Positive Electrode Active Material for Lithium Secondary Battery and Method for Preparing the Same
20240047670 ยท 2024-02-08
Assignee
Inventors
Cpc classification
H01M4/62
ELECTRICITY
H01M4/5825
ELECTRICITY
H01M4/485
ELECTRICITY
C01P2004/80
CHEMISTRY; METALLURGY
H01M4/525
ELECTRICITY
C01G53/50
CHEMISTRY; METALLURGY
H01M4/0471
ELECTRICITY
H01M4/36
ELECTRICITY
H01M4/505
ELECTRICITY
H01M4/131
ELECTRICITY
Y02E60/10
GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
H01M4/1391
ELECTRICITY
H01M2004/021
ELECTRICITY
H01M10/0525
ELECTRICITY
International classification
H01M4/525
ELECTRICITY
H01M4/505
ELECTRICITY
Abstract
A positive electrode active material for a lithium secondary battery having improved high-temperature life and an increase in resistance, and a method for preparing the same are disclosed herein. In some embodiments, a positive electrode active material includes a powder of a positive electrode active material and a lithium boron compound coating layer on the surface of the powder, wherein the lithium boron compound coating layer has a peak intensity ratio of two peaks in the spectrum of Time-of-Flight Secondary Ion Mass Spectrometry (ToF-SIMS) that is equal to the peak intensity ratio of the corresponding peaks of LiBO.sub.2 within a range of 50%.
Claims
1. A positive electrode active material for a lithium secondary battery, comprising: a powder of a positive electrode active material; and a lithium boron compound coating layer on the surface of the powder, wherein the lithium boron compound coating layer has a peak intensity ratio of two peaks measured by Time-of-Flight Secondary Ion Mass Spectrometry (ToF-SIMS) that is equal to the peak intensity ratio of the corresponding peaks of LiBO.sub.2 within a range of 50%.
2. The positive electrode active material according to claim 1, wherein the lithium boron compound coating layer has a peak intensity ratio of 4.350%, wherein the peak intensity ratio is a ratio of intensity of a peak having the highest intensity among the peaks detected at a mass of 156.85-156.95 to the intensity of a peak having the highest intensity among the peaks detected at a mass of 153.05-153.15 in the ToF-SIMS spectrum.
3. The positive electrode active material according to claim 1, wherein the lithium boron compound coating layer has a peak intensity ratio of 9.950%, wherein the peak intensity ratio is a ratio of intensity of a peak having the highest intensity among the peaks detected at a mass of 182.85-182.95 to an intensity of a peak having the highest intensity among the peaks detected at a mass of 179.05-179.15 in the ToF-SIMS spectrum.
4. A method for preparing a positive electrode active material for a lithium secondary battery, comprising: a first firing step of mixing a lithium source with a precursor and heat treating the resultant mixture to obtain a fired product; a second firing step of mixing the fired product with a first B source and heat treating the resultant mixture to form a surface protective layer on the fired product; a water-washing step of removing unreacted lithium remaining on the surface of the fired product obtained from the second firing step; and a coating step of drying the product of the water-washing step and heat treating the dried product with a second B source to form a positive electrode active material.
5. The method according to claim 4, wherein the precursor is a lithium transition metal oxide, wherein the lithium transition metal oxide has a nickel content of 70 mol % or more based on the total mole number of transition metals in the lithium transition metal oxide.
6. The method according to claim 4, wherein the heat treatment temperature in the first firing step is 0.75-1.5 times of the heat treatment temperature in the second firing step.
7. The method according to claim 4, wherein the water-washing step comprises: mixing the fired product with water at a weight ratio of 50-200%; and agitating the mixture of fired product and water.
8. The method according to claim 4, wherein the first B source and the second B source are independently any one selected from the group consisting of H.sub.3BO.sub.3, H.sub.4BO.sub.4, B.sub.2O.sub.3, LiBO.sub.2, Li.sub.2B.sub.4O.sub.7, B.sub.4C, AlBO.sub.2 and AlB.sub.2O.sub.4, and a combination thereof.
9. The according to claim 4, wherein a weight of B in the positive active material is 200-5,000 ppm.
Description
DESCRIPTION OF DRAWINGS
[0021] The accompanying drawings illustrate a preferred embodiment of the present disclosure and together with the foregoing disclosure, serve to provide further understanding of the technical features of the present disclosure, and thus, the present disclosure is not construed as being limited to the drawing.
[0022]
[0023]
[0024]
BEST MODE
[0025] Hereinafter, preferred embodiments of the present disclosure will be described in detail with reference to the accompanying drawings. Prior to the description, it should be understood that the terms used in the disclosure and the appended claims should not be construed as limited to general and dictionary meanings, but interpreted based on the meanings and concepts corresponding to technical aspects of the present disclosure on the basis of the principle that the inventor is allowed to define terms appropriately for the best explanation. Therefore, the description proposed herein is just a preferable example for the purpose of illustrations only, not intended to limit the scope of the disclosure, so it should be understood that other equivalents and modifications could be made thereto without departing from the scope of the disclosure.
[0026] In the following description, reference will be made to the accompanying drawings forming a part of the present disclosure. The embodiments described in the detailed description, drawing and claims are not intended to be limiting of the present disclosure. Other embodiments and modifications may be made without departing from the scope of the present disclosure. The embodiments described generally herein and depicted in the drawings may be arranged, substituted, combined, separated and designed with various different constitutional elements. It will be understood that all of them are clearly considered herein.
[0027] Unless otherwise stated, all of the technological and scientific terms used herein have the same meanings as understood commonly by those skilled in the art to which the present disclosure belongs.
[0028] While the present disclosure will be described with respect to the specific embodiments, it will be apparent to those skilled in the art that various changes and modifications may be made without departing from the scope of the present disclosure. In addition to the above, it should be understood that other equivalents could be made without departing from the scope of the disclosure. Such modifications and changes also fall within the scope of the following claims. The scope of the present disclosure will be defined merely by the claims together with the whole range of equivalents qualified by the claims. It should be also understood that the present disclosure is not limited to particular embodiments which are variable. Further, it should be understood that the terminology used herein is for the purpose of describing particular embodiments only and is not intended to be limiting of the present disclosure.
[0029]
[0030] First, the first firing step of mixing a lithium source with a precursor and carrying out heat treatment is carried out (step S10).
[0031] A positive electrode active material for a lithium secondary battery is prepared through the first firing step (S10). For example, a NCM-based lithium transition metal composite oxide may be prepared. Preferably, the positive electrode active material prepared according to the present disclosure is a NCM-based lithium transition metal composite oxide, but a different type of positive electrode active material used for a lithium secondary battery may also be prepared according to the present disclosure.
[0032] The precursor is a starting material, and may be prepared by mixing and reacting an aqueous solution of nickel compound, cobalt compound, manganese compound, or the like, with an alkaline solution to obtain a precipitate as a reaction product, and drying and heat treating the precipitate. For example, the precursor may be represented by the following Chemical Formula 1:
Ni.sub.x1Co.sub.y1Mn.sub.z1Al.sub.s1(OH).sub.2[Chemical Formula 1]
[0033] wherein 0.7x10.99, 0<y1<0.3, 0<z1<0.3, and 0s10.1.
[0034] For example, the precursor may be one from which a Ni-rich lithium transition metal oxide is prepared, wherein the precursor may have a nickel content of 70 mol % or more based on the total mole number of transition metals.
[0035] The lithium source may be a lithium compound, such as Li.sub.2CO.sub.3 or LiOH.Math.H.sub.2O.
[0036] The fired product obtained through the first firing step (S10) may be a lithium transition metal composite oxide represented by the following Chemical Formula 2:
Li.sub.a[Ni.sub.bCo.sub.cMn.sub.dAl.sub.e].sub.1-fM.sup.1.sub.fO.sub.2[Chemical Formula 2]
[0037] wherein M.sup.1 represents at least one selected from the group consisting of Zr, W, Mg, Ce, Hf, Ta, La, Ti, Sr, Ba, F, P and S, 0.8a1.2, 0.7b0.99, 0<c<0.3, 0<d<0.3, 0.01e0.1, and 0f0.1.
[0038] For example, the lithium transition metal composite oxide may be LiNi.sub.0.86Co.sub.0.05Mn.sub.0.07Al.sub.0.02O.sub.2.
[0039] In the first firing step, no B source is mixed.
[0040] The heat treatment in the first firing step may be carried out at an oxygen concentration of 21-100%. The heat treatment temperature of the first firing step may be set to 0.75-1.5 times of the heat treatment temperature of the second firing step carried out after the first firing step. The heat treatment temperature may be varied suitably within the above-defined range depending on the content of each element in NCM. For example, the heat treatment in the first firing step may be carried out at 500-900 C. When the temperature is lower than 500 C., the reaction may not occur sufficiently. When the temperature is higher than 900 C., the positive electrode material may be thermally decomposed to cause degradation of performance.
[0041] Next, the second firing step of mixing the fired product obtained from the first firing step with the first B source and carrying out heat treatment to form a surface protective layer on the fired product is carried out (step S20). The heat treatment in the second firing step may be carried out by cooling the fired product after the heat treatment of the first firing step (step S10) and introducing the first B source to the fired product.
[0042] The method according to an embodiment of the present disclosure is characterized in that no B source is mixed in the first firing step (step S10), and then the B source is introduced subsequently twice in division. The first introduction time point is the second firing step (step S20). The B source introduced in the second firing step is referred to as the first B source.
[0043] The first B source is a coating/doping material, and may be any one selected from H.sub.3BO.sub.3, H.sub.4BO.sub.4, B.sub.2O.sub.3, LiBO.sub.2, Li.sub.2B.sub.4O.sub.7, B.sub.4C, AlBO.sub.2 and AlB.sub.2O.sub.4, or a combination thereof. The method for mixing the fired product obtained from the first firing step with the first B source may be carried out by a solid phase process or a liquid phase process. Such a solid phase of liquid phase process may include mixing, milling, spray drying, grinding, or the like. Preferably, a dry solid phase process is used.
[0044] The heat treatment in the second firing step may be carried out at an oxygen concentration of 21-100%. Similarly to the heat treatment in the first firing step, the heat treatment in the second firing step may be carried out at 500-900 C. When the heat treatment temperature is lower than 500 C., it is not possible to form a surface protective layer smoothly or homogeneously. When the heat treatment temperature is higher than 900 C., the positive electrode active material may not retain its original properties. The heat treatment temperature may be varied suitably within the above-defined range depending on the content of each element in NCM. However, as mentioned above, the heat treatment temperature in the first firing step is preferably 0.75-1.5 times of the heat treatment temperature of the second firing step. It is shown that when the heat treatment in the first firing step is not within the above-defined range, high-temperature life characteristics are degraded even after the first B source is added and firing, water-washing and coating are performed in the second firing step. Therefore, the condition of the relationship between the heat treatment temperature in the first firing step and the heat treatment temperature in the second firing step is critical, since it is required to prevent degradation of high-temperature life characteristics.
[0045] In brief, the method according to an embodiment of the present disclosure is characterized in that firing is not carried out at once but is carried out twice (the first firing step and the second firing step) in division. In addition, the B source is not added in the first firing step but is added in the second firing step. The B source as a coating/doping material is not introduced in the first firing step, but is introduced merely in the second firing step. The first B source introduced in the second firing step allows the fired product to be coated/doped with B element to form a surface protective layer. One part of the first B source is incorporated into the fired product to perform doping, while the other part of the first B source is disposed on the surface of the fired product to form a B source coating layer, which functions as the surface protective layer.
[0046] According to the related art, the B source is introduced merely in the final step after the completion of firing to carry out coating. According to the present disclosure, the B source is added in the second firing step at a time point different from the introduction time of the lithium source. In this manner, it is possible to obtain an effect of improving the reactivity of the B source with the positive electrode active material. The surface protective layer formed in the second firing step inhibits surface deterioration of the positive electrode active material in the subsequent water-washing step (S30). Therefore, it is to be noted that the surface protective layer is already formed on the surface of the fired product before carrying out the water-washing step (S30) according to the method of the present disclosure, thereby inhibiting surface deterioration of the positive electrode active material surface in the water-washing step (S30).
[0047] The fired product obtained through the second firing step (S20) may be a lithium transition metal composite oxide represented by the following Chemical Formula 3:
Li.sub.a[Ni.sub.bCo.sub.cMn.sub.dAl.sub.e].sub.1-f(B,M.sup.1).sub.fO.sub.2[Chemical Formula 3]
[0048] wherein M.sup.1 represents at least one selected from the group consisting of Zr, W, Mg, Ce, Hf, Ta, La, Ti, Sr, Ba, F, P and S, 0.8a1.2, 0.7b0.99, 0<c<0.3, 0<d<0.3, 0.01e0.1, and 0f0.1.
[0049] Then, a water-washing step of removing unreacted lithium remaining on the surface of the fired product obtained from the second firing step is carried out (step S30).
[0050] Since the positive electrode active material may include a lithium compound, such as LiOH, remaining thereon, such a water-washing step may be required. The water-washing step may be carried out by mixing the fired product with water at a weight ratio of 50-200% and carrying out agitation. During the washing, additives, such as LiOH and NaOH, may be introduced.
[0051] Since the surface protective layer is formed on the fired product of positive electrode active material by using a process of B element coating/doping in the second firing step, the B element coating layer formed during the firing may have an effect of inhibiting surface deterioration of the positive electrode active material that may occur in the water-washing step. As compared to the method of the related art in which the B source is introduced to carry out coating merely in the final step after the completion of firing, the method according to an embodiment of the present disclosure provides a significant effect of inhibiting surface deterioration of the positive electrode active material in the water-washing step. According to the related art, the surface of the fired product subjected to water-washing includes no surface protective layer as disclosed herein.
[0052] After that, a coating step of drying the washed product obtained from the water-washing step and carrying out heat treatment together with the second B source is carried out (step S40).
[0053] The B source is not mixed in the first firing step (step S10), but is added subsequently twice in division. The first introduction time point is the above-described second firing step (step S20), and the second introduction time point is the coating step (step S40). The B source introduced in the coating step is referred to as the second B source.
[0054] The second B source is a coating/doping material, and may be any one selected from H.sub.3BO.sub.3, H.sub.4BO.sub.4, B.sub.2O.sub.3, LiBO.sub.2, Li.sub.2B.sub.4O.sub.7, B.sub.4C, AlBO.sub.2 and AlB.sub.2O.sub.4, or a combination thereof. The method for mixing the water-washed and dried product with the second B source may be carried out by a solid phase process or a liquid phase process. Such a solid phase or liquid phase process may include mixing, milling, spray drying, grinding, or the like.
[0055] The heat treatment in the second firing step may be carried out at an oxygen concentration of 21-100%. The heat treatment in step S40 may be carried out at 200-400 C. When the heat treatment temperature is lower than 200 C., the positive electrode active material may not realize its capacity sufficiently. When the heat treatment temperature is higher than 400 C., high-temperature life characteristics may be degraded. Therefore, the heat treatment temperature in step S40 is preferably lower than 400 C.
[0056] The first source may be the same as or different from the second source. However, the content of the first B source and the second B source are in such levels that the weight ratio of B/positive electrode active material equals to 200-5,000 ppm.
[0057] When the weight ratio of B/positive electrode active material is smaller than 200 ppm, there is no effect of coating. When the weight ratio of B/positive electrode active material is larger than 5,000 ppm, an excessive amount of coating layer may be formed, which is not preferred in terms of capacity and resistance. When the washed and dried product is heat treated together with the second B source at low temperature, the reactivity of the positive electrode active material surface with B is varied, thereby improving the high-temperature life, resistance increase and low-temperature output characteristics. Since deterioration of the positive electrode active material surface is inhibited by the surface protective layer in the water-washing step (step S30), the reactivity of the second B source introduced in the coating step (S40) with the positive electrode active material surface is higher than the reactivity of the B source with the deteriorated positive electrode active material surface having no surface protective layer and subjected to water-washing.
[0058] The positive electrode active material that may be prepared by the above-described method according to the present disclosure has the following characteristics. The positive electrode active material according to the present disclosure includes a lithium boron compound coating layer on the surface of a powder of a positive electrode active material for a lithium secondary battery, wherein the coating layer shows a peak intensity ratio of two optional peaks in the spectrum of Time-of-Flight Secondary Ion Mass Spectrometry (ToF-SIMS), equal to the peak intensity ratio of the corresponding peaks of LiBO.sub.2 compound within a range of 50%.
[0059] The positive electrode active material according to the present disclosure may include a lithium boron compound coating layer on the surface of a powder of a positive electrode active material for a lithium secondary battery, wherein the coating layer may show a peak intensity ratio of two optional peaks in the spectrum of Time-of-Flight Secondary Ion Mass Spectrometry (ToF-SIMS), equal to the peak intensity ratio of the corresponding peaks of LiBO.sub.2 compound within a range of 50%.
[0060] For example, the positive electrode active material may be a NCM-based lithium transition metal composite oxide. Particularly, in the case of a Ni-rich lithium transition metal composite oxide having a nickel content of 70% or more, the reactivity with an electrolyte should be reduced in order to increase the stability under cycle operation environment. The positive electrode active material including the coating layer according to the present disclosure can reduce the reactivity with an electrolyte, and thus can reduce gas generation at high temperature.
[0061] The positive electrode active material including the coating layer according to the present disclosure provides improved high-temperature life, resistance increase and output characteristics.
[0062] Herein, the coating layer may show a peak intensity ratio of the peak having the highest intensity among the peaks detected at a mass of 156.85-156.95 to the peak having the highest intensity among the peaks detected at a mass of 153.05-153.15 of 4.350%, in the ToF-SIMS spectrum. The expression 4.350% refers to a range of 4.3-2.15 (50% of 4.3) to 4.3+2.15, i.e. 2.15 to 6.43.
[0063] In addition, the coating layer may show a peak intensity ratio of the peak having the highest intensity among the peaks detected at a mass of 182.85-182.95 to the peak having the highest intensity among the peaks detected at a mass of 179.05-179.15 of 9.950%, in the ToF-SIMS spectrum. The expression 9.950% refers to a range of 9.9-4.95 (50% of 9.9) to 9.9+4.95, i.e. 4.95 to 14.85.
[0064] In other words, the coating layer of the positive electrode active material according to the present disclosure shows peaks present in a specific mass range as determined by ToF-SIMS, wherein the peaks have a predetermined peak intensity ratio, and the peak intensity ratio is equal to the peak intensity ratio of the corresponding peaks in LiBO.sub.2 compound within a range of 50%. When the positive electrode active material is used for a positive electrode for a lithium secondary battery, it is possible to provide high output and high stability.
[0065] As a result, according to the present disclosure, it is possible to improve the high-temperature life, resistance increase and low-temperature output characteristics of a positive electrode active material by controlling the time point of B coating/doping during the firing step.
MODE FOR DISCLOSURE
[0066] Hereinafter, the present disclosure will be explained in more detail with reference to Examples.
Example
[0067] First, LiOH.Math.H.sub.2O used as a lithium source and Ni.sub.0.88Co.sub.0.05Mn.sub.0.07(OH).sub.2+Al(OH).sub.3 used as a precursor were used and mixed in such a manner that the molar ratio of Li:transition metals (Ni, Co, Mn, Al) may be 1.03:1, and the resultant mixture was subjected to the first firing step at 700 C. for 5 hours to obtain LiNi.sub.0.86Co.sub.0.05Mn.sub.0.07Al.sub.0.02O.sub.2 as the first fired product. Next, the first fired product was mixed with the first B source, H.sub.3BO.sub.3, at a weight ratio of 100:0.86, and the resultant mixture was subjected to the second firing step at 750 C. for 5 hours. The fired product was mixed with water at a weight ratio of 100:100, and agitation was carried out for 5 minutes. Then, the washed product was filtered by using a filter press and vacuum dried at 130 C. After that, the dried product was mixed with the second B source, H.sub.3BO.sub.3, at a weight ratio of 100:0.57, and the resultant mixture was heat treated at 300 C. for 4 hours to obtain a positive electrode active material surface-coated with B.
Comparative Example 1
[0068] LiOH-H.sub.2O used as a lithium source was mixed with Ni.sub.0.88Co.sub.0.05Mn.sub.0.07(OH).sub.2+Al(OH).sub.3 used as a precursor in such a manner that the molar ratio of Li:transition metals (Ni, Co, Mn, Al) may be 1.03:1, and the resultant mixture was subjected to the first firing step at 700 C. for 5 hours to obtain the first fired product of LiNi.sub.0.86Co.sub.0.05Mn.sub.0.07Al.sub.0.02O.sub.2. Next, no B source was added thereto, and the second firing step was carried out at 750 C. for 5 hours.
Comparative Example 2
[0069] LiOH-H.sub.2O used as a lithium source was mixed with Ni.sub.0.88Co.sub.0.05Mn.sub.0.07(OH).sub.2+Al(OH).sub.3 used as a precursor in such a manner that the molar ratio of Li:transition metals (Ni, Co, Mn, Al) may be 1.03:1, and the resultant mixture was subjected to the first firing step at 700 C. for 5 hours to obtain the first fired product of LiNi.sub.0.86Co.sub.0.05Mn.sub.0.07Al.sub.0.02O.sub.2. Next, no B source was added thereto, and the second firing step was carried out at 750 C. for 5 hours. The fired product was mixed with water at a weight ratio of 100:100, and the resultant mixture was agitated for 5 minutes. Then, the washed product was filtered through a filter press, and vacuum drying was carried out at 130 C. After that, the dried product was mixed with H.sub.3BO.sub.3 at a weight ratio of 100:0.57, and heat treatment was carried out at 300 C. for 4 hours.
Comparative Example 3
[0070] LiOH-H.sub.2O used as a lithium source was mixed with Ni.sub.0.88Co.sub.0.05Mn.sub.0.07(OH).sub.2+Al(OH).sub.3 used as a precursor in such a manner that the molar ratio of Li:transition metals (Ni, Co, Mn, Al) may be 1.03:1, the resultant mixture was mixed with Ni.sub.0.88Co.sub.0.05Mn.sub.0.07(OH).sub.2 and H.sub.3BO.sub.3 mixed at a weight ratio of 100:0.91, and then the first firing step was carried out at 700 C. for 5 hours, and the second firing step was carried out at 750 C. for 5 hours.
Comparative Example 4
[0071] LiOH-H.sub.2O used as a lithium source was mixed with Ni.sub.0.88Co.sub.0.05Mn.sub.0.07(OH).sub.2+Al(OH).sub.3 used as a precursor in such a manner that the molar ratio of Li:transition metals (Ni, Co, Mn, Al) may be 1.03:1, the resultant mixture was mixed with Ni.sub.0.88Co.sub.0.05Mn.sub.0.07(OH).sub.2 and H.sub.3BO.sub.3 mixed at a weight ratio of 100:0.91, and then the first firing step was carried out at 700 C. for 5 hours, and the second firing step was carried out at 750 C. for 5 hours. The fired product was mixed with water at a weight ratio of 100:100, and the resultant mixture was agitated for 5 minutes. Then, the washed product was filtered through a filter press, and vacuum drying was carried out at 130 C. After that, the dried product was mixed with H.sub.3BO.sub.3 at a weight ratio of 100:0.57, and heat treatment was carried out at 300 C. for 4 hours.
Comparative Example 5
[0072] LiOH-H.sub.2O used as a lithium source was mixed with Ni.sub.0.88Co.sub.0.05Mn.sub.0.07(OH).sub.2+Al(OH).sub.3 used as a precursor in such a manner that the molar ratio of Li:transition metals (Ni, Co, Mn, Al) may be 1.03:1, and the resultant mixture was subjected to the first firing step at 700 C. for 5 hours to obtain the first fired product of LiNi.sub.0.86Co.sub.0.05Mn.sub.0.07Al.sub.0.02O.sub.2. Then, the first fired product was mixed with H.sub.3BO.sub.3 at a weight ratio of 100:0.86, and the second firing step was carried out at 750 C. for 5 hours.
[0073] In brief, the above Example and Comparative Examples are as follows. [0074] Example: Li+NCM(OH).sub.2+Al mixing.fwdarw.700 C., the first firing step.fwdarw.positive electrode active material+the first B source mixing.fwdarw.750 C., the second firing step.fwdarw.water-washing.fwdarw.drying, 130 C..fwdarw.the second B source mixing and coating (300 C.) [0075] Comparative Example 1 (Positive electrode active material+no B source mixing, two-step firing): Li+NCM(OH).sub.2+Al mixing.fwdarw.700 C., the first firing step.fwdarw.750 C., the second firing step [0076] Comparative Example 2 (Positive electrode active material+no B source mixing, two-step firing): Li+NCM(OH).sub.2+Al mixing.fwdarw.700 C., the first firing step.fwdarw.750 C., the second firing step.fwdarw.water-washing.fwdarw.drying, 130 C..fwdarw.H.sub.3BO.sub.3 mixing and coating (300 C.) [0077] Comparative Example 3 (mixing lithium source with B source in the first firing step): Li+NCM(OH).sub.2+Al+H.sub.3BO.sub.3 mixing.fwdarw.700 C., the first firing step.fwdarw.750 C., the second firing step [0078] Comparative Example 4 (mixing lithium source with B source in the firing step): Li+NCM(OH).sub.2+Al+H.sub.3BO.sub.3 mixing.fwdarw.700 C., the first firing step.fwdarw.750 C., the second firing step.fwdarw.water-washing.fwdarw.drying, 130 C..fwdarw.H.sub.3BO.sub.3 mixing and coating (300 C.) [0079] Comparative Example 5: Li+NCM(OH).sub.2+Al mixing.fwdarw.700 C., the first firing step.fwdarw.positive electrode active material+H.sub.3BO.sub.3 mixing.fwdarw.750 C., the second firing step
[0080] The test items include a time change test, an electrochemical data of a coin half-cell, a low-temperature output data of a mono-cell, a high-temperature life data of a mono-cell, and determination of peaks detected upon the B source addition through Time-of-Flight Secondary Ion Mass Spectrometry (ToF-SIMS).
[0081] Results of Time-of-Flight Secondary Ion Mass Spectrometry (ToF-SIMS)
[0082] ToF-SIMS was carried out to identify the ingredients of the coating layer. In general, X-ray diffractometry (XRD) is used to determine the composition and crystal structure of a material. However, since the coating layer of the positive electrode active material has a thickness of several nanometers to several tens of nanometers, it is difficult to detect peaks by XRD. According to the present disclosure, a significantly thin coating layer were analyzed in terms of its ingredients through ToF-SIMS. After carrying out ToF-SIMS, it was shown that a lithium boron compound coating layer was formed additionally on the positive electrode active material surface. In other words, it was shown that a lithium boron compound was formed additionally by the method according to the present disclosure.
[0083]
[0084] Referring to
[0085] In Example, the peak intensity ratio of the peak detected at a mass of 156.9 to the peak detected at a mass of 153.1 is similar to the peak intensity ratio of the corresponding peak intensity (i.e. peak intensity ratio of peak 1 to peak 2 in LiBO.sub.2 compound) of LiBO.sub.2 compound within a range of 50%. The term similar means that the ratio of Example is the same as the ratio of LiBO.sub.2 within a range of 50%. In Comparative Examples 2 and 4, those peaks are observed in a different pattern. In Comparative Examples 2 and 4, the ratio of peak 1 to peak 2 is 0.3 and 2.0, respectively.
[0086] Referring to
[0087] In Example, the peak intensity ratio of the peak detected at a mass of 182.9 to the peak detected at a mass of 179.1 is similar to the peak intensity ratio of the corresponding peak intensity (i.e. peak intensity ratio of peak 3 to peak 4 in LiBO.sub.2 compound) of LiBO.sub.2 compound within a range of 50%. The term similar means that the ratio of Example is the same as the ratio of LiBO.sub.2 within a range of 50%. In Comparative Examples 2 and 4, those peaks are observed in a different pattern. In comparative Examples 2 and 4, the ratio of peak 3 to peak 4 is 1.5 and 3.0, respectively.
[0088] According to the present disclosure, it can be seen that since the lithium boron compound having the above-mentioned peak intensity ratio characteristics is incorporated to the coating layer, high-temperature life characteristics and low-temperature output characteristics are improved.
[0089] Method for Evaluating Characteristics of Coin Half-Cell
[0090] Each of the positive electrode active materials according to Example and Comparative Examples 1-5, carbon black as a conductive material and PVDF as a binder were mixed in N-methyl pyrrolidone as a solvent at a weight ratio of 96:2:2 to prepare a positive electrode slurry. The positive electrode slurry was applied onto one surface of an aluminum current collector, dried at 130 C. and pressed to obtain a positive electrode. Lithium metal was used as a negative electrode. Then, a porous polyethylene separator was interposed between the positive electrode and the negative electrode to provide an electrode assembly, which, in turn, was received in a casing, and an electrolyte was injected into the casing to obtain a lithium secondary battery.
[0091] Herein, the electrolyte was prepared by dissolving 1.0 M of lithium hexafluorophosphate (LiPF.sub.6) in an organic solvent including ethylene carbonate/ethyl methyl carbonate/diethyl carbonate (EC/MC/DEC) mixed at a volume ratio of 3/4/3.
[0092] Each of the lithium secondary battery half-cell was charged at 0.1 C to 4.25 V at 25 C. in a constant current-constant voltage (CC-CV) mode, and discharged at a constant current of 0.1 C to 3.0 V to carry out a charge/discharge test. In the test, the charge capacity, discharge capacity, efficiency and direct current internal resistance (DCIR) were determined.
[0093] Method for Evaluating Characteristics of Mono-Cell
[0094] Each a positive electrode active material, a conductive material, a binder and an additive were mixed at a ratio of 97.5/1.0/1.35/0.15 to prepare a positive electrode slurry. The positive electrode slurry was coated on an aluminum current collector, and natural graphite was mixed with artificial graphite at a specific ratio to prepare a negative counter electrode. An electrolyte was prepared at a salt concentration of 0.7 M, and lithium bis(fluorosulfonyl)imide (LiFSI, 0.3 M) was added thereto in order to maintain the life. The electrolyte was injected in an amount of 100 L, and a separator manufactured by our own company and prepared with an adequate size was interposed between the positive electrode and the negative electrode. The electrolyte was injected to the prepared mono-cell, charge/discharge cycles were carried out, and the initial gases were removed to prepare evaluation of the mono-cell.
[0095] The charge/discharge cycles were carried out at a temperature of 25 C. When the initial capacity was completed, the mono-cell was determined in terms of a drop in voltage (A voltage) and resistance, while being discharged at 10 C. and at 2.0 C from SOC 10 to 0. To determine the high-temperature life characteristics, each mono-cell was charged at 45 C. in a constant current mode at 0.5 C to 4.2 V, discharged at a constant current of 1.0 C to 3.0 V, charged at a constant current of 0.33 C to 4.2 V at 25 C. when each of the 100.sup.th, 200.sup.th, 300.sup.th and 400.sup.th cycles reached, and discharged at a constant current of 0.33 C to 3.0 V to carry out a charge/discharge test, and the capacity retention and an increase in resistance were measured.
[0096] Test Results
[0097] The fired product of each positive electrode active material was determined in terms of improvement of a change with time. The change with time was evaluated as a change in Li.sub.2CO.sub.3 weight remaining on the surface. Table 1 shows the results of the time change test of Comparative Examples 1 and 5, wherein the weight ratio of Li.sub.2CO.sub.3/fired product was measured on the first day (0 day), after 1 day (1 day), after 2 days (2 day) and after 3 days (3 day).
TABLE-US-00001 TABLE 1 Weight ratio of Li.sub.2CO.sub.3/fired product Time change 0 day 1 day 2 day 3 day Comp. Ex. 1 0.633 0.864 1.012 1.081 Comp. Ex. 5 0.445 0.602 0.679 0.696
[0098] Referring to Table 1, Comparative 5 shows a smaller change with time as compared to Comparative Example 1. Therefore, it can be seen that Comparative Example 5 in which the second firing step is carried out with the B source added thereto provides a better result in terms of a change with time, as compared to Comparative Example 1 with no B source added thereto. According to the present disclosure, the second firing step is carried out with the B source added, and thus it is possible to accomplish improvement in terms of a change with time.
[0099] Table 2 shows the electrochemical data including the charge capacity, discharge capacity, efficiency and DCIR of each coin half-cell.
TABLE-US-00002 TABLE 2 25 C. 0.1 C/0.1 C Electrochemical data Charge Discharge of coin half-cell capacity capacity Efficiency DCIR Example 231.5 212.3 91.7 19.3 Comp. Ex. 2 230.0 207.9 90.4 19.7 Comp. Ex. 4 230.4 207.8 90.2 20.8
[0100] Referring to Table 2, Example according to the present disclosure shows a higher charge capacity, discharge capacity and efficiency, and a lower DCIR, as compared to Comparative Example 2 or 4.
[0101] Comparative Example 2 includes two-step firing, but no B source is mixed in the second firing step, unlike the present disclosure. Comparative Example 2 includes mixing the B source in the first firing step, not in the second firing step, unlike the present disclosure. Therefore, when the B source is not mixed in the first firing step but mixed in the second firing step according to the present disclosure, it is possible to improve the charge capacity, discharge capacity, efficiency and DCIR. As a result, it can be seen that it is possible to reduce the surface resistance of the positive electrode active material in the positive electrode of a lithium secondary battery by using the method according to the present disclosure. Particularly, in the case of Comparative Example 4 wherein the B source is introduced in the firing step, it can be seen that the positive electrode active material cannot realize its capacity but causes an increase in DCIR undesirably.
[0102] Table 3 shows the low-temperature output data of a mono-cell.
TABLE-US-00003 TABLE 3 Discharge at 10 C./2.0 C. Low- 0-10 sec 0-1350 sec temperature Percentage* Percentage* output data of of of mono- Resistance resistance Resistance resistance cell Voltage () (%) Voltage () (%) Example 0.212 27.107 11 0.263 33.58 10.5 Comp. Ex. 0.242 30.463 0 0.298 37.52 0 2
[0103] Referring to Table 3, Example according to the present disclosure shows improved output characteristics, including a drop in voltage (voltage) and resistance, as compared to Comparative Example 2.
[0104] Comparative Example 2 includes two-step firing, but the B source is not mixed in the second firing step, unlike the present disclosure. Therefore, when the B source is not mixed in the first firing step but mixed in the second according to the present disclosure, it is possible to improve the low-temperature output characteristics.
[0105] Table 4 shows data of high-temperature life of a mono-cell, including capacity retention and an increase in resistance, as determined every 100.sup.th cycle, and
TABLE-US-00004 TABLE 4 High- 25 C. 0.33 C./0.33 C. temperature 100.sup.th cycle 200.sup.th cycle 300.sup.th cycle 400.sup.th cycle life data of Capacity Increase in Capacity Increase in Capacity Increase in Capacity Increase in mono-cell retention resistance retention resistance retention resistance retention resistance Example 96.35 14.81 93.07 31.83 90.74 40.99 89.20 53.11 Comp. Ex. 2 95.82 18.52 92.16 37.09 89.62 45.70 87.81 56.31 Comp. Ex. 4 96.57 14.14 92.66 33.15 89.69 45.92 87.11 60.30
[0106] Referring to Table 4 and
[0107] Therefore, when the B source is not mixed in the first firing step but mixed in the second according to the present disclosure, it is possible to improve the high-temperature life characteristics. When putting the above results together, it can be seen that the coated positive electrode active material provides improved characteristics by carrying out the firing process in two steps and introducing the B source and lithium source at a different time point to improve the reactivity of the B source with the positive electrode active material.
[0108] The present disclosure has been described in detail with reference to specific Examples and drawings. However, it should be understood that the detailed description and specific examples are given by way of illustration only, since various changes and modifications within the scope of the disclosure will become apparent to those skilled in the art from this detailed description.