Positive electrode active material precursor for lithium secondary battery, positive electrode active material manufactured by using thereof, and lithium secondary battery including same
10283757 ยท 2019-05-07
Assignee
- IUCF-HYU (INDUSTRY-UNIVERSITY COOPERATION FOUNDATION HANYANG UNIVERSITY) (Seoul, KR)
- ENERCERAMIC INC. (Seoul, KR)
Inventors
Cpc classification
H01M4/13
ELECTRICITY
Y02P70/50
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
H01M4/525
ELECTRICITY
C01G53/50
CHEMISTRY; METALLURGY
C01P2002/80
CHEMISTRY; METALLURGY
C01G53/006
CHEMISTRY; METALLURGY
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
H01M2004/021
ELECTRICITY
International classification
H01M4/13
ELECTRICITY
H01M4/131
ELECTRICITY
H01M4/525
ELECTRICITY
H01M10/0525
ELECTRICITY
Abstract
The present disclosure relates to a positive electrode active material precursor for a lithium secondary battery, a positive electrode active material manufactured by using thereof, and a lithium secondary battery comprising the same. More specifically, it relates to a positive electrode active material precursor for a lithium secondary battery as a secondary particle comprising transition metals, and formed by gathering of a plurality of primary particles having different a-axis direction length to c-axis direction length ratio, wherein the a-axis direction length to c-axis direction length ratio of the primary particle making up the secondary particle is increased from the center to the surface of the secondary particle; a positive electrode active material; and a lithium secondary battery comprising the same.
Claims
1. A positive electrode active material for a lithium secondary battery, which is a secondary particle comprising transition metals, wherein the secondary particle comprises a plurality of primary particles, wherein the primary particles have a crystal structure that has an a-axis and a c-axis, wherein the a-axis direction is a direction from a center to a surface of the secondary particle, and the c-axis direction is perpendicular to the a-axis direction, wherein the secondary particle comprises the primary particles having the a-axis direction length to the c-axis direction length ratios different from each other, wherein the a-axis orientation of the primary particles is headed to the center of the secondary particle, and the primary particles are adjoining each other and align with the a-axis direction, and wherein the a-axis and the c-axis are defined by a diffraction pattern of Fast Fourier Transform from a TEM image of the primary particles.
2. The positive electrode active material for a lithium secondary battery according to claim 1, wherein at least one metal has concentration gradient in the secondary particle.
3. The positive electrode active material for a lithium secondary battery according to claim 1, wherein the primary particles comprise Ni.
4. The positive electrode active material for a lithium secondary battery according to claim 1, wherein at least one metal in a first interior has constant concentration, and wherein at least one metal in a second interior has concentration gradient.
5. The positive electrode active material for a lithium secondary battery according to claim 1, wherein the a-axis direction length to the c-axis direction length ratios of the primary particles are sequentially increased from a center to a surface of the secondary particle.
6. The positive electrode active material for a lithium secondary battery according to claim 1, wherein the primary particles comprise at least two of Ni, Co, or Mn, and wherein at least one of Ni, Co, or Mn has concentration gradient in the secondary particle.
7. The positive electrode active material for a lithium secondary battery according to claim 6, wherein Ni concentration of the center of the secondary particle is higher than Ni concentration of a surface of the secondary particle.
8. The positive electrode active material for a lithium secondary battery according to claim 6, wherein the secondary particle comprises a first primary particle adjacent to the center of the secondary particle and a second primary particle adjacent to the surface of the secondary particle, and wherein average Ni concentration of the first primary particle is higher than average Ni concentration of the second primary particle.
9. A positive electrode active material for a lithium secondary battery, which is a secondary particle comprising transition metals, wherein the secondary particle comprises a plurality of primary particles, wherein the plurality of the primary particles provide lithium ion path headed to the center of the secondary particle, wherein a crystal structure of the primary particles has an a-axis and a c-axis, wherein the a-axis direction is a direction from a center to a surface of the secondary particle, and the c-axis direction is perpendicular to the a-axis direction, and wherein the a-axis and the c-axis are defined by a diffraction pattern of Fast Fourier Transform from a TEM image of the primary particles.
10. A positive electrode active material for a lithium secondary battery, which is a secondary particle comprising transition metals, wherein the secondary particle comprises a plurality of primary particles, wherein the secondary particle comprises at least one of Ni, Co, or Mn, wherein at least one metal in the primary particles has concentration gradient, wherein a crystal structure of the primary particles has an a-axis and a c-axis, wherein the a-axis direction is a direction from a center to a surface of the secondary particle, and the c-axis direction is perpendicular to the a-axis direction, and wherein the a-axis and the c-axis are defined by a diffraction pattern of Fast Fourier Transform from a TEM image of the primary particles.
11. The positive electrode material for a lithium secondary battery according to claim 10, wherein at least one metal in the primary particles has continuous concentration gradient in the primary particles from a center of the secondary particle to a surface of the secondary particle.
12. The positive electrode material for a lithium secondary battery according to claim 10, wherein the secondary particle comprises Ni, and Ni in the primary particles has concentration gradient in the primary particles.
Description
BRIEF DESCRIPTION OF DRAWINGS
(1) The above and other objects and features of the present invention will become apparent from the following description of the invention taken in conjunction with the following accompanying drawings, which respectively show:
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DETAILED DESCRIPTION OF THE INVENTION
(15) Hereinafter, the present invention now will be described in detail with reference to the accompanying drawings.
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(17) As shown in
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(19) In one embodiment of the present invention as shown in
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(21) In one embodiment of the present invention, the primary particle of the first interior is characterized that the a-axis direction length to c-axis direction length ratio of the primary particle of the first interior may be 0.5 to 2.0, and the a-axis direction length to c-axis direction length ratio of the primary particle of the second interior may be 2 to 30.
(22) Namely, the positive electrode active material for a lithium secondary battery 100 according to one embodiment of the present invention is characterized that primary particles of relatively circular type having width and length of 0.8 to 1.2 are formed in the interior, and primary particles having increased aspect ratio as going to the surface are agglutinated. In the present invention, the a-axis direction length to c-axis direction length ratio is highly increased in the second interior, compared with the first interior.
(23) In one embodiment of the present invention, it is characterized that the a-axis direction length of the primary particle is in the range of 0.01 to 0.95 of the secondary particle radius. In the present invention, the primary particles are adjoined each other and grow to a fixed route, but in the range thereof, it is preferred that the a-axis direction length of the primary particle is in the range of 0.01 to 0.95 of the secondary particle radius.
(24) In one embodiment of the present invention, it is characterized that the first interior of the secondary particle of the positive electrode active material for a lithium secondary battery is expressed by an empirical formula of Li.sub.[Ni.sub.1(a+b+c)Co.sub.aMn.sub.bM.sub.c]O.sub.2 (1.01.2, 0.00a0.40, 0.00b0.35, 0.00c0.05, 0.05a+b+c0.5), and the secondary interior of the secondary particle of the positive electrode active material for a lithium secondary battery is expressed by an empirical formula of Li.sub.[Ni.sub.1(x+y+z)Co.sub.xMn.sub.yM.sub.z]O.sub.2 (1.01.2, 0.07x0.3, 0.2y0.5, 0.00z0.1, 0.3x+y+z0.7), wherein M is at least one selected from the group consisting elements Al, Mg, Fe, Cr, V, Ti, Mo, Sc, Ce and La. Namely, in one embodiment of the present invention, the positive electrode active material for a lithium secondary battery is characterized by high Ni content in the first interior, and low Ni content and high Mn content in the second interior.
(25) In the positive electrode active material according to the present invention, the secondary particle of the positive electrode active material for a lithium secondary battery is characterized that oxidation numbers, +2 and +3, of Ni are mixed from the particle surface to the part having radius 0.1 to 0.7 time of the particle radius, i.e., at the part where the active material particles are directly contacted to an electrolyte solution. In accordance with mixing the oxidation numbers of Ni, higher oxidation number than the average oxidation number of Ni used in the existing positive electrode active material is maintained, and electric charge also becomes higher as the oxidation number of Ni becomes higher, thereby Coulomb force between the transition metal atom and oxygen is also increased. Accordingly, a stable binding structure and higher binding force between the transition metal atom and oxygen can be obtained.
(26) In one embodiment of the present invention, it is characterized that at least one metal making up the primary particle of the positive electrode active material for a lithium secondary battery shows continuous concentration gradient in the primary particle, and particularly, at least one metal making up the primary particle existing in the second interior of the secondary particle shows continuous concentration gradient in the primary particle itself.
(27) In the present invention, the positive electrode active material for a lithium secondary battery grows while also showing continuous concentration gradient inside of the primary particle. Further, the a-axis orientation of the primary particle is headed to the center of the positive electrode active material as a secondary particle, and the particles are adjoining each other and grow to a fixed route.
EXAMPLE
(28) Hereinafter, Examples and Comparative Example will be described. The Examples are presented for illustrative purposes only, and do not limit the present invention.
(29) Distilled water 4 liter was poured into a coprecipitation reactor (Volume: 4 L, Power of a rotary motor: 80 W or more), and then nitrogen gas was supplied into the reactor at the rate of 0.5 liter/min to remove dissolved oxygen followed by stirring at 1000 rpm while keeping the reactor temperature at 50 C.
(30) In order to make the Mn concentration in the entire particle constant as 0.25 and concentration gradients of Co and Ni transition metal ions, first of all, 2.4 M metal aqueous solution, wherein nickel sulfate, cobalt sulfate and manganese sulfate are mixed at the molar ratio of 75:0:25 was continuously put into the reactor at the rate of 0.3 liter/hour, and 4.8 mol ammonia solution was continuously put into the reactor at the rate of 0.03 liter/hour. Further, for adjusting pH, 4.8 mol sodium hydroxide solution was supplied thereto to keep pH at 11. Impeller speed was controlled to 1000 rpm. Average retention time of the resulting solution in the reactor became about 6 hours by controlling flow rate. After fixing the volume of the metal aqueous solution of nickel sulfate, cobalt sulfate and manganese sulfate, which was supplied, to 4 L at the time when the particle size of the composite metal hydroxide became 2-5 m, concentration was changed until the molar ratio of nickel sulfate, cobalt sulfate and manganese sulfate of the metal aqueous solution became from 75:0:25 to 55:20:25, and the reaction was continued with the changing metal aqueous solution. The metal composite hydroxide was filtered and washed with water followed by drying in a 110 C. hot air dryer for 15 hours, thereby a metal composite hydroxide as a positive electrode active material precursor was manufactured.
(31) The metal composite hydroxide manufactured as described above and lithium hydroxide (LiOH) were mixed at the molar ratio of 1:1.07, heated at the rate of 2 C./min, and then kept at 500 C. for 10 hours for conducting pre-calcination. Then, the resulting material was calcined at 780 C. for 20 hours to obtain positive electrode active material powder of Example 1-1, wherein the first interior was constant as Li[Ni.sub.0.75Mn.sub.0.25]O.sub.2, and in the second interior, the Mn concentration was maintained as 0.25 from Li[Ni.sub.0.75Mn.sub.0.25]O.sub.2 to Li[Ni.sub.0.55Co.sub.0.20Mn.sub.0.25]O.sub.2, and Ni and Co have continuous constant concentration gradient in the entire particle, and average concentration in the particle was expressed by Li(Ni.sub.0.60Co.sub.0.15Mn.sub.0.25)O.sub.2.
(32) The procedure of Example 1-1 was repeated except for continuing the reaction as maintaining the said molar ratio when the molar ratio of the metal aqueous solution reached 55:20:25 during the particle forming process for further comprising a surface maintaining sections having thickness of 0.2 m, 0.5 m and 1.0 m, respectively, so as to obtain spherical nickel-manganese-cobalt composite hydroxides of Examples 1-2 to 1-4 containing the second interior having concentration gradient and a surface maintaining section.
Comparative Example 1
(33) Particles having constant metal ion concentration expressed by Li(Ni.sub.0.60Co.sub.0.15Mn.sub.0.25)O.sub.2 in the entire particle were manufactured.
(34) Approximate centers of the precursors and the active material particles manufactured in Example 1-1, Example 1-3 and Example 1-4, and the powder manufactured in Comparative Example 1 were cut with a hydrogen ion beam, and samples for measurement were prepared. Then, TEM images of each sample were taken, and the results were shown in
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(39) Batteries were manufactured by using the active material particle powders manufactured in Examples 1-1 to 1-4, and then capacity, life time characteristic and DSC characteristic were measured. The results were shown in the following Table 1.
(40) As shown in the following Table 1, it was confirmed that the batteries using Examples 1-1 to 1-4 having concentration gradient showed improved capacity, life time characteristic and DSC characteristic, compared with the battery using Comparative Example not showing concentration gradient, and in particular, the life time characteristic and the DSC characteristic were improved as the thickness of the surface maintaining section was increased.
(41) TABLE-US-00001 TABLE 1 Capacity Life Time Characteristic DSC (mAhg.sup.1) (%, 100.sup.th) ( C.) Example 1-1 193.0 94.5 277.3 Example 1-2 191.1 95.2 280.1 Example 1-3 188.2 96.1 287.2 Example 1-4 184.8 97.3 294.7 Comparative 181.3 93.9 266.3 Example 1
(42) In order to make the Mn concentration in the entire particle constant as 0.3 and concentration gradients of Co and Ni, first of all, 2.4 M metal aqueous solution, wherein nickel sulfate, cobalt sulfate and manganese sulfate are mixed at the molar ratio of 70:0:30, was used, and then the procedure of Example 1 was repeated except for continuing the reaction by using the metal aqueous solution whose concentration was changing until the concentration became 50:20:30 to obtain a precursor and an active material of Example 2-1.
(43) The procedure of Example 2-1 was repeated except for continuing the reaction as maintaining the said molar ratio when the molar ratio of the metal aqueous solution reached 50:20:30 during the composite particle forming process for further comprising a surface maintaining sections having thickness of 0.5 m, so as to obtain a precursor and an active material of Example 2-2.
(44) Approximate center of the active material particle powder manufactured in Example 2-2 was cut with a hydrogen ion beam, and a sample for measurement was prepared. Then, TEM images were taken.
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(46) Batteries were manufactured by using the active material particle powders manufactured in Examples 2-1 to 2-2, and then capacity, life time characteristic and DSC characteristic were measured. The results were shown in the following Table 2.
(47) As shown in the following Table 2, it was confirmed that the batteries using Examples 2-1 to 2-2 showed improved capacity, life time characteristic and DSC characteristic, and in particular, the life time characteristic and the DSC characteristic were improved as the thickness of the surface maintaining section was increased.
(48) TABLE-US-00002 TABLE 2 Capacity Life Time Characteristic DSC (mAhg.sup.1) (%, 100.sup.th) ( C.) Example 2-1 183.9 96.2 291.8 Example 2-2 182.3 97.0 295.3
(49) In order to make the Co concentration in the entire particle constant as 0.1 and concentration gradients of Ni and Mn, first of all, 2.4 M metal aqueous solution, wherein nickel sulfate, cobalt sulfate and manganese sulfate are mixed at the molar ratio of 85:10:05, was used, and then the procedure of Example 1 was repeated except for continuing the reaction by using the metal aqueous solution whose concentration was changing until the concentration became 60:10:30 to obtain a positive electrode active material precursor and a positive electrode active material, thereby obtaining a positive electrode active material powder of Example 3-1.
(50) The procedure of Example 3-1 was repeated except for continuing the reaction as maintaining the said molar ratio when the molar ratio of the metal aqueous solution reached 60:10:30 during the composite particle forming process for further comprising a surface maintaining sections having thickness of 0.2 m and 0.5 m, respectively, so as to obtain spherical nickel-manganese-cobalt composite hydroxide precursors of Examples 3-2 and 3-3 containing the second interior having concentration gradient and a surface maintaining section.
(51) TEM images of the cross-sections of the nickel-manganese-cobalt composite hydroxide precursors and the positive electrode active material of Examples 3-2 to 3-3 were taken, and the results were shown in
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Comparative Example 2
(53) Particles having constant metal ion concentration expressed by Li(Ni.sub.0.65Co.sub.0.10Mn.sub.0.25)O.sub.2 in the entire particle were manufactured, and the cross-sectional TEM image thereof was shown in
(54) Batteries were manufactured by using the active material particle powders manufactured in Examples 3-1 to 3-3, and then capacity, life time characteristic and DSC characteristic were measured. The results were shown in the following Table 3.
(55) As shown in the following Table 3, it was confirmed that the batteries using Examples 3-1 to 3-3 having concentration gradient showed improved capacity, life time characteristic and DSC characteristic, compared with the battery using Comparative Example 2 not showing concentration gradient, and in particular, the life time characteristic and the DSC characteristic were improved as the thickness of the surface maintaining section was increased.
(56) TABLE-US-00003 TABLE 3 Capacity Life Time Characteristic DSC (mAhg.sup.1) (%, 100.sup.th) ( C.) Example 3-1 197.1 94.5 270.3 Example 3-2 196.0 95.2 273.5 Example 3-3 194.8 96.1 278.1 Comparative 185.8 91.8 261.2 Example 2
(57) In order to make the Ni concentration in the entire particle constant as 0.8 and concentration gradients of Co and Mn, first of all, nickel sulfate, cobalt sulfate and manganese sulfate were mixed at the molar ratio of 80:20:00, and then the procedure of Example 1 was repeated except for continuing the reaction by using the metal aqueous solution whose concentration was changing until the concentration became 80:01:19 to obtain a positive electrode active material powder of Example 4-1, wherein the first interior had concentration of Li[Ni.sub.0.80Co.sub.0.20]O.sub.2 and the second interior had constant continuous concentration gradient from Li[Ni.sub.0.80Co.sub.0.20]O.sub.2 to Li[Ni.sub.0.80Co.sub.0.01Mn.sub.0.19]O.sub.2.
(58) The procedure of Example 4 was repeated except for continuing the reaction as maintaining the said molar ratio when the molar ratio of the metal aqueous solution reached 80:01:19 during the composite particle forming process for further comprising a surface maintaining sections having thickness of 0.2 m and 0.5 m, respectively, so as to obtain spherical nickel-manganese-cobalt composite hydroxides of Examples 4-2 and 4-3 containing the second interior having concentration gradient and a surface maintaining section.
(59) TEM images of the cross-sections of the nickel-manganese-cobalt composite hydroxide precursor and the positive electrode active material of Example 4-3 were taken, and the results were shown in
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Comparative Example 3
(61) Particles having constant metal ion concentration expressed by Li(Ni.sub.0.65Co.sub.0.10Mn.sub.0.25)O.sub.2 in the entire particle were manufactured.
(62) In order to make the Ni concentration in the entire particle constant as 0.75 and concentration gradients of Co and Mn as Example 5-1, first of all, nickel sulfate, cobalt sulfate and manganese sulfate were mixed at the molar ratio of 75:25:00, and then the procedure of Example 1 was repeated except for continuing the reaction by using the metal aqueous solution whose concentration was changing until the concentration became 75:02:23 to obtain a positive electrode active material powder, wherein the first interior had concentration of Li[Ni.sub.0.75Co.sub.0.25]O.sub.2 and the second interior had constant continuous concentration gradient from Li[Ni.sub.0.75Co.sub.0.25]O.sub.2 to Li[Ni.sub.0.75Co.sub.0.02Mn.sub.0.23]O.sub.2.
(63) The procedure of Example 4 was repeated except for continuing the reaction as maintaining the said molar ratio when the molar ratio of the metal aqueous solution reached 75:02:23 during the composite particle forming process for further comprising a surface maintaining sections having thickness of 0.2 m and 0.5 m, respectively, so as to obtain spherical nickel-manganese-cobalt composite hydroxides of Examples 5-2 and 5-3 containing the second interior having concentration gradient and a surface maintaining section.
(64) In order to make the Ni concentration in the entire particle constant as 0.70 and concentration gradients of Co and Mn as Example 6, first of all, nickel sulfate, cobalt sulfate and manganese sulfate were mixed at the molar ratio of 70:30:00, and then the procedure of Example 1 was repeated except for continuing the reaction by using the metal aqueous solution whose concentration was changing until the concentration became 70:02:28 to obtain a positive electrode active material powder, wherein the first interior had concentration of Li[Ni.sub.0.70Co.sub.0.30]O.sub.2 and the second interior had constant continuous concentration gradient up to Li[Ni.sub.0.70Co.sub.0.02Mn.sub.0.28]O.sub.2.
(65) The procedure of Example 4 was repeated except for continuing the reaction as maintaining the said molar ratio when the molar ratio of the metal aqueous solution reached 70:02:28 during the composite particle forming process for further comprising a surface maintaining sections having thickness of 0.2 m and 0.5 m, respectively, so as to obtain spherical nickel-manganese-cobalt composite hydroxides of Examples 6-2 and 6-3 containing the second interior having concentration gradient and a surface maintaining section.
(66) In order to make the Ni concentration in the entire particle constant as 0.65 and concentration gradients of Co and Mn as Example 7, first of all, nickel sulfate, cobalt sulfate and manganese sulfate were mixed at the molar ratio of 65:35:00, and then the procedure of Example 1 was repeated except for continuing the reaction by using the metal aqueous solution whose concentration was changing until the concentration became 65:02:33 to obtain a positive electrode active material powder, wherein the first interior had concentration of Li[Ni.sub.0.65Co.sub.0.35]O.sub.2 and the second interior had constant continuous concentration gradient up to Li[Ni.sub.0.65Co.sub.0.02Mn.sub.0.33]O.sub.2.
(67) The procedure of Example 4 was repeated except for continuing the reaction as maintaining the said molar ratio when the molar ratio of the metal aqueous solution reached 65:02:33 during the composite particle forming process for further comprising a surface maintaining sections having thickness of 0.2 m and 0.5 m, respectively, so as to obtain spherical nickel-manganese-cobalt composite hydroxides of Examples 7-2 and 7-3 containing the second interior having concentration gradient and a surface maintaining section.
Comparative Example 4
(68) Particles having constant metal ion concentration expressed by Li(Ni.sub.0.62Co.sub.0.15Mn.sub.0.23)O.sub.2 in the entire particle were manufactured.
(69) Batteries were manufactured by using the active material particle powders, which were manufactured in Examples 4 to 7 and had constant Ni concentration and concentration gradients of Co and Mn in the entire particle, and then capacity, life time characteristic and DSC characteristic were measured. The results were shown in the following Table 4.
(70) As shown in the following Table 4, it was confirmed that the batteries using Examples 4 to 7 having concentration gradient showed improved capacity, life time characteristic and DSC characteristic, compared with the battery using Comparative Example 4 not showing concentration gradient, and in particular, the life time characteristic and the DSC characteristic were improved as the thickness of the surface maintaining section was increased.
(71) TABLE-US-00004 TABLE 4 Capacity Life Time Characteristic DSC (mAhg.sup.1) (%, 100.sup.th) ( C.) Example 4 211.3 86.1 244.7 Example 4-2 210.8 86.8 245.5 Example 4-3 209.7 87.2 247.1 Example 5 205.6 91.0 256.5 Example 5-2 204.7 91.7 258.8 Example 5-3 203.9 92.5 260.1 Example 6 200.8 92.9 266.9 Example 6-2 199.8 93.5 268.2 Example 6-3 198.5 94.2 270.0 Example 7 195.7 94.3 275.1 Example 7-2 195.2 94.9 275.9 Example 7-3 194.5 95.7 277.2 Comparative 200.9 53.2 229.9 Example 4
(72) In order to make the Ni concentration in the entire particle constant as 0.9 and concentration gradients of Co and Mn as Example 8, first of all, nickel sulfate, cobalt sulfate and manganese sulfate were mixed at the molar ratio of 90:10:00, and then the procedure of Example 1 was repeated except for continuing the reaction by using the metal aqueous solution whose concentration was changing until the concentration became 90:01:09 to obtain a positive electrode active material powder, wherein the first interior had concentration of Li[Ni.sub.0.90Co.sub.0.10]O.sub.2 and the second interior had constant continuous concentration gradient up to Li[Ni.sub.0.90Co.sub.0.01Mn.sub.0.09]O.sub.2.
(73) In order to make the Ni concentration in the entire particle constant as 0.6 and concentration gradients of Co and Mn as Example 9, first of all, nickel sulfate, cobalt sulfate and manganese sulfate were mixed at the molar ratio of 60:40:00, and then the procedure of Example 1 was repeated except for continuing the reaction by using the metal aqueous solution whose concentration was changing until the concentration became 60:02:38 to obtain a positive electrode active material powder of Example 9-1, wherein the first interior had concentration of Li[Ni.sub.0.60Co.sub.0.40]O.sub.2 and the second interior had constant continuous concentration gradient up to Li[Ni.sub.0.60Co.sub.0.02Mn.sub.0.38]O.sub.2.
(74) Further, first of all, nickel sulfate, cobalt sulfate and manganese sulfate were mixed at the molar ratio of 60:20:20, and then the procedure of Example 1 was repeated except for continuing the reaction by using the metal aqueous solution whose concentration was changing until the concentration became 60:02:38 to obtain a positive electrode active material powder of Example 9-2, wherein the first interior had concentration of Li[Ni.sub.0.60Co.sub.0.20Mn.sub.0.20]O.sub.2 and the second interior had constant continuous concentration gradient up to Li[Ni.sub.0.60Co.sub.0.02Mn.sub.0.38]O.sub.2.
(75) In order to make the Ni concentration in the entire particle constant as 0.5 and concentration gradients of Co and Mn as Example 10, first of all, nickel sulfate, cobalt sulfate and manganese sulfate were mixed at the molar ratio of 50:50:00, and then the procedure of Example 1 was repeated except for continuing the reaction by using the metal aqueous solution whose concentration was changing until the concentration became 50:20:30 to obtain a positive electrode active material powder of Example 10-1, wherein the first interior had concentration of Li[Ni.sub.0.50Co.sub.0.50]O.sub.2 and the second interior had constant continuous concentration gradient up to Li[Ni.sub.0.50Co.sub.0.2Mn.sub.0.3]O.sub.2.
(76) Further, first of all, nickel sulfate, cobalt sulfate and manganese sulfate were mixed at the molar ratio of 50:30:20, and then the procedure of Example 1 was repeated except for continuing the reaction by using the metal aqueous solution whose concentration was changing until the concentration became 50:20:30 to obtain a positive electrode active material powder of Example 10-2, wherein the first interior had concentration of Li[Ni.sub.0.50 Co.sub.0.30Mn.sub.0.20]O.sub.2 and the second interior had constant continuous concentration gradient up to Li[Ni.sub.0.50Co.sub.0.20Mn.sub.0.30]O.sub.2.
(77) Further, first of all, nickel sulfate, cobalt sulfate and manganese sulfate were mixed at the molar ratio of 50:20:30, and then the procedure of Example 1 was repeated except for continuing the reaction by using the metal aqueous solution whose concentration was changing until the concentration became 50:05:45 to obtain a positive electrode active material powder of Example 10-3, wherein the first interior had concentration of Li[Ni.sub.0.50 Co.sub.0.20Mn.sub.0.30]O.sub.2 and the second interior had constant continuous concentration gradient up to Li[Ni.sub.0.50Co.sub.0.05Mn.sub.0.45]O.sub.2.
(78) Batteries were manufactured by using the active material particle powders, which were manufactured in Examples 8 to 10 and had constant Ni concentration and concentration gradients of Co and Mn in the entire particle, and then capacity, life time characteristic and DSC characteristic were measured. The results were shown in the following Table 5.
(79) As shown in the following Table 5, it was confirmed that the batteries using the active material particle powders manufactured in Examples 8 to 10 having concentration gradient showed improved life time characteristic and DSC characteristic.
(80) TABLE-US-00005 TABLE 5 Capacity Life Time Characteristic DSC Tap (mAhg.sup.1) (%, 100.sup.th) ( C.) density Example 8 215.4 87.6 241.2 2.39 Example 9 189.8 93.6 279.2 2.48 Example 9-2 188.2 94.8 282.2 2.53 Example 10 184.2 95.1 291.2 2.49 Example 10-2 182.7 95.9 295.1 2.51 Example 10-3 178.5 93.2 302.5 2.58
(81) In order to make the concentration gradients of Co, Ni and Mn, first of all, nickel sulfate, cobalt sulfate and manganese sulfate were mixed at the molar ratio of 80:05:15, and then the procedure of Example 1 was repeated except for using the metal aqueous solution whose concentration was changing until the molar ratio became as shown in the following Table to obtain positive electrode active material powders having constant continuous concentration gradients of Co, Ni and Mn.
(82) TABLE-US-00006 TABLE 6 Ni:Co:Mn Example 11-1 55:15:30 Example 11-2 55:20:25 Example 11-3 60:15:25 Example 11-4 60:10:30
(83) Samples of the nickel-manganese-cobalt composite hydroxide and the positive electrode active material manufactured in Example 11-4 were manufactured, and then TEM images were taken. The result was shown in
Comparative Example 5
(84) Particles having constant metal ion concentration expressed by Li(Ni.sub.0.62Co.sub.0.13Mn.sub.0.25)O.sub.2 in the entire particle were manufactured.
(85) Batteries were manufactured by using the active material particle powders manufactured in Examples 11 to 11-4, and then capacity, life time characteristic and DSC characteristic were measured. The results were shown in the following Table 7.
(86) As shown in the following Table 7, it was confirmed that the batteries using Examples 11 to 11-4 having concentration gradient showed improved capacity, life time characteristic and DSC characteristic, compared with the battery using Comparative Example 5 not showing concentration gradient, and in particular, the life time characteristic and the DSC characteristic were improved as the thickness of the surface maintaining section was increased.
(87) TABLE-US-00007 TABLE 7 Capacity Life Time Characteristic DSC (mAhg.sup.1) (%, 100.sup.th) ( C.) Example 11 191.2 94.7 275.9 Example 11-2 192.8 94.2 270.7 Example 11-3 195.8 93.3 269.9 Example 11-4 196.2 94.4 272.5 Comparative 183.6 92.8 264.1 Example 5
(88) In order to make the concentration gradients of Co, Ni and Mn, first of all, nickel sulfate, cobalt sulfate and manganese sulfate were mixed as shown in the following Table 8, and then the procedure of Example 1 was repeated except for using the metal aqueous solution whose concentration was changing until the concentration became 55:15:30 to obtain nickel-manganese-cobalt composite hydroxides and positive electrode active material particles having constant continuous concentration gradients of Co, Ni and Mn.
(89) TABLE-US-00008 TABLE 8 Ni:Co:Mn Example 12-1 80:00:20 Example 12-2 80:10:10 Example 12-3 80:15:05 Example 12-4 80:20:00
(90) Samples of the nickel-manganese-cobalt composite hydroxide and the positive electrode active material manufactured in Example 12-1 were manufactured, and then TEM images were taken. The result was shown in
Comparative Example 6
(91) Particles having constant metal ion concentration expressed by Li(Ni.sub.0.62Co.sub.0.15Mn.sub.0.23)O.sub.2 in the entire particle were manufactured.
(92) Batteries were manufactured by using the active material particle powders manufactured in Examples 12 to 12-4, and then capacity, life time characteristic and DSC characteristic were measured. The results were shown in the following Table 9.
(93) As shown in the following Table 9, it was confirmed that the batteries using Examples 12-1 to 12-4 having concentration gradient showed improved capacity, life time characteristic and DSC characteristic, compared with the battery using Comparative Example 6 not showing concentration gradient, and in particular, the life time characteristic and the DSC characteristic were improved as the thickness of the surface maintaining section was increased.
(94) TABLE-US-00009 TABLE 9 Capacity Life Time Characteristic DSC (mAhg.sup.1) (%, 100.sup.th) ( C.) Example 12-1 190.8 95.1 277.9 Example 12-2 191.4 95.0 274.7 Example 12-3 191.5 94.7 272.9 Example 12-4 191.9 94.5 271.8 Comparative 184.1 92.0 260.8 Example 6
(95) In order to make the outside composition constant as 63:12:25 but concentration gradients of Co, Ni and Mn in the entire particle, first of all, nickel sulfate, cobalt sulfate and manganese sulfate were mixed at the molar ratio shown in the following Table 10, and then the procedure of Example 1 was repeated except for using the metal aqueous solution whose concentration was changing until the concentration became 63:12:25 to obtain positive electrode active material particles, so as to obtain positive electrode active material powder, wherein the concentrations of Co, Ni and Mn showed gradient in the entire particle.
(96) TABLE-US-00010 TABLE 10 Ni:CO:Mn Example 13-1 75:00:25 Example 13-2 80:00:20 Example 13-3 85:00:15 Example 13-4 75:10:15 Example 13-5 80:10:10 Example 13-6 85:10:05
(97) A sample of the nickel-manganese-cobalt composite hydroxide manufactured in Example 13-6 was manufactured, and then a TEM image was taken. The result was shown in
Comparative Example 7
(98) Particles having constant metal ion concentration expressed by Li(Ni.sub.0.68Co.sub.0.12Mn.sub.0.20)O.sub.2 in the entire particle were manufactured.
(99) Batteries were manufactured by using the active material particle powders manufactured in Examples 13-1 to 13-6, and then capacity, life time characteristic and DSC characteristic were measured. The results were shown in the following Table 11.
(100) As shown in the following Table 11, it was confirmed that the batteries using Examples 13-1 to 13-6 having concentration gradient showed improved capacity, life time characteristic and DSC characteristic, compared with the battery using Comparative Example 7 not showing concentration gradient, and in particular, the life time characteristic and the DSC characteristic were improved as the thickness of the surface maintaining section was increased.
(101) TABLE-US-00011 TABLE 11 Capacity Life Time Characteristic DSC (mAhg.sup.1) (%, 100.sup.th) ( C.) Example 13-1 196.9 94.6 271.2 Example 13-2 197.5 94.0 269.9 Example 13-3 198.2 93.2 267.4 Example 13-4 197.1 94.2 270.0 Example 13-5 198.1 93.7 268.9 Example 13-6 198.9 92.8 266.9 Comparative 188.3 90.2 257.5 Example 7
Example 14
(102) In order to manufacture a positive electrode active material precursor and a positive electrode active material continuously comprising the first interior, wherein the Co composition was constant, and the Ni and Mn compositions showed concentration gradient, and the second interior, wherein the Mn composition was constant, and the Co and Ni compositions showed concentration gradient, the procedure of Example 1 was repeated except for using a metal aqueous solution whose concentration was changing until the concentration became 55:20:25 while mixing a mixture of nickel sulfate, cobalt sulfate and manganese sulfate at the composition of 65:10:25 to a mixture of nickel sulfate, cobalt sulfate and manganese sulfate at the composition of 75:10:15 to manufacture a positive electrode active material particle, so as to obtain a positive electrode active material precursor positive electrode active material of Example 14-1, wherein in the first interior, the Co composition was constant, and the Ni and Mn compositions showed concentration gradient, and in the second interior, wherein the Mn composition was constant, and the Co and Ni compositions showed concentration gradient.
(103) The procedure of Example 4 was repeated except for continuing the reaction as maintaining the said molar ratio when the molar ratio of the metal aqueous solution reached 55:20:25 during the particle forming process for further comprising surface maintaining sections having thickness of 0.2 m and 0.5 m, respectively, so as to obtain spherical nickel-manganese-cobalt composite hydroxides of Examples 14-2 and 14-3 containing the second interior having concentration gradient and a surface maintaining section.
(104) Batteries were manufactured by using the active material particle powders manufactured in Examples 14-1 to 14-3, and then capacity, life time characteristic and DSC characteristic were measured. The results were shown in the following Table 12.
(105) As shown in the following Table 12, it was confirmed that the batteries using Examples 14-1 to 14-3 having concentration gradient showed improved capacity, life time characteristic and DSC characteristic, compared with the battery using Comparative Example 7 not showing concentration gradient, and in particular, the life time characteristic and the DSC characteristic were improved as the thickness of the surface maintaining section was increased.
(106) TABLE-US-00012 TABLE 12 Capacity Life Time Characteristic DSC (mAhg.sup.1) (%, 100.sup.th) ( C.) Example 14-1 193.1 94.2 275.7 Example 14-2 191.0 95.0 278.8 Example 14-3 189.5 95.9 285.9 Comparative 181.3 93.9 266.3 Example 7
(107) A positive electrode active material precursor and a positive electrode active material of Example 15-1, wherein the nickel:manganese:cobalt composition was constant as 90:05:05 in the first interior, and the composition of Co, Ni and Mn showed concentration gradient from 90:05:05 to 0.33:0.33:0.33 in the second interior, were manufactured.
(108) A positive electrode active material precursor and a positive electrode active material of Example 15-2, wherein the composition was constant as 90:05:05 in the first interior, and the composition of Co, Ni and Mn showed concentration gradient from 70:10:20 to 60:10:30 in the second interior, were manufactured.
(109) TEM images of the cross-sections of the nickel-manganese-cobalt composite hydroxide precursors and the positive electrode active material of Examples 15-1 and 15-2 were taken, and the results were shown in
(110)
(111) Positive electrode active material precursors and positive electrode active materials having a core-shell structure, wherein the composition of nickel:manganese:cobalt at the core part and the shell part were as shown in the following Table 13, were manufactured.
(112) TABLE-US-00013 TABLE 13 Core Shell Shell Composition Composition Thickness Example 16-1 90:05:05 50:20:30 0.2 m Example 16-2 80:10:10 50:20:30 0.2 m Example 16-3 70:10:20 50:20:30 0.2 m Example 16-4 70:10:20 40:20:40 0.2 m Example 16-5 60:20:20 50:20:30 0.2 m Example 16-6 70:10:20 50:20:30 0.5 m Example 16-7 70:10:20 50:20:30 1.0 m Example 16-8 70:10:20 50:20:30 1.5 m Example 16-9 70:10:20 50:20:30 2.0 m Example 16-10 70:10:20 50:20:30 2.5 m
(113) Batteries were manufactured by using the manufactured active material particle powders, and then capacity, life time characteristic and DSC characteristic were measured. The results were shown in the following Table 14.
(114) TABLE-US-00014 TABLE 14 Capacity Life Time Characteristic DSC Tap (mAhg.sup.1) (%, 100.sup.th) ( C.) Density Example 16-1 191.4 92.7 269.7 2.45 Example 16-2 186.7 94.1 273.2 2.44 Example 16-3 181.9 95.5 275.5 2.44 Example 16-4 182.8 94.9 272.5 2.46 Example 16-5 177.9 96.5 279.8 2.45 Example 16-6 185.7 93.9 271.8 2.43 Example 16-7 181.9 95.5 275.2 2.44 Example 16-8 179.4 96.0 279.8 2.44 Example 16-9 176.2 97.1 284.6 2.46 Example 16-10 172.1 97.5 288.4 2.45
(115) In order to measure oxidation number of the active material particle manufactured in Example 1-1 to the direction of the particle radius, X-ray photoelectron spectroscopy was measured. The result was shown in
(116) As shown in
INDUSTRIAL APPLICABILITY
(117) In the positive electrode active material precursor for a lithium secondary battery of the present invention and a positive electrode active material manufactured by using thereof, the a-axis direction length to c-axis direction length ratio is changed primary particle from the center to the surface in the interior of the secondary particle, and the a-axis orientation of the primary particle is headed to the center of the positive electrode active material as a secondary particle, and the particles are adjoining each other and grow to a fixed route. Accordingly, it has effects that insertion and secession of a lithium ion may become easier, and high capacity can be obtained by reduced electric resistance between particles.
(118) While the invention has been described with respect to the above specific embodiments, it should be recognized that various modifications and changes may be made and also fall within the scope of the invention as defined by the claims that follow.