This application claims priority to and the benefit of Korean Patent Application No. 10-2020-0142522, filed on Oct. 29, 2020, in the Korean Intellectual Property Office, the entire content of which is incorporated herein by reference.
One or more aspects of embodiments of the present disclosure relate to a nickel (Ni)-based active material precursor for a lithium secondary battery, a preparing (preparation) method thereof, a Ni-based active material for a lithium secondary battery formed thereof, and a lithium secondary battery including a positive electrode including the nickel-based active material.
With the development of portable electronic devices, communication devices, and/or the like, there is a great need for the development of lithium secondary batteries having high energy density. However, a lithium secondary battery having high energy density may have poor safety, and thus there is a need to improve safety. As a positive active material of lithium secondary batteries, a lithium-nickel-manganese-cobalt composite oxide, a lithium-cobalt oxide, and/or the like has been used. However, when such a positive active material is used, the travel distance of lithium ions during charging and discharging is determined by the size (e.g., diameter) of secondary particles, and the charging and discharging efficiency of such materials may be insufficient (e.g., not high enough) due to such physical distance. Furthermore, the lithium secondary battery may have a decreased lifespan, an increased resistance, and/or unsatisfactory capacity characteristics due to cracks occurring in the primary particles after repeated charging and discharging of the lithium secondary battery. Therefore, improvement in these characteristics is desired.
One or more aspects of embodiments of the present disclosure are directed toward a novel nickel (Ni)-based active material precursor for a lithium secondary battery.
One or more aspects of embodiments of the present disclosure are directed toward a method of preparing the Ni-based active material precursor.
One or more aspects of embodiments of the present disclosure are directed toward a lithium secondary battery having improved lifespan characteristics by including a Ni-based active material obtained from the Ni-based active material precursor, and a positive electrode including the same.
Additional aspects will be set forth in part in the description that follows and, in part, will be apparent from the description, or may be learned by practice of the presented embodiments of the disclosure.
One or more embodiments of the present disclosure provide a nickel (Ni)-based active material precursor for a lithium secondary battery including a secondary particle including a plurality of particulate structures, wherein each of the plurality of particulate structures includes a porous core portion and a shell portion including primary particles radially arranged on the porous core portion; phosphorus (P) is present in the porous core portion, between the plurality of primary particles, and on the surface of the secondary particle; and the content of the phosphorus is in a range of 0.01 wt % to 2 wt % based on a total weight of the Ni-based active material precursor.
One or more embodiments of the present disclosure provide a method of preparing the nickel (Ni)-based active material precursor includes: a first act of supplying a feedstock at a first feed rate and stirring the feedstock to form a precursor seed; a second act of supplying the feedstock to the precursor seed formed in the first act at a second feed rate and stirring the feedstock to grow the precursor seed; a third act of supplying the feedstock to the precursor seed grown in the second act at a third feed rate and stirring the feedstock to adjust the growth of the precursor seed; and acts of washing a product obtained in the third act to obtain a preliminary Ni-based active material precursor, and supplying an ionizable phosphorus compound to the preliminary Ni-based active material precursor to obtaining a phosphorus-containing Ni-based active material precursor, wherein the feedstock includes a complexing agent, a pH adjusting agent, and a metal raw material for forming the nickel-based active material precursor, and the second feed rate of the metal raw material for forming the nickel-based active material precursor is greater than the first feed rate, and the third feed rate is greater than the second feed rate.
One or more embodiments of the present disclosure provide a nickel (Ni)-based active material for a lithium secondary battery including a secondary particle including a plurality of particulate structures, wherein each of the plurality of particulate structures includes: a porous core portion; and a shell portion including primary particles radially arranged on the porous core portion, and where lithium phosphate is present in the porous core portion, between the plurality of primary particles, and on the surface of the secondary particle.
One or more embodiments of the present disclosure provide a lithium secondary battery including a positive electrode including the Ni-based active material for a lithium secondary battery.
The above and other aspects, features, and advantages of certain embodiments of the disclosure will be more apparent from the following description taken in conjunction with the accompanying drawings, in which:
Reference will now be made in more detail to embodiments, examples of which are illustrated in the accompanying drawings, wherein like reference numerals refer to like elements throughout, and duplicative descriptions thereof may not be provided. In this regard, the present embodiments may have different forms and should not be construed as being limited to the descriptions set forth herein. Accordingly, the embodiments are merely described below, by referring to the drawings, to explain aspects of the present description. As used herein, the term “and/or” includes any and all combinations of one or more of the associated listed items. Expressions such as “at least one of,” “one of,” and “selected from,” when preceding a list of elements, modify the entire list of elements and do not modify the individual elements of the list.
It will be further understood that the terms “includes,” “including,” “comprises,” and/or “comprising,” when used in this specification, specify the presence of stated features, acts, steps, operations, elements, and/or components, but do not preclude the presence or addition of one or more other features, acts, steps, operations, elements, components, and/or groups thereof. Further, the use of “may” when describing embodiments of the present disclosure refers to “one or more embodiments of the present disclosure”.
Hereinafter, a nickel (Ni)-based active material precursor for a lithium secondary battery, a preparing (e.g. preparation) method thereof, a Ni-based active material obtained therefrom, and a lithium secondary battery including a positive electrode including the same will be described in more detail. Accordingly, it should be apparent to those skilled in the art that the following description of various embodiments of the present disclosure is provided for illustration purposes only, and not for the purpose of limiting the present disclosure as defined by the appended claims and their equivalents.
In the drawings, elements may be enlarged or exaggerated for clarity. The aforementioned descriptions are only for illustrative purposes, and it will be apparent that those skilled in the art can make various modifications thereto. In addition, in layered structures described below, when a layer is referred to as being “on” another layer, it can be directly on the other element or intervening elements may be present therebetween. When an element is referred to as being “directly on,” another element, there are no intervening elements present.
Provided is a nickel (Ni)-based active material precursor for a lithium secondary battery including a secondary particle including a plurality of particulate structures, wherein each of the plurality of particulate structures includes a porous core portion and a shell portion including primary particles radially arranged on the porous core portion; and phosphorus (P) is present in the porous core portion, between the plurality of primary particles, and on the surface of the secondary particle, wherein the content of phosphorus is in a range of 0.01 wt % to 2 wt % based on a total weight of the Ni-based active material precursor. In this regard, the surface of the secondary particle includes surfaces of the plurality of primary particles.
When the content of phosphorus is less than 0.01 wt % based on the total weight of the Ni-based active material precursor, improvement of electrochemical characteristics may be insignificant. When the content of phosphorus is greater than 2 wt %, the charge/discharge capacity of the material may considerably decrease.
As used herein, the term “phosphorus (P)” is interpreted to indicate phosphorus itself, or to include PO32−, PO43−, or any combination thereof.
As used herein, the terms “between the plurality of primary particles” and “between the plurality of primary particles of the shell portion” may include and/or refer to grain boundaries of the plurality of primary particles.
As used herein, the term “particulate structure” refers to a structure formed by the aggregation of a plurality of primary particles.
As used herein, the term “radially arranged” refers to a shape, arrangement, or orientation in which the major axes of primary particles included in the shell portion are arranged in a normal direction (e.g., perpendicular) to the surface of the particulate structure, or in (along) a direction inclined from the normal direction by an angle of ±30° or less, for example as shown in
Forming a coating film utilizing lithium phosphate has been attempted to improve lifespan characteristics of a Ni-based active material.
However, in related art methods of forming a coating film, the coating film is formed only on the surface (e.g., outermost surface or shell) of the secondary particle of the Ni-based active material, and thus lifespan characteristics are not satisfactorily improved, or a deposition device may be required, thereby increasing manufacturing costs and/or limiting mass production.
However, embodiments of the present disclosure provide a Ni-based active material precursor that is mass-produced with reduced manufacturing costs and substantially uniform coating of phosphorus on the surfaces of and between a plurality of primary particles included in the Ni-based active material, as well as a Ni-based active material obtained therefrom. The Ni-based active material is a product obtained from the above-described Ni-based active material precursor, for example by mixing the Ni-based active material precursor and a lithium precursor, and heat-treating the mixture. The Ni-based active material is coated with lithium phosphate instead of phosphorus when compared with the Ni-based active material precursor.
The Ni-based active material precursor according to the present disclosure has a porous structure, in which primary particles are radially arranged for easy intercalation and deintercalation of lithium. The Ni-based active material precursor includes the porous core portion having pores and the shell portion having a radial arrangement structure. When an ionizable phosphorus compound is provided thereto, phosphorus may be well coated in the porous core portion and between the plurality of primary particles (e.g., at, in, and/or along one or more grain boundaries of the plurality of primary particles) of the shell portion of the Ni-based active material precursor. Also, phosphorus may be present on the secondary particle of the Ni-based active material in the form of a coating film. In this regard, the coating film may be a substantially continuous or discontinuous coating film.
In preparation of the Ni-based active material precursor including phosphorus, an act (process) of providing an ionizable phosphorus compound to a preliminary Ni-based active material precursor is performed. This process may be performed by a wet process using the preliminary Ni-based active material precursor and the ionizable phosphorus compound. This process provides a mixture (e.g., solution, partial solution, or suspension) of the ionizable phosphorus compound and (e.g., in) a solvent to the preliminary Ni-based active material precursor. The preliminary Ni-based active material precursor is impregnated with the mixture of the ionizable phosphorus compound and the solvent and then dried. Through this process using the mixture of the ionizable phosphorus compound and the solvent, phosphorus (P) may be adsorbed on (and/or in some embodiments absorbed in) the porous core portion, the shell portion, and/or the surface of the secondary particle of the precursor, thereby providing the Ni-based active material precursor containing phosphorus. In this case, phosphorus may refer to PO32−, PO43− or any combination thereof (e.g., the term “phosphorus” may in some embodiments refer to a compound or ion including phosphorus atoms).
The impregnation may be performed at a temperature of 20° C. to 40° C., and the drying may be performed at a temperature of 150° C. to 200° C.
When a solid-phase reaction is used in the above-described process of providing the ionizable phosphorus compound to the preliminary Ni-based active material precursor, it is difficult to introduce lithium phosphate into the porous core portion, compared to the above-described wet process.
In the mixture of the ionizable phosphorus compound and the solvent, the concentration of the phosphorus compound may be in a range of 0.02 M to 0.25 M. When the concentration of the ionizable phosphorus compound is within the above range, phosphorus may be well-adsorbed and coated on the surface of the Ni-based active material precursor and therein along the pores without substantial impurities, thereby obtaining a Ni-based active material having excellent lifespan characteristics.
The ionizable phosphorus-containing compound may be, for example, H3PO4, NH3PO4, NH4HPO4, NH4H2PO4, or any combination thereof. The content of the ionizable phosphorus-containing compound may be stoichiometrically adjusted as suitable to finally obtain the Ni-based active material precursor and the Ni-based active material. As used herein, the term “preliminary Ni-based active material precursor” refers to a resultant obtained by washing a product produced using metal raw materials for forming a Ni-based active material precursor (e.g., as described herein in connection with first to third acts of growing a precursor seed). As used herein, the term “phosphorus-containing Ni-based active material precursor” refer to a resultant obtained by providing or supplying the mixture of the ionizable phosphorus compound and the solvent to the preliminary Ni-based active material precursor, as described above. The term “Ni-based active material precursor” may be used to refer to one or both of the above, and may be further understood from context.
The solvent may be or include water, an alcohol (such as ethanol, methanol, and/or isopropanol), or any combination thereof.
In the preparation of the phosphorus-containing Ni-based active material precursor, an ionizable phosphorus compound may be used as a phosphorus source. When a phosphorus compound that is difficult to ionize, such as aluminum phosphate and tungsten phosphate, is used, it may be difficult to obtain a Ni-based active material precursor having a desired or suitable structure.
The Ni-based active material precursor and the Ni-based active material obtained therefrom have multi-center spherical (e.g., substantially spherical) shapes, in which primary particles located at the outer periphery and constituting a secondary particle are radially arranged, and the core portions thereof have pores. Thus, phosphorus (P) is coated on grain boundaries of the primary particles through (e.g., delivered by way of) multiple pores formed from (e.g., in) the Ni-based active material precursor.
In the Ni-based active material precursor according to an embodiment, the content of phosphorus may be selected to hardly affect (e.g., substantially not affect) the porosity of the Ni-based active material precursor. For example, the content of phosphorus may be about 0.01 wt % to about 2 wt %, about 0.01 wt % to about 1.5 wt %, about 0.01 wt % to about 1 wt %, about 0.01 wt % to about 0.5 wt %, about 0.01 wt % to about 0.3 wt %, about 0.01 wt % to about 0.2 wt %, or about 0.01 wt % to 0.1 wt % based on the total weight of the Ni-based active material precursor. In this regard, the term “the total weight of the Ni-based active material precursor” refers to a total weight of the Ni-based active precursor material including phosphorus (e.g., the phosphorus-containing Ni-based active material precursor).
When the content of phosphorus is within the above range, a lithium secondary battery using the Ni-based active material obtained from the Ni-based active material precursor may have improved lifespan characteristics, enhanced high-rate characteristics, and/or reduced gas generation. The content of phosphorus in the Ni-based active material precursor may be confirmed or analyzed by inductively coupled plasma (ICP) analysis.
In the Ni-based active material precursor for a lithium secondary battery according to an embodiment, lithium phosphate may be present in the form of a coating film on the surface of the secondary particle. The thickness of the coating film may be 1 μm or less, for example, 500 nm or less, about 5 nm to about 300 nm, about 8 nm to about 200 nm, or for example, about 10 nm to about 50 nm. When the thickness of the coating film is within the ranges above, gas generation may be efficiently inhibited or decreased after repeated charging and discharging, lithium may be easily diffused in the interface between a positive active material and an electrolyte, and lithium may be easily diffused into the active material.
Referring to
A according to an embodiment is a product obtained from the Ni-based active material precursor of
A Ni-based active material for a lithium secondary battery according to an embodiment of the present disclosure includes a secondary particle including a plurality of particulate structures, wherein each of the particulate structures includes a porous core portion and a shell portion including primary particles radially arranged on the porous core portion, and lithium phosphate is present in the porous core portion, between the plurality of primary particles of the shell portion, and/or on the surface of the secondary particle.
In the Ni-based active material precursor (e.g., the phosphorus-containing Ni-based active material precursor) according to an embodiment, a ratio of a phosphorus peak intensity in the inner portion to that in the outer portion (obtained as described next) may be 1:2 to 1:4. In the Ni-based active material precursor, the phosphorus peak intensities in the porous core portion and the outer portion, and the ratio thereof, may be identified by time-of-flight secondary ion mass spectrometry (TOF-SIMS) analysis using intensity differences of PO3 peaks in each region.
In the Ni-based active material precursor according to another embodiment, the ratio of phosphorus peak intensity in the inner portion to that in the outer portion may be, for example, in the range of 1:2.1 to 1:3.8, 1:2.3 to 1:3.7, 1:2.4 to 1:3.6, or 1:2.5 to 1:3.5. Here, the inner portion includes the porous core portion and spaces between the plurality of primary particles of the shell portion, and the outer portion refers to the surface of the secondary particle.
In the Ni-based active material according to an embodiment, the ratio of phosphorus (P) peak intensity of the inner portion (porous core portion and shell portion) to that of the outer portion (shell portion and surface of secondary particle) may be in the range of 1:2 to 1:4, 1:2.1 to 1:3.8, 1:2.3 to 1:3.7, or 1:2.5 to 1:3.5, as the above-described Ni-based active material precursor.
A Ni-based active material precursor for a lithium secondary battery according to an embodiment includes a secondary particle including a plurality of particulate structures, wherein each of the particulate structures includes a porous core portion and a shell portion including primary particles radially arranged on the porous core portion, and in 50% or more of the primary particles constituting the surface (e.g., the shell or outermost shell) of the secondary particle, the major axes of the primary particles are arranged in the normal direction of (e.g., arranged along a direction substantially normal or perpendicular to) the surface of the secondary particle.
Referring to
Referring to
Referring to
Referring to
Referring to
Referring to
Referring to
Further, referring to
Referring to
Referring to
As used herein, the term “particle size” refers to an average particle diameter in the case of spherical particles, and refers to an average major axis length in the case of non-spherical particles. The particle size may be measured using a particle size analyzer (PSA).
As used herein, the term “pore size” refers to an average pore diameter or an opening width in the case of spherical or circular pores. The term “pore size” refers to an average major axis length in the case of non-spherical or non-circular pores such as elliptical pores.
Referring to
Referring to
In an example of the particulate structure 100, the porous core portion 10 may have closed pores, and the shell portion 20 may have closed pores and/or open pores. The closed pores may exclude electrolyte, whereas the open pores may allow the electrolyte to be contained in the pores of the particulate structure 100. Further, the porous core portion of the particulate structure 100 may have irregular pores. The core portion 10 having irregular pores, like the shell portion 20, may include plate particles, and the plate particles of the core portion 10, unlike the plate particles of the shell portion 20, may be arranged without regularity.
As used herein, the term “irregular pores” refer to pores that are not regular in pore size and pore shape and do not have uniformity. The core portion including irregular pores, unlike the shell portion, may include amorphous particles, and the amorphous particles are arranged without regularity, unlike the shell portion.
The Ni-based active material precursor may be a compound represented by Formula 1:
Ni1-x-y-zCoxMnyMz(OH)2. Formula 1
In the Formula 1, M may be an element selected from boron (B), magnesium (Mg), calcium (Ca), strontium (Sr), barium (Ba), titanium (Ti), vanadium (V), chromium (Cr), iron (Fe), copper (Cu), and zirconium (Zr), and
0.3≤(1-x-y-z)<1, 0<x<1, 0≤y<1, and 0≤z<1 are satisfied.
As described above, in the nickel-based active material precursor of Formula 1, the content of nickel is higher than the content of cobalt, and the content of nickel is higher than the content of manganese. In Formula 1, 0<x≤1/3 may be satisfied, and 0≤y≤0.5, 0≤z≤0.05, and 1/3≤(1-x-y-z)≤0.98 may be satisfied.
According to an embodiment, in Formula 1, x may be about 0.1 to about 0.3, y may be about 0.05 to about 0.3, and z may be 0.
In Formula 1, the content of Ni of the Ni-based active material precursor may be about 30 mol % to about 98 mol %, about 70 mol % to about 96 mol %, or about 85 mol % to 95 mol %.
The Ni-based active material precursor may be, for example, Ni0.92Co0.05Al0.03(OH)2, Ni0.94Co0.03Al0.03(OH)2, Ni0.88Co0.06Al0.06(OH)2, Ni0.96Co0.02Al0.02(OH)2, Ni0.93Co0.04Al0.03(OH)2, Ni0.8Co0.15Al0.05O2(OH)2, Ni0.75Co0.20Al0.05(OH)2, Ni0.92Co0.05Mn0.03(OH)2, Ni0.94Co0.03Mn0.03(OH)2, Ni0.88Co0.06Mn0.06(OH)2, Ni0.96Co0.02Mn0.02(OH)2, Ni0.93Co0.04Mn0.03(OH)2, Ni0.8Co0.15Mn0.05O2(OH)2, Ni0.75Co0.20Mn0.05(OH)2 Ni0.6Co0.2Mn0.2(OH)2, Ni0.7Co0.15Mn0.15(OH)2, Ni0.7Co0.1Mn0.2(OH)2, Ni0.5Co0.2Mn0.3(OH)2, Ni1/3Co1/3Mn1/3(OH)2, Ni0.8Co0.1Mn0.1(OH)2, Ni0.85Co0.1Al0.05(OH)2, Ni0.7Co0.15Mn0.15(OH)2, Ni0.7Co0.1Mn0.2(OH)2, Ni0.5Co0.2Mn0.3(OH)2, Ni1/3Co1/3Mn1/3(OH)2, Ni0.8Co0.1Mn0.1(OH)2, and/or Ni0.85Co0.1Al0.05(OH)2.
A method of preparing a Ni-based active material precursor according to another embodiment includes: a first act of supplying a feedstock at a first feed rate and stirring the feedstock to form a precursor seed; a second act of supplying the feedstock to the precursor seed formed in the first act at a second feed rate and stirring the feedstock to grow the precursor seed; and a third act of supplying the feedstock to the precursor seed grown in the second act at a third feed rate and stirring the feedstock to adjust the growth of the precursor seed, wherein the feedstock includes a complexing agent, a pH adjusting agent, and a metal raw material for forming the nickel-based active material precursor, and the second feed rate of the metal raw material for forming the nickel-based active material precursor is greater than the first feed rate, and the third feed rate is greater than the second feed rate.
A nickel-based active material precursor having the aforementioned new structure may be obtained by sequentially increasing the feed rate of the metal raw material in the order of the first act, the second act, and the third act. In the first act, the second act, and the third act, the reaction temperature may be in a range of about 40° C. to about 60° C., the stirring power may be in a range of about 0.5 kW/m3 to about 6.0 kW/m3, the pH may be in a range of about 10 to about 12, and the content of the complexing agent in the reaction mixture may be in a range of about 0.2 M to about 0.8 M, for example, about 0.4 M to about 0.6 M. In the above ranges, a nickel-based active material precursor that more closely matches the aforementioned structure may be obtained.
In the first act, the precursor seed may be formed and grown by adjusting the pH while supplying the metal raw material and the complexing agent to a reactor including an aqueous solution containing the complexing agent and the pH adjusting agent and having an adjusted pH at a set or predetermined feed rate. In the first act, the growth rate of precursor particles may be about 0.32 μm/hr±about 0.05 μm/hr. In the first act, the stirring power of the reaction mixture may be about 4 kW/m3 to about 6 kW/m3, for example 5.0 kW/m3, and the pH may be about 11 to about 12. For example, in the first act, the feed rate of the metal raw material may be about 1.0 L/hr to about 10.0 L/hr, for example, 5.1 L/hr, and the feed rate of the complexing agent may be about 0.3 times to about 0.6 times, for example, 0.45 times the molar feed rate of the metal raw material. The temperature of the reaction mixture may be about 40° C. to about 60° C., for example, 50° C., and the pH of the reaction mixture is about 11.20 to about 11.70, for example about 11.3 to about 11.5.
In the second act, the precursor seed formed in the first act is grown by changing the reaction conditions. The growth rate of the precursor seed in the second act may be equal to the growth rate of the precursor seed in the first act or may be increased by 20% or more. The feed rate of the metal raw material in the second act may be 1.1 times or more, for example, about 1.1 times to about 1.5 times as compared with the feed rate of the metal raw material in the first act, and the concentration of the complexing agent in the reaction mixture may be increased by 0.05 M or more, for example, about 0.05 M to about 0.15 M based on the concentration of the complexing agent in the first act. In the second act, the stirring power of the reaction mixture may be equal to or more than 1 kW/m2 and less than 4 kW/m2, for example, 3 kW/m2, and the pH thereof may be about 10.5 to about 11. An average particle diameter D50 of the precursor particles obtained in the second act may be about 9 μm to about 12 μm, for example, about 10 μm.
In the third act, the growth rate of the precursor seed may be adjusted to suitably obtain a nickel-based active material precursor for a lithium secondary battery. When the average particle diameter D50 of the precursor particles in the second act reaches about 9 μm to about 12 μm, for example, about 10 μm, the third act proceeds (e.g., may be initiated). The growth rate of the precursor particles in the third act may be increased by twice or more, for example, three times or more, as compared with the growth rate of the precursor particles in the second act. For this purpose, a part of the reaction product contained in the reactor after the second act may be removed to dilute the concentration of the reaction product in the reactor. The product removed from the reactor may be used in another reactor. The feed rate of the metal raw material in the third act may be 1.1 times or more, for example, about 1.1 times to about 1.5 times as compared with the feed rate of the metal raw material in the second act, and the concentration of the complexing agent in the reaction mixture may be increased by 0.05 M or more, for example, about 0.05 M to about 0.15 M based on the concentration of the complexing agent in the second act. In the third act, a precipitate rapidly grows to obtain a nickel-based active material precursor. The stirring power of the reaction mixture in the third act may be 0.5 kW/m2 or more and less than 1 kW/m2, for example, 0.8 kW/m2, and the pH thereof may be about 10 to about 10.5.
In the method of preparing the precursor, the feed rate of the metal raw material may be sequentially increased in the order of the first act, the second act, and the third act. For example, the feed rate of the metal raw material in the second act may be increased by about 10% to about 50% based on the feed rate of the metal raw material in the first act, and the feed rate of the metal raw material in the third act may be increased by about 10% to about 50% based on the feed rate of the metal raw material in the second act. As such, the feed rate of the metal raw material may be gradually increased to thereby suitably obtain a nickel-based active material precursor that more closely matches the aforementioned structure.
In the method of preparing the precursor, the stirring speed of the reaction mixture in the reactor may be sequentially decreased in the order of the first act, the second act, and the third act. As such, the stirring speed of the reaction mixture may be gradually decreased, thereby obtaining a nickel-based active material precursor that more closely matches the aforementioned structure.
In the method of preparing the precursor, the stirring power (e.g., stirring speed) of the reaction mixture in the reactor may be sequentially decreased in the order of the first act, the second act, and the third act. The stirring power in the first act may be about 4 kW/m2 to about 6 kW/m2, the stirring power in the second act may be about 1 kW/m2 to about 4 kW/m2, and the stirring power in the third act may be about 0.5 kW/m2 to about 1 kW/m2. As such, the stirring power of the reaction mixture may be gradually decreased, thereby obtaining a nickel-based active material precursor that more closely matches the aforementioned structure.
In the method of preparing the precursor, the pH of the reaction mixture in the reactor may be sequentially decreased in the order of the first act, the second act, and the third act. For example, the pH of the reaction mixture in the first act, the second act, and the third act may be in (e.g., span) a range of about 10.10 to about 11.50 when the reaction temperature is 50° C. For example, the pH of the reaction mixture in the third act may be lower than the pH of the reaction mixture in the first act at a reaction temperature of 50° C. by about 1.1 to about 1.6, or about 1.2 to about 1.5. For example, the pH of the reaction mixture in the second act may be lower than the pH of the reaction mixture in the first act by about 0.55 to about 0.85 at a reaction temperature of 50° C., and the pH of the reaction mixture in the third act may be lower than the pH of the reaction mixture in the second act by about 0.35 to about 0.55 at a reaction temperature of 50° C. As such, the pH of the reaction mixture may be gradually decreased, thereby obtaining a nickel-based active material precursor that more closely matches the aforementioned structure.
In the method of preparing the precursor, the concentration of the complexing agent included in the reaction mixture in the second act may be increased as compared with the concentration of the complexing agent included in the reaction mixture in the first act, and the concentration of the complexing agent included in the reaction mixture in the third act may be increased as compared with the concentration of the complexing agent included in the reaction temperature in the second act.
The feed rate of the metal raw material for growing the nickel-based active material precursor particles to control the growth rate of the precursor particles in the second act may be increased by about 15% to about 35%, for example, about 25%, as compared with the feed rate thereof in the first act, and the feed rate thereof in the third act may be increased by about 20% to about 35%, for example, about 33%, as compared with the feed rate thereof in the second act. Further, the feed rate of aqueous ammonia in the second act may be increased by about 10% to about 30%, for example, about 20%, based on the feed rate of aqueous ammonia in the first act to increase the density of particles.
Considering the composition of the nickel-based active material precursor, a metal precursor may be used as the metal raw material. Examples of the metal raw material may include, but are not limited to, metal carbonates, metal sulfates, metal nitrates, and metal chlorides. Any metal precursor may be used as long as it may be used in the art.
The pH adjusting agent acts to lower the solubility of metal ions in the reactor to precipitate metal ions into hydroxides. Non-limiting examples of the pH adjusting agent include sodium hydroxide (NaOH) and/or sodium carbonate (Na2CO3). The pH adjusting agent may be, for example, sodium hydroxide (NaOH).
The complexing agent acts to control the reaction rate in formation of a precipitate in a coprecipitation reaction. Non-limiting examples of the complexing agent include ammonium hydroxide (NH4OH) (aqueous ammonia), citric acid, acrylic acid, tartaric acid, and/or glycolic acid. The content of the complexing agent is used at a general level. The complexing agent may be, for example, aqueous ammonia.
To obtain the Ni-based active material precursor according to an embodiment, the product obtained according to the above-described three acts is washed and an ionizable phosphorus-containing compound is added to the washed product. During washing, water and/or the like may be used. During washing, an alcohol solvent (such as ethanol, isopropanol, and/or propanol) may further be used, if desired.
The adding of the ionizable phosphorus-containing compound to the washed product is an act of impregnating the washed product in a mixture of an ionizable water-soluble phosphorus-containing compound and a solvent. The solvent may be water, an alcohol solvent, or any combination thereof.
Then, the resultant is dried to obtain a desired or suitable Ni-based active material precursor.
The Ni-based active material precursor prepared according to the above-described preparation method may be subjected to TOF-SIMS to identify the shape, structure, and composition of the Ni-based active material precursor. An Ni-based active material according to another embodiment may be obtained from the above-described Ni-based active material precursor. The Ni-based active material may be a compound represented by Formula 2:
Lia(Ni1-x-y-zCOxAlyMz)O2±α1. tm Formula 2
In Formula 2, M may be an element selected from boron (B), magnesium (Mg), calcium (Ca), strontium (Sr), barium (Ba), titanium (Ti), vanadium (V), chromium (Cr), iron (Fe), copper (Cu), and zirconium (Zr), and
0.95≤a≤1.1, 0.3≤(1-x-y-z)<1, 0<x<1, 0≤y<1, 0≤z<1, and 0≤1≤0.1 are satisfied.
In the compound represented by Formula 2, the content of nickel may be higher than the content of cobalt, and the content of nickel may be higher than the content of manganese. In Formula 2, 1.0≤a≤1.3 and 0<x≤1/3 may be satisfied, and 0≤y≤0.5, 0≤z≤0.05, and 1/3≤(1-x-y-z)≤0.98 may be satisfied.
In Formula 2, a may be from 1 to 1.1, x may be from 0.1 to 0.3, y may be from 0.05 to 0.3, and z may be 0.
In the Ni-based active material, the content of nickel may be about 33 mol % to about 98 mol %, for example, about 70 mol % to about 96 mol %, or for example, about 85 mol % to about 95 mol % based on the total content of the transition metals. The total content of the transition metals refers to a sum of the contents of nickel, cobalt, manganese, and M in Formula 2.
The Ni-based active material may be, for example, LiNi0.6Co0.2Mn0.2O2, LiNi0.7Co0.15Mn0.15O2, LiNi0.7Co0.1Mn0.2O2, LiNi0.5Co0.2Mn0.3O2, LiNi1/3Co1/3Mn1/3O2, LiNi0.8Co0.1Mn0.1O2, LiNi0.92Co0.05Al0.3O2, LiNi0.94Co0.03Al0.03O2, LiNi0.88Co0.06Al0.06O2, LiNi0.96Co0.02Al0.02O2, LiNi0.93Co0.04Al0.03O2, LiNi0.8Co0.15Al0.05O2O2, LiNi0.75Co0.20Al0.05O2, LiNi0.92Co0.05Mn0.03O2, LiNi0.94Co0.03Mn0.03O2, LiNi0.88Co0.06Mn0.06O2, LiNi0.96Co0.02Mn0.02O2, LiNi0.93Co0.04Mn0.03O2, LiNi0.8Co0.15Mn0.05O2O2, LiNi0.75Co0.20Mn0.05O2, LiNi0.6Co0.2Mn0.2O2, LiNi0.7Co0.15Mn0.15O2, LiNi0.7Co0.1Mn0.2O2, LiNi0.5Co0.2Mn0.3O2, LiNi1/3Co1/3Mn1/3O2, LiNi0.8Co0.1Mn0.1O2, LiNi0.85Co0.1Al0.05O2, or LiNi0.85Co0.1Al0.05O2.
The nickel-based active material may have a similar/same particle structure and/or characteristics to/as the aforementioned nickel-based active material precursor, except that lithium ions are arranged (e.g., incorporated) in the crystal structure and hydroxides are changed (e.g., converted) to oxides.
Because the secondary particle included in the nickel-based active material has multiple centers and includes a plurality of particulate structures arranged in an isotropic array, the travel distance of lithium ions and electrons from the surface of the secondary particle and the center of the secondary particle is reduced, so that intercalation and desorption (e.g., deintercalation) of lithium ions are easy, and the transmission of electrons is easy. Further, because the particulate structure included in the nickel-based active material includes the porous core portion and the primary particles radially arranged on the porous core portion, the volume of the nickel-based active material is effectively buffered during charging and discharging, and thus cycling stress of the nickel-based active material may be reduced. Accordingly, the nickel-based active material obtained from the aforementioned nickel-based active material precursor may have better (improved) capacity characteristics with respect to a material having the same composition but being a related art structure, even when the content of nickel is not increased.
As used herein, the term “multi-center” indicates that one particle has a plurality of centers. In a multi-center particle, the travel distance of lithium ions from the surface of the particle to a center of the particle may be reduced. Because the travel distance of lithium ions is reduced, a particulate structure having reduced internal resistance, increased charge-discharge efficiency, and/or long lifetime may be obtained.
The nickel-based active material includes a secondary particle including a plurality of particulate structures, and each of the particulate structure includes a porous core portion and a shell portion including primary particles radially arranged on the porous core portion. In 50% or more of the primary particles constituting the surface of the secondary particle, a major axis of each of the primary particles is aligned in (along or with) the normal direction of the surface of the secondary particle. For example, in 60% to 80% of the primary particles constituting the surface of the secondary particle, the major axis of each of the primary particles may be aligned in the normal direction of the surface of the secondary particle. In 50% or more of the primary particles constituting the surface of the secondary particle, the major axis of each of the primary particles may be aligned in the normal direction of the surface of the secondary particle. In 50% or more of the primary particles constituting the surface of the secondary particle, the direction of the major axis of each of the primary particles is (e.g., may be or coincide with the) [110] direction (e.g., of the active material). In 60% to 80% of the primary particles constituting the surface of the secondary particle, the major axis of each of the primary particles may be aligned in the normal direction of the surface of the secondary particle. In 60% to 80% of the primary particles constituting the surface of the secondary particle, the direction of the major axis of each of the primary particles is [110] direction. The (110) plane of the primary particle is a crystal plane where lithium ions are injected into and discharged from the nickel-based active material. When the major axis of the (one or more) primary particles at the outermost of the secondary particle is aligned in the normal direction of the surface of the secondary particle, diffusion of lithium on (at or through) the interface between the nickel-based active material and the electrolyte may be easy. The intercalation and deintercalation of lithium in the nickel-based active material may be easy, and the diffusion distance of lithium ions may be reduced. The primary particle included in the nickel-based active material includes a plate particle, the major axis of the plate particle is aligned in the normal direction of the surface of the secondary particle, and the ratio of thickness to length of the plate particle may be about 1:2 to about 1:20.
The method of preparing the nickel-based active material from the nickel-based active material precursor is not particularly limited, but may be, for example, a dry method.
The nickel-based active material may be prepared by mixing a lithium precursor and the nickel-based active material precursor at a set or predetermined molar ratio and primarily (e.g., initially) heat-treating (low-temperature heat-treating) the mixture at about 600° C. to about 800° C.
As the lithium precursor, for example, lithium hydroxide, lithium fluoride, lithium carbonate, or a mixture thereof may be used. The mixing ratio of the lithium precursor and the nickel-based active material precursor may be stoichiometrically adjusted so that the nickel-based active material of Formula 2 is suitably prepared.
The mixing of the lithium precursor and the nickel-based active material precursor may be performed by dry mixing or using a mixer. The dry mixing may be carried out by milling. The conditions of the milling are not particularly limited, but the milling may be carried out so that the precursor used as a starting material is hardly (e.g., substantially not) deformed (e.g., atomized). The size of the lithium precursor mixed with the nickel-based active material precursor may be previously controlled. The size (average particle diameter) of the lithium precursor may be in a range of about 5 μm to about 15 μm, for example, about 10 μm. A desired or suitable mixture may be obtained by milling the lithium precursor having such a size and the nickel-based active material precursor at a rotation speed of about 300 rpm to 3,000 rpm. When the temperature in the mixer increases to 30° C. or higher during the milling process, a cooling process may be performed to maintain the temperature in the mixer at or near room temperature (25° C.).
The low-temperature heat treatment may be carried out under an oxidation gas (e.g., oxidizing) atmosphere. The oxidation gas atmosphere may be obtained by using oxidation gas (such as oxygen or air). For example, the oxidation gas may include about 10 vol % to about 20 vol % of oxygen or air and about 80 vol % to about 90 vol % of an inert gas. The low-temperature heat treatment may be carried out at a temperature below densification temperature as the reaction of the lithium precursor and the nickel-based active material precursor proceeds. The densification temperature is a temperature at which sufficient crystallization may be achieved to realize a charging capacity that the active material may provide. The low-temperature heat treatment may be carried out at about 600° C. to about 800° C., for example, about 650° C. to about 800° C. The low-temperature heat treatment time varies depending on the heat treatment temperature and/or the like, but may be, for example, about 3 hours to about 10 hours.
The method of preparing the nickel-based active material may further include a secondary heat treatment (high-temperature heat treatment) performed under an oxidation gas atmosphere in which exhaust gas is suppressed from the inside of the reactor after the low-temperature heat treatment. The high-temperature heat treatment may be carried out, for example, at about 700° C. to about 900° C. The high-temperature heat treatment time varies depending on the heat treatment temperature and/or the like, but may be, for example, about 3 hours to about 10 hours.
In the Ni-based active material obtained in the above-described process, the content of lithium phosphate may be about 0.03 wt % to about 0.4 wt %, about 0.03 wt % to about 0.3 wt %, about 0.03 wt % to about 0.2 wt %, about 0.03 wt % to about 0.1 wt %, about 0.03 wt % to about 0.08 wt %, about 0.03 wt % to about 0.06 wt %, about 0.03 wt % to about 0.05 wt %, or about 0.03 wt % to about 0.04 wt % based on the total weight of the Ni-based active material.
According to another embodiment, the content of the lithium phosphate in the Ni-based active material may be about 0.04 wt % to about 0.4 wt % based on the total weight of the Ni-based active material.
The total weight of the Ni-based active material is a weight of the Ni-based active material including lithium phosphate. When the content of the lithium phosphate is within the above range, a Ni-based active material having improved electrochemical characteristics and/or excellent capacity characteristics may be obtained.
In the Ni-based active material according to an embodiment, the content of lithium phosphate present on the surface (e.g., outermost surface) of the secondary particle may be greater than the content of lithium phosphate present in the porous core portion and (e.g. between primary particles of) the shell portion. Also, according to another embodiment, in the Ni-based active material, the content of the lithium phosphate present between the plurality of primary particles of the shell portion may be greater than the content of lithium phosphate present in the porous core portion.
In the Ni-based active material according to another embodiment, the content of phosphorus present on the surface of the secondary particle may be greater than the content of phosphorus present in the porous core portion and the shell portion. Also, according to an embodiment, in the Ni-based active material, the content of phosphorus present between the plurality of primary particles of the shell portion may be greater than the content of phosphorus present in the porous core portion. In this regard, phosphorus may refer to PO3, PO4 or any combination thereof, for example, PO3.
A lithium secondary battery according to another embodiment includes a positive electrode including the above-described Ni-based active material for a lithium secondary battery, a negative electrode, and an electrolyte interposed therebetween.
Methods of preparing the lithium secondary battery are not particularly limited, and any suitable method in the art may be used. For example, the lithium secondary battery may be prepared according to the following method.
The positive electrode and the negative electrode may be fabricated by applying a composition for forming a positive active material layer and a composition for forming a negative active material layer onto respective current collectors and drying the applied compositions.
The positive electrode and the negative electrode may be fabricated by forming a positive active material layer and a negative active material layer on different current collectors by applying a composition for forming a positive active material layer and a composition for forming a negative active material layer onto respective current collectors and drying the applied compositions.
The composition for forming a positive active material layer may be prepared by mixing a positive active material, a conductive material, a binder, and a solvent. As the positive active material, a positive active material according to an embodiment may be used.
The binder of the positive electrode may increase an adhesive force among (between) particles of the positive active material and an adhesive force between the positive active material and a positive current collector. Non-limiting examples of the binder include polyvinylidene fluoride (PVDF), a vinylidene fluoride/hexafluoropropylene copolymer (PVDF-co-HFP), polyvinyl alcohol, polyacrylonitrile, carboxymethyl cellulose (CMC), starch, hydroxypropyl cellulose, regenerated cellulose, polyvinyl pyrrolidone, tetrafluoroethylene, polyethylene, polypropylene, ethylene-propylene-diene terpolymer (EPDM), sulfonated EPDM, styrene butylene rubber (SBR), fluorine rubber, and/or various copolymers. These compounds may be used alone or in a combination of at least two thereof.
The conductive material is not particularly limited as long as it does not cause any unwanted chemical change in the corresponding battery, and has conductivity. Non-limiting examples of the conductive material include: graphite (such as natural graphite and/or artificial graphite); carbon-based materials (such as carbon black, acetylene black, ketjen black, channel black, furnace black, lamp black, and/or thermal black); conductive fibers (such as a carbon nanotube, a carbon fiber, and/or a metal fiber); carbon fluoride; metal powders (such as aluminum powder and/or nickel powder); conductive whiskers (such as zinc oxide and/or potassium titanate); conductive metal oxides (such as titanium oxide); and/or conductive polymers (such as polyphenylene derivatives).
The content of the conductive material may be in a range of 1 part by weight to 10 parts by weight or 1 part by weight to 5 parts by weight based on 100 parts by weight of the positive active material. When the content of the conductive material is within the above range, an electrode finally obtained may have suitable or excellent conductivity.
Non-limiting examples of the solvent may include N-methylpyrrolidone, and the content of the solvent may be in a range of 20 parts by weight to 200 parts by weight based on 100 parts by weight of the positive active material. When the amount of the solvent is within the above range, the positive active material may be easily formed.
The positive current collector is not limited as long as it has a thickness of about 3 μm to about 500 μm and has high conductivity without causing any unwanted chemical change in the corresponding battery. For example, the positive current collector may include stainless steel, aluminum, nickel, titanium, and/or fired carbon, or may include aluminum and/or stainless steel surface-treated with carbon, nickel, titanium, and/or silver. The positive current collector may have fine irregularities on the surface thereof to increase the binding force of the positive active material, and may have various forms (such as a film, a sheet, a foil, a net, a porous body, a foam, and/or non-woven fabric).
Separately, a negative active material, a binder, and a solvent may be mixed to prepare the composition for forming a negative active material layer.
A material capable of absorbing and discharging lithium ions is used as the negative active material. Non-limiting examples of the negative active material include carbon-based materials (such as graphite and/or carbon), lithium metal and alloys thereof, and/or silicon oxide-based materials. According to an embodiment of the present disclosure, silicon oxide may be used.
Non-limiting examples of the binder of the negative electrode include a polyvinylidene fluoride/hexafluoropropylene copolymer (PVDF-co-HFP), polyvinylidene fluoride, polyacrylonitrile, polymethyl methacrylate, polyvinyl alcohol, carboxymethyl cellulose (CMC), starch, hydroxypropyl cellulose, regenerated cellulose, polyvinyl pyrrolidone, tetrafluoroethylene, polyethylene, polypropylene, polyacrylic acid, ethylene-propylene-diene terpolymer (EPDM), sulfonated EPDM, styrene butylene rubber (SBR), fluorine rubber, similar compounds thereof in which hydrogen is substituted with Li, Na, Ca, and/or the like, and/or various copolymers.
The negative active material layer may further include a conductive material. The conductive material is not particularly limited as long as it does not cause any unwanted chemical change in the corresponding battery and has conductivity. Non-limiting examples of the conductive material include: graphite (such as natural graphite and/or artificial graphite); carbon black (such as carbon black, acetylene black, ketjen black, channel black, furnace black, lamp black, and/or thermal black); conductive fibers (such as carbon fiber and/or metal fiber); conductive tubes (such as carbon nanotubes); fluorocarbons; metal powders (such as aluminum powder and/or nickel powder); conductive whiskers (such as zinc oxide and/or potassium titanate); conductive metal oxides (such as titanium oxide); and/or conductive materials (such as polyphenylene derivatives). The conductive material may be carbon black, for example, carbon black having an average particle diameter of dozens of nanometers.
The content of the conductive material may be 0.01 parts by weight to 10 parts by weight, 0.01 parts by weight to 5 parts by weight, or 0.1 parts by weight to 2 parts by weight based on 100 parts by weight of a total weight of the negative active material layer.
The composition for forming a negative active material layer may further include a thickener. As the thickener, at least one of carboxymethyl cellulose (CMC), carboxyethyl cellulose, starch, regenerated cellulose, ethyl cellulose, hydroxymethyl cellulose, hydroxyethyl cellulose, hydroxypropyl cellulose, styrene butadiene rubber (SBR), or polyvinyl alcohol may be used; for example, CMC may be used.
The content of the solvent may be in a range of 100 parts by weight to 300 parts by weight based on 100 parts by weight of the total weight of the negative active material. When the content of the solvent is within the above range, the negative active material layer may be easily formed.
In general, the negative current collector may have a thickness of 3 μm to 500 μm. The negative current collector is not particularly limited as long as it has high conductivity without causing any unwanted chemical change in the corresponding battery. For example, the negative current collector may include copper, stainless steel, aluminum, nickel, titanium, and/or fired carbon, may include copper and/or stainless steel surface-treated with carbon, nickel, titanium and/or silver, or may include an aluminum-cadmium alloy. Similarly to the positive current collector, the negative current collector may have fine irregularities on the surface thereof to increase the binding force of the positive active material, and may have various suitable forms (such as film, sheet, foil, net, porous body, foam, and/or non-woven fabric).
A separator is interposed between the positive electrode and the negative electrode fabricated according to the above-described process.
Generally, the separator has a pore diameter of about 0.01 μm to about 10 pm and a thickness of about 5 μm to about 300 μm. In one example, as the separator, a sheet or non-woven fabric made of an olefin-based polymer (such as polypropylene or polyethylene, and/or glass fiber) may be used. When a solid electrolyte (such as a polymer electrolyte) is used, the solid electrolyte may also act as a separator.
A non-aqueous electrolyte containing a lithium salt includes a non-aqueous electrolyte and a lithium salt. As the non-aqueous electrolyte, a non-aqueous electrolytic solution, an organic solid electrolyte, and/or an inorganic solid electrolyte may be used.
Non-limiting examples of the non-aqueous electrolytic solvent may include aprotic organic solvents (such as N-methyl-2-pyrrolidinone, propylene carbonate, ethylene carbonate, butylene carbonate, dimethyl carbonate, diethyl carbonate, gamma-butyrolactone, 1,2-dimethoxyethane, 2-methyl tetrahydrofuran, dimethyl sulfoxide, 1,3-dioxolane, N,N-formamide, N,N-dimethylformamide, dioxolane, acetonitrile, nitromethane, methyl formate, methyl acetate, phosphoric acid triester, trimethoxy methane, dioxolane derivatives, sulfolane, methyl sulfolane, 1,3-dimethyl-2-imidazolidinone, propylene carbonate derivatives, tetrahydrofuran derivatives, ethers, methyl propionate, and/or ethyl propionate).
Non-limiting examples of the organic solid electrolyte may include polyethylene derivatives, polyethylene oxide derivatives, polypropylene oxide derivatives, phosphate ester polymers, polyester sulfide, polyvinyl alcohols, and/or polyvinylidene fluoride.
Non-limiting examples of the inorganic solid electrolyte may include a nitride, halide, and/or sulfate of Li (such as Li3N, Lil, Li5NI2, Li3N—LiI—LiOH, LiSiO4, Li2SiS3, Li4SiO4, Li4SiO4—LiI—LiOH, and/or Li3PO4—Li2S—SiS2).
The lithium salt is a material easily soluble in the non-aqueous electrolyte, and non-limiting examples thereof include LiCI, LiBr, Lil, LiCIO4, LiBF4, LiB10Cl10, LiPF6, LiCF3SO3, LiCF3CO2, LiAsF6, LiSbF6, LiAICl4, CH3SO3Li, CF3SO3Li, (CF3SO2)2NLi, (FSO2)2NLi, lithium chloroborate, lower aliphatic carboxylic acid lithium, and/or lithium tetraphenylborate imide.
Referring to
In addition, due to excellent storage stability, lifespan characteristics, and/or high-rate characteristics at high temperature, the lithium secondary battery may be used in electric vehicles (EVs). For example, the lithium secondary battery may be used in hybrid vehicles (such as plug-in hybrid electric vehicles (PHEVs)).
Hereinafter, the present disclosure will be described in more detail with reference to examples and comparative examples. However, these examples are for illustrating the present disclosure, and the scope of the present disclosure is not limited thereto.
A Ni-based active material precursor(Ni0.6Co0.2Mn0.2(OH)2) was synthesized by a coprecipitation method. In the following preparation process, as metal raw materials for forming a Ni-based active material precursor, nickel sulfate (NiSO4.6H2O), cobalt sulfate (CoSO4.7H2O), and manganese sulfate (MnSO4.H2O) were dissolved in distilled water (as a solvent) in a molar ratio of Ni:Co:Mn=6:2:2 to prepare a mixed solution. Also, aqueous ammonia (NH4OH) for forming a complex and sodium hydroxide (NaOH) as a precipitant were prepared.
(1) First Act: Feed Rate of 5.10 L/hr, Stirring Power of 5.0 kW/m3, 0.5 M NH3, and pH of 11.30 to 11.50
Aqueous ammonia having a concentration of 0.5 mol/L (M) was added to a reactor equipped with a stirrer. 2 mol/L (M) of metal raw materials (mixed solution of nickel sulfate, cobalt sulfate, and manganese sulfate) were supplied at a feed rate of 5.10 L/hr, and 0.5 mol/L (M) of aqueous ammonia was supplied at a feed rate of 0.77 L/hr while maintaining a stirring power of 5.0 kW/m3 and a reaction temperature of 50° C. Then, sodium hydroxide (NaOH) was supplied to maintain the pH. The pH of the reaction mixture in the reactor was maintained at 11.30 to 11.50. The first act was performed while stirring at this pH range for 6 hours.
(2) Second Act: Feed Rate of 6.38 L/hr, Stirring Power of 3.0 kW/m3, 0.6 M NH3, and pH of 10.65 to 10.75
After the first act reaction was completed, 2 mol/L (M) of the metal raw materials were supplied at a feed rate of 6.38 L/hr, and 0.6 mol/L (M) of aqueous ammonia was supplied at a feed rate of 1.01 L/hr while reducing the stirring power to 3.0 kW/m3 and maintaining the reaction temperature at 50° C. Then, sodium hydroxide (NaOH) was supplied to maintain the pH. The pH of the reaction mixture in the reactor was maintained at 10.65 to 10.75. The second act was performed while stirring until an average particle diameter D50 of particles contained in the reactor reached about 10 μm. Then, a part of the product obtained in the second act reaction was removed from the reactor to reduce the concentration of the product.
(3) Third Act: Feed Rate of 8.50 L/hr, Stirring Power of 0.8 kW/m3, 0.7 M NH3, and pH of 10.10 to 10.20
After the second act reaction was completed and the average particle diameter D50 of the particles contained in the reactor reached about 10 μm, 2 mol/L (M) of the metal raw materials were supplied at a feed rate of 8.50 L/hr and 0.7 mol/L (M) of aqueous ammonia was supplied at a feed rate of 1.18 L/hr while reducing the stirring power to 0.8 kW/m3 and maintaining the reaction temperature at 50° C., and NaOH was added to maintain the pH. The pH of the reaction mixture in the reactor was maintained at 10.10 to 10.20. The third reaction was performed while stirring at this pH range for 6 hours. Subsequently, a slurry solution contained in the reactor was filtered and washed with high-purity distilled water. A preliminary Ni-based active material precursor that is a resultant obtained by washing as described above was impregnated in (with) a mixture of phosphoric acid (H3PO4) and water at 25° C. for 2 hours and dried at 150° C. for 12 hours to obtain a Ni-based active material precursor adsorbed with phosphorus. In the mixture of phosphoric acid and water, the content of phosphoric acid is 0.2 parts by weight based on 100 parts by weight of the mixture.
The precursor adsorbed with the phosphorus was dried in a hot-air oven for 24 hours to obtain a Ni-based active material precursor (Ni0.6Co0.2Mn0.2(OH)2) adsorbed with phosphorus.
Phosphorus was present in the porous core portion, between the plurality of primary particles of the shell portion, and on the surface of the secondary particle in the phosphorus-containing Ni-based active material precursor. In the finally obtained Ni-based active material precursor (Ni0.6Co0.2Mn0.2(OH)2), the total content of phosphorus (P) was 0.05 wt % based on the total weight of the Ni-based active material precursor. In this regard, phosphorus may refer to PO3, PO4 or any combination thereof.
A Ni-based active material precursor was prepared in substantially the same manner as in Preparation Example 1, except that the content of phosphoric acid was adjusted in the mixture of phosphoric acid (H3PO4) and water such that the total content of phosphorus was 1 wt % in the finally obtained Ni-based active material precursor (Ni0.6Co0.2Mn0.2(OH)2). The total content of phosphorus was 1 wt % in the finally obtained Ni-based active material precursor (Ni0.6Co0.2Mn0.2(OH)2) based on the total weight of the Ni-based active material precursor.
A Ni-based active material precursor was prepared in substantially the same manner as in Preparation Example 1, except that the content of phosphoric acid was adjusted in the mixture of phosphoric acid (H3PO4) and water such that the total content of phosphorus was 0.5 wt % in the finally obtained Ni-based active material precursor (Ni0.6Co0.2Mn0.2(OH)2). The total content of phosphorus was 0.5 wt % in the finally obtained Ni-based active material precursor (Ni0.6Co0.2Mn0.2(OH)2) based on the total weight of the Ni-based active material precursor.
A Ni-based active material precursor was prepared in substantially the same manner as in Preparation Example 1, except that the content of phosphoric acid was adjusted in the mixture of phosphoric acid (H3PO4) and water such that the total content of phosphorus was 2 wt % in the finally obtained Ni-based active material precursor (Ni0.6Co0.2Mn0.2(OH)2). The total content of phosphorus was 2 wt % in the finally obtained Ni-based active material precursor (Ni0.6Co0.2Mn0.2(OH)2) based on the total weight of the Ni-based active material precursor.
A Ni-based active material precursor (Ni0.7Co0.15Mn0.15(OH)2) was synthesized in substantially the same manner as in Preparation Example 1, except that the mixed solution was prepared such that a molar ratio of the nickel sulfate (NiSO4.6H2O), cobalt sulfate (CoSO4.7H2O), and manganese sulfate (MnSO4.H2O), as metal raw materials, was Ni:Co:Mn=7:1.5:1.5 instead of Ni:Co:Mn=6:2:2 in Preparation Example 1.
A Ni-based active material precursor (Ni0.7Co0.1Mn0.2(OH)2) was synthesized in substantially the same manner as in Preparation Example 1, except that the mixed solution was prepared such that a molar ratio of the nickel sulfate (NiSO4.6H2O), cobalt sulfate (CoSO4.7H2O), and manganese sulfate (MnSO4.H2O), as metal raw materials, was Ni:Co:Mn=7:1:2 instead of Ni:Co:Mn=6:2:2 in Preparation Example 1.
First and second acts were performed in substantially the same manner as in Preparation Example 1.
Third Act parameters: feed rate of 8.50 L/hr, stirring power of 0.8 kW/m3, 0.7 M NH3, and pH of 10.10 to 10.20.
After the second act reaction was completed and the average particle diameter D50 of the particles contained in the reactor reached about 10 μm, 2 mol/L (M) of the metal raw materials were supplied at a feed rate of 8.50 L/hr, and 0.7 mol/L (M) of aqueous ammonia was supplied at a feed rate of 1.18 L/hr while reducing stirring power to 0.8 kW/m3 and maintaining reaction temperature at 50° C., and NaOH was added to maintain the pH. The pH of the reaction mixture in the reactor was maintained at 10.10 to 10.20. The third act reaction was performed while stirring at this pH range for 6 hours.
After the third act reaction was completed, the slurry solution was filtered and washed with high-purity distilled water. Subsequently, the washed resultant was dried in a hot-air oven for 24 hours to obtain a Ni-based active material precursor (Ni0.6Co0.2Mn0.2(OH)2).
The Ni-based active material precursor (Ni0.6Co0.2Mn0.2(OH)2) obtained in Comparative Preparation Example 1 and NH4H2PO4 as a phosphorus compound were mixed by milling at 250 rpm to obtain a mixture. The mixture was heat-treated in an oxygen atmosphere at about 700° C. for 6 hours to obtain a Ni-based active material precursor coated with NH4H2PO4.
A Ni-based active material precursor was prepared in substantially the same manner as in Preparation Example 1, except that aluminum phosphate was used instead of phosphoric acid (H3PO4).
In the case of Comparative Preparation Example 3, because aluminum phosphate, unlike phosphoric acid, is not an ionizable phosphorus compound, it is more difficult to coat phosphorus in pores of the porous core portion of the Ni-based active material precursor and/or grain boundaries of the primary particles of the shell portion using the aluminum phosphate.
A Ni-based active material precursor was prepared in substantially the same manner as in Preparation Example 1, except that the content of phosphoric acid was adjusted in the mixture of phosphoric acid (H3PO4) and water such that the total content of phosphorus was 0.005 wt % in the finally obtained Ni-based active material precursor (Ni0.6Co0.2Mn0.2(OH)2). The total content of phosphorus was 0.005 wt % in the finally obtained Ni-based active material precursor (Ni0.6Co0.2Mn0.2(OH)2) based on the total weight of the Ni-based active material precursor
In the Ni-based active material precursor prepared in Comparative Preparation Example 4, effects obtained by including phosphorus were insignificant.
A Ni-based active material precursor was prepared in substantially the same manner as in Preparation Example 1, except that the content of phosphoric acid was adjusted in the mixture of phosphoric acid (H3PO4) and water such that the total content of phosphorus was 3 wt % in the finally obtained Ni-based active material precursor (Ni0.6Co0.2Mn0.2(OH)2). The total content of phosphorus was 3 wt % in the finally obtained Ni-based active material precursor (Ni0.6Co0.2Mn0.2(OH)2) based on the total weight of the Ni-based active material precursor.
Most of the pores of the porous inner portion disappeared in the Ni-based active material precursor prepared in Comparative Preparation Example 5. When a positive electrode including a Ni-based active material obtained therefrom is used, effects on improving lifespan characteristics of a lithium secondary battery were insignificant.
Preparation of Ni-Based Active Material
Lithium hydroxide NOM was added to a composite metal hydroxide (Ni0.6Co0.2Mn0.2(OH)2), which is the phosphorus-containing Ni-based active material precursor prepared in Preparation Example 1, and mixed at a molar ratio of 1:1 by a dry method. The mixture was heat-treated at about 700° C. for 6 hours in an oxygen atmosphere to obtain a Ni-based active material (LiNi0.6Co0.2Mn0.2O2). The obtained Ni-based active material had an inner portion having a porous structure and an outer portion having a radial arrangement structure. The Ni-based active material was heat-treated under atmospheric conditions at about 800° C. for 6 hours to obtain a Ni-based active material (LiNi0.6Co0.2Mn0.2O2) including a secondary particle in which primary particle aggregates having at least two radial centers are arranged in a multi-center isotropic array.
In the Ni-based active material, the content of lithium phosphate was 0.15 wt % based on the total weight of the lithium phosphate-containing Ni-based active material. The structure of the Ni-based active material is identical to that of the Ni-based active material precursor.
As used herein, the term “radial center” refers to a center of a particulate structure including the porous core portion and the shell portion including primary particles radially arranged on the porous core portion, as shown in
Additional Ni-based active materials were prepared in substantially the same manner as in Example 1, except that the Ni-based active material precursors prepared in Preparation Examples 2 to 6 were used instead of the Ni-based active material precursor of Preparation Example 1.
Additional Ni-based active materials were prepared in substantially the same manner as in Example 1, except that the Ni-based active material precursors prepared in Comparative Preparation Examples 1 to 5 were used instead of the Ni-based active material precursor of Preparation Example 1.
The Ni-based active material obtained in Comparative Example 2 was prepared using the Ni-based active material precursor of Comparative Preparation Example 2, and thus lithium phosphate was formed only on the surface of the Ni-based active material. When observing the surface with a scanning electron microscope (SEM), lithium phosphate was not uniformly formed, but substantially non-uniform aggregates of lithium phosphate were formed on the surface.
Also, the Ni-based active material obtained in Comparative Example 5 was prepared using the Ni-based active material precursor of Comparative Preparation Example 5, and thus most pores of the porous inner portion of the Ni-based active material precursor disappeared. When a coin cell is prepared using the Ni-based active material according to the following method, effects on improving lifespan characteristics of the coin cell were insignificant.
MANUFACTURE OF COIN CELL
A coin cell was manufactured as follows using the Ni-based active material (LiNi0.6Co0.2Mn0.2O2) obtained according to Example 1 as a positive active material.
A mixture of 96 g of the Ni-based active material (LiNi0.6Co0.2Mn0.2O2) obtained according to Example 1, 2 g of polyvinylene fluoride, 47 g of N-methyl pyrrolidone as a solvent, and 2 g of carbon black as a conductive agent was defoamed using a mixer to prepare a uniformly dispersed slurry for forming a positive active material layer.
The slurry prepared in this way was applied onto an aluminum foil using a doctor blade to form a thin plate, and then the thin plate was dried at 135° C. for 3 hours or more and then rolled and vacuum-dried to fabricate a positive electrode.
A 2032 format coin cell was manufactured using the positive electrode and a lithium metal as a counter electrode. A separator (thickness: 16 μm) made of a porous polyethylene (PE) film was interposed between the positive electrode and the lithium metal counter electrode, and an electrolyte was injected into the separator to manufacture the 2032 format coin cell. As the electrolyte, a solution in which 1.1 M LiPF6was dissolved in a mixed solvent in which ethylene carbonate (EC) and ethylmethyl carbonate (EMC) were mixed at a volume ratio of 3:5 was used.
A coin cell was manufactured in substantially the same manner as in Manufacture Example 1, except that the Ni-based active material of Example 2 was used instead of the Ni-based active material of Example 1.
A coin cell was manufactured in substantially the same manner as in Manufacture Example 1, except that the Ni-based active material of Example 3 was used instead of the Ni-based active material of Example 1.
Coin cells were manufactured in substantially the same manner as in Manufacture Example 1, except that the Ni-based active materials prepared in Comparative Examples 1 to 5 were respectively used instead of the Ni-based active material of Example 1.
Cross-sections of the Ni-based active material precursor prepared according to Preparation Example 1 were analyzed. A Magellan 400L (FEI company) was utilized as the scanning electron microscope. Analysis results are shown in
As shown in
The Ni-based active materials of Example 1 and Comparative Example 2 were evaluated by TOF-SIMS. TOF-SIMS analysis was performed using an Ion TOFS manufactured by Ion TOF. TOF-SIMS analysis was performed under the conditions of Primary ion: Bi1+, Sputter ion: Cs+.
TOF-SIMS spectra are shown in
The P component was observed in the Ni-based active material of Example 1 when compared with (e.g., but not observed in) the Ni-based active material of Comparative Example 1, as shown in
Referring to the above, it may be confirmed that, as in the cross-section analysis results, when P is coated on the precursor by impregnation/adsorption and then the active material is prepared, P is detected in the inner portion as well as the surface.
Also, the Ni-based active material precursor of Preparation Example 1 was subjected to TOF-SIMS analysis.
As a result of analysis, the Ni-based active material precursor of Preparation Example 1 had the same TOF-SIMS results as the above-described Ni-based active material. Thus, the ratio of the peak intensity related to P in the inner portion of the Ni-based active material precursor to that in the outer portion of the
Ni-based active material precursor was in a range of 1:2 to 1:4, for example, 1:2.2, indicating that a relatively low intensity was observed in the porous inner portion compared to the shell portion and the surface.
The Ni-based active material precursor of Preparation Example 1 was subjected to scanning electron microscope-energy dispersive X-ray Spectroscopy (SEM-EDX), and the results are shown in
The coin cells manufactured according to Manufacture Example 1 and Comparative Manufacture Example 1 were charged and discharged once at 25° C. at 0.1C as a formation protocol. Subsequently, charging-discharging was performed once at 0.1C to confirm initial charge-discharge characteristics. During charging, the coin cells were each set such that a constant current (CC) mode starts, is converted into a constant voltage (CV) mode, and the coin cells are cut off at 4.3 V and 0.05C. During discharging, the coin cells were set such that the coin cells are cut off at 3.0 V at the constant current (CC) mode. Initial charge efficiency (I.C.E) were measured according to Equation 1 below, and the results thereof are given in Table 1 below.
Initial Charge Efficiency [%]=[discharge capacity at 1st cycle/charge capacity at 1st cycle]×100 Equation 1
As shown in Table 1, the coin cell manufactured according to Manufacture Example 1 had charge-discharge efficiency (initial characteristics) and initial discharge capacity similar to those of the coin cell prepared in Comparative Manufacture Example 1. However, as shown in Evaluation Examples 5 and 6 below, the coin cell of Manufacture Example 1 had improved high-rate characteristics and lifespan characteristics compared to that of Comparative Manufacture Example 1.
The coin cells manufactured according to Manufacture Example 1 and Comparative Manufacture Examples 1 and 2 were charged at a constant current of 0.2C and a constant voltage of 4.3 V (0.05C cut-off), rested for 10 minutes, and discharged at a constant current of 0.2C, 0.33C, 0.5C, 1C, 2C, or 3C) until the voltage reached 3.0 V. For example, rate capability of each coin cell was evaluated while periodically changing the discharge rate at 0.2C, 0.33C, 0.5C, 1C, 2C, or 3C as the number of charging and discharging cycles increases. However, during the first to third charging and discharging, the cell was discharged at a rate of 0.1C. In this regard, rate capability is obtained by Equation:
Rate property (%)=(discharge capacity when cell is discharged at a specific constant current)/(discharge capacity when cell is discharged at a rate of 0.1 C)×100 Equation 2
High-rate characteristics evaluation results are shown in Table 2:
Referring to Table 2, the coin cell of Manufacture Example 1 had increased high-rate characteristics compared to the coin cell manufactured in Comparative Manufacture Example 1.
The high-rate characteristics of the coin cell of Comparative Manufacture Example 2 was evaluated in substantially the same manner as in the above-described method of evaluating the charge-discharge efficiency of Manufacture Example 1.
As a result of evaluation, the coin cell of Comparative Manufacture Example 2 had the same discharge amount as that of the coin cell of Comparative Manufacture Example 1 but a slightly increased charge-discharge efficiency due to a decreased charge amount. However, the coin cell of Comparative Manufacture Example 2 showed deteriorated lifespan characteristics at high temperature, as described in Evaluation Example 6 below.
The coin cells manufactured according to Manufacture Example 1 and Comparative Manufacture Examples 1 and 2 were charged and discharged once at 0.1C to proceed formation. Subsequently, charging-discharging was performed once at 0.2C to confirm initial charge-discharge characteristics. Cycle characteristics were observed by repeating charging and discharging 50 times at 45° C. and 1C. During charging, the coin cells were set such that a constant current (CC) mode starts, is converted into a constant voltage (CV) mode, and the coin cells are cut off at 4.3 V and 0.05C. During discharging, the coin cells were set such that the coin cells are cut off at 3.0 V at the constant current (CC) mode. This cycle was repeated 80 times. Changes in discharge capacity with respect to the number of cycles are shown in
Referring to
Lifespan characteristics of the coin cell of Comparative Manufacture Example 2 at high temperature (e.g., 60° C.) were evaluated in substantially the same manner as the evaluation method of the charge-discharge efficiency of the coin cell of Manufacture Example 1.
As a result of evaluation, the coin cell of Comparative Manufacture Example 2 lifespan characteristics at high temperature less than those of the coin cell of Comparative Manufacture Example 1 by about 1%.
The lithium secondary batteries prepared in Manufacture Example 1 and Comparative Manufacture Example 1 were charged and discharged 50 times at a high temperature (60° C.) at a driving voltage of 3 V to 4.4 V under the conditions of 0.5C/1C, and the volume of gas generated in the batteries was measured. The results are shown in
Referring to
By using the Ni-based active material obtained from the Ni-based active material precursor for a lithium secondary battery according to an embodiment, gas generation may effectively be inhibited during and after repeated charging and discharging of the lithium secondary battery. In addition, by using the Ni-based active material precursor, lithium may be easily diffused in the interface between a positive active material and an electrolyte, and lithium may be easily diffused into the active material. Further, it is possible to obtain a nickel-based active material that easily intercalates and deintercalates lithium, and has a short diffusion distance of lithium ions. In the lithium secondary battery manufactured using such a positive active material, the utilization of lithium is improved, and the breakage of the active material according to charging and discharging may be suppressed to increase capacity and/or lifetime.
As used herein, the terms “substantially,” “about,” and similar terms are used as terms of approximation and not as terms of degree, and are intended to account for the inherent deviations in measured or calculated values that would be recognized by those of ordinary skill in the art.
Any numerical range recited herein is intended to include all sub-ranges of the same numerical precision subsumed within the recited range. For example, a range of “1.0 to 10.0” is intended to include all subranges between (and including) the recited minimum value of 1.0 and the recited maximum value of 10.0, that is, having a minimum value equal to or greater than 1.0 and a maximum value equal to or less than 10.0, such as, for example, 2.4 to 7.6. Any maximum numerical limitation recited herein is intended to include all lower numerical limitations subsumed therein and any minimum numerical limitation recited in this specification is intended to include all higher numerical limitations subsumed therein. Accordingly, Applicant reserves the right to amend this specification, including the claims, to expressly recite any sub-range subsumed within the ranges expressly recited herein.
It should be understood that embodiments described herein should be considered in a descriptive sense only and not for purposes of limitation. Descriptions of features or aspects within each embodiment should typically be considered as being available for other similar features or aspects in other embodiments. While one or more embodiments have been described with reference to the figures, it will be understood by those of ordinary skill in the art that various suitable changes in form and details may be made therein without departing from the spirit and scope of the disclosure, as defined by the following claims and equivalents thereof.
Number | Date | Country | Kind |
---|---|---|---|
10-2020-0142522 | Oct 2020 | KR | national |