in Table 3 below.
NCM-based positive electrode active material powders were prepared in the same manner as in Preparation Example 39, except that the calcination temperatures were 750° C. and 770° C., respectively, as shown in Table 3 below.
NCM-based positive electrode active material powder was prepared in the same manner as in Preparation Example 30, except that the concentration gradient-type composite metal hydroxide powder Ni0.90Co0.05Mn0.05 (OH) 2 prepared in Preparation Example 30, tantalum oxide (Ta2O5) as a heteroatom, and lithium hydroxide (LiOH) were mixed together at the molar ratio shown in Table 3 below.
NCM-based positive electrode active material powders were prepared in the same manner as in Preparation Example 43, except that the calcination temperatures were 750° C. and 770° C., respectively, as shown in Table 3 below.
NCM-based positive electrode active material powder was prepared in the same manner as in Preparation Example 30, except that the concentration gradient-type composite metal hydroxide powder Ni0.90Co0.05Mn0.05 (OH) 2 prepared in Preparation Example 30, tantalum oxide (Ta2O5) as a heteroatom, and lithium hydroxide (LiOH) were mixed together at the molar ratio shown in Table 3 below.
NCM-based positive electrode active material powders were prepared in the same manner as in Preparation Example 45, except that the calcination temperatures were 750° C. and 770° C., respectively, as shown in Table 3 below.
NCM-based positive electrode active material powder was prepared in the same manner as in Preparation Example 30, except that the concentration gradient-type composite metal hydroxide powder Ni0.90Co0.05Mn0.05 (OH) 2 prepared in Preparation Example 30, niobium pentoxide (Nb2O5) as a heteroatom, and lithium hydroxide (LiOH) were mixed together at the molar ratio shown in Table 3 below.
NCM-based positive electrode active material powders were prepared in the same manner as in Preparation Example 48, except that the calcination temperatures were 750° C. and 770° C., respectively, as shown in Table 3 below.
NCM-based positive electrode active material powder was prepared in the same manner as in Preparation Example 30, except that the concentration gradient-type composite metal hydroxide powder Ni0.90Co0.05Mn0.05 (OH) 2 prepared in Preparation Example 30, niobium pentoxide (Nb2O5) as a heteroatom, and lithium hydroxide (LiOH) were mixed together at the molar ratio shown in Table 3 below.
NCM-based positive electrode active material powders were prepared in the same manner as in Preparation Example 51, except that the calcination temperatures were 750° C. and 770° C., respectively, as shown in Table 3 below.
NCM-based positive electrode active material powder was prepared in the same manner as in Preparation Example 30, except that the concentration gradient-type composite metal hydroxide powder Ni0.90Co0.05Mn0.05 (OH) 2 prepared in Preparation Example 30, niobium pentoxide (Nb2O5) as a heteroatom, and lithium hydroxide (LiOH) were mixed together at the molar ratio shown in Table 3 below.
NCM-based positive electrode active material powders were prepared in the same manner as in Preparation Example 54, except that the calcination temperatures were 750° C. and 770° C., respectively, as shown in Table 3 below.
10 liters of distilled water was placed in a co-precipitation reactor (volume: 47 L; rotary motor output: 750 W or more), and then N2 gas was supplied into the reactor at a rate of 6 liters/minute and stirring was performed at 350 rpm while the temperature of the reactor was maintained at 45° C. A nickel sulfate aqueous solution (NiSO4·6H2O, Samchun Chemicals), a cobalt sulfate aqueous solution (CoSO4·7H2O, Samchun Chemicals) and a manganese sulfate aqueous solution (MnSO4·H2O, Samchun Chemicals) were mixed together in amounts such that the molar ratio between nickel (Ni), cobalt (Co) and manganese (Mn) was 90:5:5, thus preparing a 2 M metal solution. The prepared metal solution, a 16 M ammonia solution (NH4OH, JUNSEI) and a 4 M sodium hydroxide solution (NaOH, Samchun Chemicals) were continuously introduced into the reactor at rates of 0.561 liters/hour, 0.08 liters/hour and 0.60 liters/hour, respectively, for 24 hours. While the pH in the reactor was maintained in the range of 10 to 12, a co-precipitation reaction was performed to produce a Ni0.9Co0.05Mn0.05 (OH) 2 composite metal hydroxide.
The produced Ni0.9Co0.05Mn0.05 (OH) 2 composite metal hydroxide was filtered, washed several times with distilled water, and then dried in a vacuum dryer at 110° C. for 12 hours to obtain powder. The obtained Ni0.9Co0.05Mn0.05 (OH) 2 composite metal hydroxide powder and lithium hydroxide (LiOH) were mixed together at a molar ratio of 1:1.01 and then pre-calcined by heating at a rate of 2° C./min and then keeping at 450° C. for 5 hours. Next, the mixture was calcined at 750° C. for 10 hours, thus preparing NCM-based positive electrode active material powder. Conditions for preparing the NCM-based positive electrode active material powder are shown in Table 4 below.
NCM-based positive electrode active material powder was prepared in the same manner as in Preparation Example 57, except that the Ni0.9Co0.05Mn0.05 (OH) 2 composite metal hydroxide powder prepared in Preparation Example 57, tin oxide (SnO2), and lithium hydroxide (LiOH) were mixed together at the molar ratio shown in Table 4 below.
10 liters of distilled water was placed in a co-precipitation reactor (volume: 47 L; rotary motor output: 750 W or more) , and then N2 gas was supplied into the reactor at a rate of 6 liters/minuteand stirring was performed at 350 rpm while the temperature of the reactor was maintained at 45° C. A nickel sulfate aqueous solution (NiSO4·6H2O, Samchun Chemicals), a cobalt sulfate aqueous solution (CoSO4·7H2O, Samchun Chemicals) and a manganese sulfate aqueous solution (MnSO4·H2O, Samchun Chemicals) were mixed together in amounts such that the molar ratio between nickel (Ni), cobalt (Co) and manganese (Mn) was 90:5:5, thus preparing a 2 M metal solution. The prepared metal solution, a 16 M ammonia solution (NH4OH, JUNSEI) and a 4 M sodium hydroxide solution (NaOH, Samchun Chemicals) were continuously introduced into the reactor at rates of 0.561 liters/hour, 0.08 liters/hour and 0.60 liters/hour, respectively, for 24 hours. While the pH in the reactor was maintained in the range of 10 to 12, a co-precipitation reaction was performed to produce a Ni0.9Co0.05Mn0.05 (OH) 2 composite metal hydroxide.
The produced Ni0.9Co0.05Mn0.05 (OH) 2 composite metal hydroxide was filtered, washed several times with distilled water, and then dried in a vacuum dryer at 110° C. for 12 hours to obtain powder. The obtained Ni0.9Co0.05Mn0.05 (OH) 2 composite metal hydroxide powder and lithium hydroxide (LiOH) were mixed together at a molar ratio of 1:1.01 and then pre-calcined by heating at a rate of 2° C./min and then keeping at 450° C. for 5 hours. Next, the mixture was calcined at 750° C. for 10 hours, thus preparing NCM-based positive electrode active material powder. Conditions for preparing the NCM-based positive electrode active material powder are shown in Table 5 below.
NCM-based positive electrode active material powders were prepared in the same manner as in Preparation Example 59, except that the Ni0.9Co0.05Mn0.05 (OH) 2 composite metal hydroxide powder prepared in Preparation Example 59, niobium pentoxide (Nb2O5) as a heteroatom, and lithium hydroxide (LiOH) were mixed together at the molar ratio shown in Table 5 below such that the concentrations of Nb in the positive electrode active materials were 0.5 mol% (Preparation Example 60) and 1 mol% (Preparation Example 61), respectively.
10 liters of distilled water was placed in a co-precipitation reactor (volume: 47 L; rotary motor output: 750 W or more), and then N2 gas was supplied into the reactor at a rate of 6 liters/minute and stirring was performed at 350 rpm while the temperature of the reactor was maintained at 45° C. A nickel sulfate aqueous solution (NiSO4·6H2O, Samchun Chemicals), a cobalt sulfate aqueous solution (CoSO4·7H2O, Samchun Chemicals) and a manganese sulfate aqueous solution (MnSO4·H2O, Samchun Chemicals) were mixed together in amounts such that the molar ratio between nickel (Ni), cobalt (Co) and manganese (Mn) was 90:5:5, thus preparing a 2 M metal solution. The prepared metal solution, a 16 M ammonia solution (NH4OH, JUNSEI) and a 4 M sodium hydroxide solution (NaOH, Samchun Chemicals) were continuously introduced into the reactor at rates of 0.561 liters/hour, 0.08 liters/hour and 0.60 liters/hour, respectively, for 24 hours. While the pH in the reactor was maintained in the range of 10 to 12, a co-precipitation reaction was performed to produce a Ni0.9Co0.05Mn0.05 (OH) 2 composite metal hydroxide.
The produced Ni0.9Co0.05Mn0.05 (OH) 2 composite metal hydroxide was filtered, washed several times with distilled water, and then dried in a vacuum dryer at 110° C. for 12 hours to obtain powder. The obtained Ni0.9Co0.05Mn0.05 (OH) 2 composite metal hydroxide powder, aluminum hydroxide (Al(OH)3) and lithium hydroxide (LiOH) were mixed together at a molar ratio of 0.995:0.005:1.01 and then pre-calcined by heating at a rate of 2° C./minand then keeping at 450° C. for 5 hours. Next, the mixture was calcined at 750° C. for 10 hours, thus preparing NCMA-based positive electrode active material powder. Conditions for preparing the NCMA-based positive electrode active material powder are shown in Table 5 below.
NCMA-based positive electrode active material powders were prepared in the same manner as in Preparation Example 62, except that the Ni0.9Co0.05Mn0.05 (OH) 2 composite metal hydroxide powder prepared in Preparation Example 62, niobium pentoxide (Nb2O5) as a heteroatom, and lithium hydroxide (LiOH) were mixed together at the molar ratio shown in Table 6 below such that the concentrations of Nb in the positive electrode active materials were 0.5 mol% (Preparation Example 60) and 1 mol% (Preparation Example 61), respectively.
10 liters of distilled water was placed in a co-precipitation reactor (volume: 40 L; rotary motor output: 750 W or more) , and then N2 gas was supplied into the reactor at a rate of 6 liters/minute and stirring was performed at 350 rpm while the temperature of the reactor was maintained at 45° C. Nickel sulfate aqueous solution (NiSO4·6H2O, Samchun Chemicals) was mixed with distilled water to obtain a 2 M metal solution. The obtained metal solution, a 16 M ammonia solution (NH4OH, JUNSEI) and a 4 M sodium hydroxide solution (NaOH, Samchun Chemicals) were continuously introduced into the reactor at rates of 0.067 liters/hour, 0.561 liters/hour and 0.067 liters/hour, respectively, for 24 hours. While the pH in the reactor was maintained in the range of 10 to 12, a co-precipitation reaction was performed to produce a Ni(OH)2 composite metal hydroxide.
The produced composite metal hydroxide was filtered, washed several times with distilled water, and then dried in a dry oven at 110° C. for 12 hours to obtain powder. The obtained Ni(OH)2 composite metal hydroxide powder and lithium hydroxide (LiOH) were mixed at a molar ratio of 1:1.01, and then pre-calcined by heating at a rate of 2° C./min and then keeping at 450° C. for 5 hours. Next, the mixture was calcined at 650° C. for 10 hours, thus preparing LNO-based positive electrode active material powder. Conditions for preparing the LNO-based positive electrode active material powder are shown in Table 7 below.
LNO-based positive electrode active material powder was prepared in the same manner as in Preparation Example 65, except that the Ni(OH)2 composite metal hydroxide powder prepared in Preparation Example 65, antimony trioxide (Sb2O3,[3+]) as a heteroatom, and lithium hydroxide (LiOH) were mixed together at the molar ratio shown in Table 7 below, and the calcination temperature was 700° C.
LNO-based positive electrode active material powders were prepared in the same manner as in Preparation Example 66, except that the calcination temperatures were 730° C. and 750° C., respectively, as shown in Table 7 below.
10 liters of distilled water was placed in a co-precipitation reactor (volume: 47 L; rotary motor output: 750 W or more), and then N2 gas was supplied into the reactor at a rate of 6 liters/minute and stirring was performed at 350 rpm while the temperature of the reactor was maintained at 45° C. A nickel sulfate aqueous solution (NiSO4·6H2O, Samchun Chemicals), a cobalt sulfate aqueous solution (COSO4·7H2O, Samchun Chemicals) and a manganese sulfate aqueous solution (MnSO4·H2O, Samchun Chemicals) were mixed together in amounts such that the molar ratio between nickel (Ni) and cobalt (Co) was 8:1:1, thus preparing a 2 M metal solution. The prepared metal solution, a 16 M ammonia solution (NH4OH, JUNSEI) and a 4 M sodium hydroxide solution (NaOH, Samchun Chemicals) were continuously introduced into the reactor at rates of 0.561 liters/hour, 0.08 liters/hour and 0.60 liters/hour, respectively, for 24 hours. While the pH in the reactor was maintained in the range of 10 to 12, a co-precipitation reaction was performed to produce a Ni0.8Co0.1Mn0.1 (OH)2 composite metal hydroxide.
The produced Ni0.8Co0.1Mn0.1 (OH)2 composite metal hydroxide was filtered, washed several times with distilled water, and then dried in a dry oven at 110° C. for 12 hours to obtain powder. The obtained Ni0.8Co0.1Mn0.1 (OH) 2 composite metal hydroxide powder, and lithium hydroxide (LiOH) were mixed together at a molar ratio of 1:1.01, and then pre-calcined by heating at a rate of 2° C./min and then keeping at 450° C. for 5 hours. Next, the mixture was calcined at 770° C. for 10 hours, thus preparing positive electrode active material powder. Conditions for preparing the positive electrode active material powder are shown in Table 8 below.
Positive electrode active material powders were prepared in the same manner as in Preparation Example 69, except that the Ni0.8Co0.1Mn0.1 (OH) 2 composite metal oxide powder prepared in Preparation Example 69, antimony trioxide (Sb2O3, [3+]) as a heteroatom, and lithium hydroxide (LiOH) were mixed together at the molar ratio shown in Table 8 below, and the calcination temperatures 790° C. and 810° C., respectively.
10 liters of distilled water was placed in a co-precipitation reactor (volume: 40 L; rotary motor output: 750 W or more), and then N2 gas was supplied into the reactor at a rate of 6 liters/minute and stirring was performed at 350 rpm while the temperature of the reactor was maintained at 45° C. A nickel sulfate aqueous solution (NiSO4·6H2O, Samchun Chemicals), a cobalt sulfate aqueous solution (CoSO4·7H2O, Samchun Chemicals) and a manganese sulfate aqueous solution (MnSO4·H2O, Samchun Chemicals) were mixed together in amounts such that the molar ratio between nickel (Ni), cobalt (Co) and manganese (Mn) was 100:0:0, thus preparing a first 2 M metal solution. In addition, these solutions were mixed together in amounts such that the molar ratio between nickel (Ni), cobalt (Co) and manganese (Mn) was 73.5:12.25:14.25, thus preparing a second 2 M metal solution. The prepared first metal solution, a 16 M ammonia solution (NH4OH, JUNSEI) and a 4 M sodium hydroxide solution (NaOH, Samchun Chemicals) were continuously introduced into the reactor at rates of 0.561 liters/hour, 0.08 liters/hour and 0.60 liters/hour, respectively, for 14 hours, thus forming a first constant-concentration portion. Next, the second metal solution was continuously introduced into the first metal solution chamber at a rate of 0.561 liters/hour for 10 hours while constantly changing the concentration of the metal solution introduced into the reactor, thus forming a second concentration gradient portion on the outside of the first constant-concentration portion. Next, addition of the second metal solution to the first metal solution was stopped, and then only the first metal solution having a changed concentration was introduced into the reactor at a rate of 0.561 liters/hour to form a third constant-concentration portion on the outside of the second concentration gradient portion. While the pH in the reactor was maintained in the range of 10 to 12, a co-precipitation reaction was performed to produce a concentration gradient-type composite metal hydroxide having an average composition of Ni0.78Co0.10Mn0.12 (OH) 2.
The produced Ni0.78Co0.10Mn0.12 (OH) 2 composite metal hydroxide was filtered, washed several times with distilled water, and then dried in a vacuum dryer at 110° C. for 12 hour to obtain powder. The obtained composite metal hydroxide powder and lithium hydroxide (LiOH) were mixed at a molar ratio of 1:1.01 as shown in Table 9 below, and then pre-calcined by heating at a rate of 2° C./min and then keeping at 450° C. for 5 hours. Next, the mixture was calcined at 790° C. for 10 hours, thus preparing NCM-based (gradient NCM type) positive electrode active material powder.
Concentration gradient-type NCM-based positive electrode active material was prepared in the same manner as in Preparation Example 72, except that the Ni0.78Co0.10Mn0.12 (OH) 2 composite metal hydroxide powder prepared in Preparation Example 72, antimony trioxide (Sb2O3, [3+]) as a heteroatom, and lithium hydroxide (LiOH) were mixed together at the molar ratio shown in Table 9 below.
Concentration gradient-type NCM-based positive electrode active material was prepared in the same manner as in Preparation Example 73, except that the calcination temperature was 800° C. as shown in Table 9 below.
Half-cells and full-cells were fabricated using the positive electrode active materials according to the above-described Preparation Examples.
To fabricate the half-cells and the full-cells, the powder-type positive electrode active material prepared according to each of the Preparation Examples, poly(vinylidene fluoride) and carbon black at a weight ratio of 90:4.5:5.5 were added into N-methyl pyrrolidone (0.4 g per g of the positive electrode active material) and then uniformly mixed together, thereby preparing positive electrode slurries. An aluminum foil was coated with each of the prepared positive electrode slurries, roll-pressed, and then dried under vacuum, thereby producing positive electrodes.
To fabricate half-cells using the prepared positive electrode active materials, an aluminum foil was coated with each of the prepared positive electrode active material slurries so that the loading level of the positive electrode active material was 5 mg/cm2 (meaning that, when a square of 1 cm2 is sampled from the aluminum foil coated with the positive electrode active material, the weight of only the positive electrode active material in the positive electrode is 5 mg), thereby producing positive electrodes. The electrolyte used was obtained by uniformly dissolving 2 wt% vinylene carbonate (VC) and 1.2 mol/L lithium salt LiPF6 as additives in ethylene carbonate: ethyl methyl carbonate (EC:EMC = 3:7 v/v) as a solvent. As half-cells, 2032-coin type half-cells (hereinafter referred to as coil cells) employing Lio as a negative electrode were fabricated.
To fabricate full-cells using the prepared positive electrode active materials, an aluminum foil was coated with each of the prepared positive electrode active material slurries so that the loading level of the positive electrode active material was 8.5 mg/cm2, thereby producing positive electrodes. In addition, an aluminum foil was coated with a prepared graphite slurry at a loading level of 6.5 mg/cm2, roll-pressed, and then dried under vacuum, thereby producing a negative electrode. The electrolyte used was obtained by uniformly dissolving 2 wt% vinylene carbonate (VC) and 1.2 mol/L lithium salt LiPF6 as additives in ethylene carbonate: ethyl methyl carbonate (EC:EMC = 3:7 v/v) as a solvent. Each of the positive electrodes, a separator (Celgard, model 2320) and the negative electrode were stacked in a pouch-type battery case, and sealed together with the prepared electrolyte, thereby fabricating pouch-type full-cells.
Each of the fabricated half-cells was subjected to a 300-cycle charge/discharge test by charging to 4.3 V and discharging to 2.7 V at a constant current of 0.5 C (1 C: 180 mA/g) at 30° C., and the capacity retentions were measured (hereinafter referred to as 2.7 V-4.3 V).
The fabricated full cells were cycled between 3.0 V (discharge voltage) and 4.2 V (charge voltage) at a constant current of 1 C at 25° C., and the capacities and capacity retentions were measured.
For the positive electrode active materials according to the Preparation Examples and the composite metal hydroxide (precursor) before pre-calcination, the microstructures were analyzed by SEM (Nova Nano SEM 450, FEI).
Hereinafter, the microstructures, surface properties, and electrochemical properties of the positive electrode active materials according to the Preparation Examples will be described.
Referring to
In particular, when aluminum and molybdenum were added in equal amounts (1 mol%), respectively, followed by calcination at 600° C., agglomeration of the primary particles could be observed after calcination.
The precursor (NC96 precursor) is composed of radial preliminary primary particles, wherein the preliminary primary particles have a width of 3 nm to 4 nm (
When aluminum was added to the precursor, followed by calcination at 600° C., agglomeration between the particles occurred. Referring to
On the other hand, it could be confirmed that, in the case of the positive electrode active material to which molybdenum was added, agglomeration between the primary particles did not occur. Specifically, in the positive electrode active material to which molybdenum was added, only a thin primary particle having a width of approximately 46 nm was confirmed, and when it was Fourier transformed, a single line appeared unlike the positive electrode active material to which aluminum was added, which means a single primary particle consisting of a single crystal.
Referring to
The analysis method in
It could be confirmed that, when calcination was performed at a high temperature of 700° C. or higher, the positive electrode active material containing aluminum gradually lost orientation because aluminum does not have the effect of a sintering inhibitor, whereas in the case of the positive electrode active material containing molybdenum, the rod shape of the primary particle was maintained because molybdenum functioned as a sintering inhibitor.
Referring to
Referring to
Referring to
Aluminum is uniformly doped into the primary particles, whereas molybdenum and niobium are doped into the primary particles, and at the same time, compounds containing molybdenum and niobium, respectively, are segregated at the grain boundaries between the primary particles. When the compounds containing molybdenum and niobium, respectively, provided at the grain boundaries between the primary particles at a higher concentration than the inside of the primary particles, can reduce the degree of agglomeration of the primary particles during high-temperature calcination of the precursor composite metal hydroxide, whereby the rod shape of the preliminary primary particles shown in the composite metal hydroxide can be maintained at approximately the same shape even in the calcined positive electrode material. That is, molybdenum or niobium provided at the grain boundary between the primary particles can act as a sintering inhibitor to maintain the shape of the primary particles of the precursor even during high-temperature calcination.
That is, in the positive electrode active material to which aluminum has been added, a compound containing aluminum is not formed at the grain boundary between the primary particles and is uniformly doped only into the primary particles, and thus it does not function as a sintering inhibitor during high-temperature calcination, and the primary particles are agglomerated together to form an equiaxed positive electrode active material. The positive electrode active material to which titanium was added maintained the rod shape after calcination at 700° C., unlike the positive electrode active material containing aluminum, but after calcination at 750° C. and 800° C., the size of the primary particles thereof increased and the aspect ratio decreased. In the case of the positive electrode active materials to which tantalum, antimony and niobium were added, respectively, the rod shape was maintained after calcination at 700° C. and 750° C., but after calcination at 800° C., the size of the primary particles thereof increased and the aspect ratio decreased. It could be confirmed that the positive electrode active materials to which tungsten and molybdenum were added, respectively, maintained the rod shape after calcination at 700° C., 750° C. and 800° C. That is, it could be confirmed that the temperature range in which the rod shape was maintained changed depending on the kind of metal added.
Tables 10 to 12 below show the results of evaluating the capacities of the half-cells fabricated using Preparation Examples 1 to 21 and evaluating the capacity retention after cycles, and Table 13 below shows the results of evaluating full-cells employing graphite as the negative electrode.
Referring to Tables 10 to 12 above and
As described above, the degree of function of the sintering inhibitor was different between the positive electrode active material containing aluminum (a first heteroatom), the positive electrode active material containing titanium (a second heteroatom), the positive electrode active materials containing tantalum, antimony and niobium (a third heteroatom), and the positive electrode active materials containing tungsten and molybdenum (a fourth heteroatom). Thereby, it could be confirmed that the degree of agglomeration of the primary particles provided in the surface portion of the secondary particle in each of the positive electrode active materials was significantly low, and it could be confirmed that the capacity retention characteristics after 100 cycles of charging and discharging also exhibited the same pattern. That is, it could be confirmed that, among the heteroatoms added to the positive electrode active materials, titanium (second heteroatom), tantalum, antimony and niobium (third heteroatom), and tungsten and molybdenum (fourth heteroatom), except for aluminum (first heteroatom), formed compounds containing titanium, tantalum, antimony, niobium, tungsten, and molybdenum, respectively, at the grain boundaries between the primary particles at higher concentrations than inside of the primary particles, and among them, tungsten and molybdenum (fourth heteroatom) had the best sintering inhibitor function during calcination at the highest temperature.
As shown in Table 13 above and
Table 14 below shows the characteristics of the primary particles of the positive electrode active materials to which aluminum and molybdenum were added in equal amounts, when charged to 4.3 V.
Referring to
Referring to Table 14 above and
Referring to
In the case of nickel-rich positive electrode active materials such as NC90, there is a problem in that excessive agglomeration of primary particles generally occurs during high-temperature calcination, resulting in degradation in electrochemical properties and cycle life characteristics. On the other hand, in the embodiment of the present invention, tantalum, antimony, niobium, tungsten and molybdenum, which are the added heteroatoms, form compounds containing tantalum, antimony, niobium, tungsten and molybdenum at the grain boundaries between the primary particles constituting the positive electrode active materials, thereby reducing the degree of agglomeration of the primary particles during calcination of the positive electrode active materials at a high temperature of 700° C. or higher.
That is, in the positive electrode active material containing molybdenum, the molybdenum is provided in the form of a compound at the grain boundary between the primary particles and doped into the primary particles. In this case, the molybdenum is provided at a higher concentration at the grain boundary than inside the primary particles, and thus prevents or reduces the agglomeration of the preliminary primary particles during high-temperature calcination of the precursor composite metal hydroxide. Thus, the rod shape of the preliminary primary particles is maintained almost unchanged even in the primary particles of the positive electrode active material, which is a calcined body, and the structural orientation of the primary particles in the secondary particle constituting the positive electrode active material is improved so that lithium ions can efficiently move reversibly to the central portion of the secondary particle. The primary particles constituting the positive electrode active material containing molybdenum have high particle strength due to enhanced crystallinity, do not morphologically change, and thus undergo shrinkage/expansion with little irreversibility during the charging/discharging process. In addition, the occurrence of micro-strain therein is relieved and stress accumulation therein is reduced. Thus, the positive electrode active material containing molybdenum exhibits excellent cycle life characteristics.
Referring to
Electron diffraction patterns for the [010] zone axis or [100] zone axis can be seen. The electron diffraction patterns show: a first diffraction spot group G1 in which one or more diffraction spots having a first intensity and corresponding to a lattice formed by the lithium layer and transition metal layer stacked adjacent to each other are aligned in one direction; and a second diffraction spot group G2 in which one or more diffraction spots having a second intensity relatively lower than the first intensity of the diffraction spots of the first diffraction group G1 and corresponding to a lattice formed by the first mixed layer and second mixed layer stacked adjacent to each other are aligned in one direction. They show an ordered structure.
The positive electrode active material may prevent the penetration of an electrolyte due to the ordered structure even when microcracks are formed, and may also exhibit excellent characteristics without reduction in capacity due to the ordered structure that has low reactivity with an electrolyte, even when the electrolyte penetrates the positive electrode active material.
Table 15 below shows each Preparation Example depending on calcination temperature. In Table 15, classification 1 shows each Preparation Example, and classification 2 shows the type and content of heteroatom and the type of positive electrode active material in order.
In the following, when the same positive electrode active material and heteroatoms were included, the average values of the widths, aspect ratios, grain sizes, orientation angles and orientation distances of the primary particles provided in the surface portion of the secondary particle with respect to the cross-section of the secondary particle were measured by experiments at different calcination temperatures. The surface portion of the secondary particle refers to a thickness (T) region ranging from the outermost surface of the secondary particle to a portion corresponding to 40% of the diameter (L) in a direction toward the center (see
The orientation angle and orientation distance were measured as shown in
Table 16 below shows the average width of the primary particles located in the surface portion of the secondary particle of the positive electrode active material according to each Preparation Example of the present invention at each calcination temperature. Table 17 below shows the average aspect ratio of the primary particles located in the surface portion of the secondary particle of the positive electrode active material according to each Preparation Example of the present invention at each calcination temperature. Table 18 below shows the average grain size of the primary particles located in the surface portion of the secondary particle of the positive electrode active material according to each Preparation Example of the present invention at each calcination temperature.
Table 16 above and
Referring to Table 17 above and
Referring to Table 18 above and table, which show the grain size of the primary particles provided in the surface portion of the secondary particle according to each Preparation Example, it can be confirmed that, in the case of the positive electrode active materials containing titanium (the second heteroatom) and the positive electrode active materials containing tantalum, antimony and niobium (third heteroatom), except for the positive electrode active material containing aluminum (the first heteroatom), the grain size tended to increase as the calcination temperature increased. On the other hand, it could be confirmed that the grain size in the positive electrode active materials containing tungsten and molybdenum (the fourth heteroatom) was almost constant regardless of the calcination temperature.
As described above, it could be confirmed that, in the case of the positive electrode active material containing aluminum (the first heteroatom), aluminum was not present at the grain boundary between the primary particles and the added aluminum was completely doped into the primary particles. Therefore, when the positive electrode active material containing aluminum is calcined at high temperature, the primary particles are excessively agglomerated, so that the rod shape almost disappears, and thus the primary particles are provided in an approximately equiaxed form. It could be confirmed that, at a calcination temperature of 700° C., the primary particles of the positive electrode active material containing titanium (the second heteroatom) had the rod shape while having as a higher aspect ratio than the positive electrode active material containing aluminum, but at calcination temperatures of 750° C. and 800° C., the primary particles were agglomerated and the rod shape could not be maintained. It could be confirmed that, in the case of the positive electrode active materials containing tantalum, antimony and niobium (the third heteroatom), the rod shape of the primary particle was maintained at 700° C. and 750° C., but could not be maintained at 800° C. It could be confirmed that the rod shape of the primary particles in the positive electrodes containing tungsten and molybdenum (the fourth heteroatom) was maintained at all calcination temperatures of 700° C., 750° C. and 800° C.
Table 19 below shows the average orientation angle in the positive electrode active material containing each heteroatom at each calcination temperature.
Referring to Table 19 above and
Here, it could be confirmed that the aluminum-containing positive electrode active material (the first heteroatom) having the largest average orientation angle showed wide distributions of the average value, maximum value and minimum values of the orientation angles, and the positive electrode active materials containing tungsten and molybdenum (the fourth heteroatom), which have the smallest orientation angle, showed a narrow distribution of the orientation angle even when the calcination temperature increased. In addition, In addition, it could be confirmed that the positive electrode active material containing aluminum (the first heteroatom) and the positive electrode active material containing no heteroatom exhibited similar orientation angle characteristics. That is, it could be confirmed that, even in the case of the positive electrode active material in which the aluminum was distributed like a dopant inside the primary particles, the positive electrode active material exhibited characteristics similar to those of the positive electrode active material containing no heteroatom, suggesting that characteristics such as alignment and shape maintenance of the primary particles during high-temperature calcination are irrelative to doping of the heteroatom and are attributable to the heteroatom provided at the grain boundary between the primary particles at a higher concentration than inside the primary particles.
That is, it could be confirmed that, in the case of the positive electrode active materials containing tungsten and molybdenum (the fourth heteroatom), not only the average value of the orientation angle of the primary particles provided in the surface portion of the secondary particle, but also the overall orientation and alignment of the primary particles were improved and uniformly appeared.
Table 20 below shows the average orientation distance depending on the type of heteroatom and calcination temperature.
It could be confirmed that the orientation distance in the positive electrode active material containing no heteroatom and in the positive electrode active material containing aluminum (the first heteroatom) was about double that in the positive electrode active materials containing tungsten and molybdenum, even at the lowest calcination temperature of 700° C., and the average value and standard deviation of the orientation distances therein increased and decreased as the calcination temperature increased.
It could be confirmed that the orientation angle and orientation distance characteristics almost unchanged depending on the type of heteroatom, and were better in the order of the positive electrode active material containing titanium (the second heteroatom), the positive electrode active materials containing tantalum, antimony and niobium (third heteroatoms), and the positive electrode active materials containing tungsten and molybdenum (the fourth heteroatom), depending on the calcination temperature.
Referring to
It was confirmed through experiments that, when the nickel content in the positive electrode active material according to this embodiment was 96 mol%, 80% or more of the primary particles provided in the surface portion of the secondary particle were oriented particles, and when the width, grain size, aspect ratio, orientation angle and orientation distance of the oriented particles were within the ranges described below, the positive electrode active material exhibited capacity retention of 80% or more after 100 cycles. Average width of the oriented particles: 0.2 µm to 0.5 µm; average grain size: 0.2 µm to 0.5 µm; average aspect ratio: 2 to 5; an average orientation angle: 4° to 10°; and average orientation distance: 0.2 µm to 0.9 µm.
In the process of calcining the positive electrode active material, the primary particles provided in the surface portion of the secondary particle are most affected by the heat of calcination. In addition, in the positive electrode active material, the primary particles provided in the surface portion of the secondary particle are in direct contact with an electrolyte and may function as an inlet through which lithium ions flow into the secondary particle, thereby providing a path for lithium ions. That is, in the case of the positive electrode active material according to this embodiment, the primary particles constituting the secondary particle are doped with a specific heteroatom, and the heteroatom is provided as a compound at the grain boundary between the primary particles at a higher concentration than the inside of the primary particles, thereby reducing the degree of agglomeration of the primary particles even during high-temperature calcination, so that the rod shape which is the shape of the preliminary primary particles of the composite metal hydroxide before calcination can be maintained. In addition, the compound containing an excess of a heteroatom, formed at the grain boundary between the primary particles, is provided on the outer surfaces of the primary particles in a crystalline phase different from that of the primary particles, and thus it may protect the primary particles and, at the same time, stabilize the boundary between adjacent primary particles, whereby the primary particles provided in the surface portion of the secondary particle may be aligned toward the center of the secondary particles and have high orientation.
Referring to
It could be confirmed that the primary particles in the positive electrode active material (Al-NC90) containing aluminum alone had a shape similar to that of the primary particles of the positive electrode active material (B1, Al1-NC90) containing both boron and aluminum, but the rod shape of the primary particles in the positive electrode active material containing both boron and aluminum was maintained. This is because, when aluminum was added alone, the aluminum was uniformly doped only into the primary particles and did not exist at the grain boundaries between the primary particles. In the case of the positive electrode active material containing both boron and aluminum, both the boron and aluminum were doped into the primary particles, and at the same time, the born formed a compound containing the boron at the grain boundary between the primary particles.
Referring to
That is, it could be confirmed that, when the heteroatom was provided at the grain boundary between the primary particles at a higher concentration than the inside of the primary particles, the primary particles maintained the rod shape having a predetermined aspect ratio even in the positive electrode active material calcined at high temperature, and thus the orientation thereof was increased. This is believed to be because the heteroatom-containing compound provided at the grain boundary between the primary particles acted as a sintering inhibitor to prevent agglomeration of the primary particles.
Tables 21 and 22 below show the average width, aspect ratio, grain size, orientation angle and orientation distance values of primary particles provided in the surface portions of secondary particles in NC90 positive electrode active materials containing different heteroatoms.
Referring to Table 21 above and
Referring to
Referring to
That is, it could be confirmed that the average width of the primary particles provided in the surface portion of the secondary particle did differ depending on the type of heteroatom, and was large in the positive electrode active material containing no heteroatom, the positive electrode active material containing magnesium, and the positive electrode active material containing aluminum, and was small in the positive electrode active materials containing tantalum, antimony and molybdenum, respectively, and the positive electrode active material containing titanium showed an intermediate value.
Table 23 shows the results of evaluating the electrochemical characteristics of NC90-based positive electrode active materials containing different types of heteroatoms, and Table 24 below shows the results of evaluating the cycle life characteristics.
Referring to Tables 23 and Table 24 above and
Referring to
Referring to
Table 26 below shows the average width, aspect ratio, grain size, orientation angle, and orientation distance values of primary particles provided in the surface portion of the secondary particle in each of concentration gradient-type NCM-based cathode active materials containing different types of heteroatoms at each calcination temperature.
Referring to Table 25 above and
Referring to
It could be confirmed that, in the case of the positive electrode active material containing no heteroatom (Preparation Examples 30 to 32), the rod shape of the primary particles provided in the surface portion of the secondary particle gradually collapsed as the calcination temperature increased, resulting in deterioration in the performance of the positive electrode active material, whereas the positive electrode active material containing a heteroatom exhibited excellent electrochemical properties while the rod shape was maintained even when the calcination temperature increased. Here, the positive electrode active materials containing 0.5 mol% antimony, 0.5 mol% tantalum, and 1 mol% niobium, respectively, exhibited excellent characteristics at a calcination temperature of 770° C., and the positive electrode active material containing 0.75 mol% molybdenum exhibited excellent characteristics at a calcination temperature of 750° C.
Referring to
It can be confirmed that, in the case of the positive electrode active material containing no heteroatom (Preparation Examples 30 to 32), as the calcination temperature increased, the primary particles provided in the surface portion of the secondary particle lost their rod shape, resulting in deterioration in the electrochemical performance, whereas the positive electrode active materials containing antimony, molybdenum, tantalum and niobium, respectively, which are heteroatoms provided at the grain boundaries between the primary particles at higher concentrations than the inside of the primary particles, exhibited excellent electrochemical performance regardless of the calcination temperature. Regarding the width, the positive electrode active materials containing 0.5 mol% antimony, 0.5 mol% tantalum and 1 mol% niobium, respectively, exhibited excellent characteristics at a calcination temperature of 770° C., and the positive electrode active material containing 0.75 mol% molybdenum exhibited excellent characteristics at a calcination temperature of 750° C.
Referring to
Referring to
Referring to the results for heteroatoms added in different amounts at each calcination temperature, it could be confirmed that 0.5 mol% antimony, 0.5 mol% tantalum, 1.0 mol% niobium, and 0.75 mol% molybdenum exhibited the best electrochemical characteristics. In addition, in the case of the same heteroatom, as the amount of heteroatom added increased, the rod shape of the primary particles provided in the surface portion of the secondary particle was better maintained, which means that the heteroatom more effectively prevents agglomeration of the primary particles during calcination.
Referring to
That is, it could be confirmed that, in the case of the positive electrode active material containing no heteroatom, as the calcination temperature increased, the primary particles provided in the surface portion of the secondary particle lost their rod shape, resulting in deterioration in the electrochemical characteristics, whereas the positive electrode active materials containing antimony, molybdenum, tantalum and niobium, respectively, exhibited excellent electrochemical characteristics while the rod shape of the primary particles provided in the surface portion of the secondary particles was maintained even when the calcination temperature increased.
Referring to
Table 26 below shows the results of measuring the electrochemical characteristics of concentration gradient type NCM-based positive electrode active materials containing no heteroatom or containing different types of heteroatoms, at each calcination temperature.
Referring to Table 26 above and
Table 27 shows the results of measuring the changes in nickel concentration in concentration gradient type NCM-based positive electrode active material depending on calcination temperature.
Referring to Table 27 above and
In addition, as shown in
Table 28 below the results of measuring the electrochemical characteristics of a NCM 90-based positive electrode active material containing or not containing 0.3 mol% tin.
Referring to Table 28 above and
Table 29 below shows the results of measuring the electrochemical characteristics of NCM90-based positive electrode active materials containing niobium as a heteroatom.
Referring to Table 29 above and
Table 30 below shows the results of measuring the electrochemical characteristics of NCMA89-based positive electrode active materials containing niobium as a heteroatom.
Referring to Table 30 above and
Table 31 below shows the results of measuring the electrochemical characteristics of LNO-based positive electrode active materials containing antimony as a heteroatom.
When comparing Preparation Example 65 and Preparation Example 66, it could be confirmed that the capacity retention characteristics after 100 cycles were excellent in the positive electrode active material containing 0.7 mol% antimony. In addition, it could be confirmed that, in the case of the positive electrode active material containing 0.7 mol% antimony, the capacity retention characteristics after 100 cycles were maintained almost unchanged even when the calcination temperature increased. Even in the case of the LNO-based positive electrode active material, a compound containing an excess of antimony may be provided at the grain boundary between the primary particles, and can maintain the rod shape of the primary particles during calcination, thereby improving electrochemical characteristics.
Table 32 below shows the results of measuring the electrochemical properties of NCM811-based positive electrode active materials containing antimony as a heteroatom.
Referring to Tables 32 above and
Table 33 below shows the results of measuring the electrochemical characteristics of concentration gradient type NCM78-based positive electrode active materials containing antimony as a heteroatom.
It could be confirmed that the electrochemical characteristics of the positive electrode active material containing antimony were improved even when the calcination temperature increased. This is believed to be because antimony formed a compound at the grain boundary between the primary particles provided in the surface portion of the secondary particle of the positive electrode active material at a higher concentration than inside the primary particles.
Although the present invention has been described above in detail with reference to preferred embodiments, the scope of the present invention is not limited to specific embodiments, and should be defined by the appended claims. In addition, those skilled in the art will understand that many modifications and variations are possible without departing from the scope of the present invention.
Number | Date | Country | Kind |
---|---|---|---|
10-2020-0021604 | Feb 2020 | KR | national |
10-2020-0093548 | Jul 2020 | KR | national |
10-2021-0021976 | Feb 2021 | KR | national |
Filing Document | Filing Date | Country | Kind |
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PCT/KR2021/002141 | 2/19/2021 | WO |