POSITIVE ACTIVE MATERIAL AND METHOD FOR PRODUCING THE SAME

Abstract

The present invention relates to a positive active material and a method for producing same and, more specifically, to a positive active material comprising LiAlO2 at the surface thereof as a result of reacting an Al compound with residual lithium and to a method for producing same.

Claims

1. A positive active material comprising LiAlO.sub.2 in a surface.

2. The positive active material of claim 1, including LiAlO.sub.2 exhibiting a peak, where 2θ is ranged from 45° to 46°, in XRD.

3. The positive active material of claim 1, being given in Formula 1 that is Li.sub.1+aNi.sub.bM1.sub.cM2.sub.dO.sub.2 where 0.95≧b≧0.75, a+b+c=1, M1 is one or more selected from a group of Co, B, Ba, Cr, F, Li, Mo, P, Sr, Ti, and Zr, and M2 is one or more selected from a group of Mn, Al, B, Ba, Cr, F, Li, Mo, P, Sr, Ti, and Zr.

4. The positive active material of claim 1, wherein residual lithium is equal to or smaller than 0.6 wt %.

5. The positive active material of claim 1, wherein particle strength is equal to or larger than 150 MPa.

6. A method for producing a positive active material according to claim 1, comprising: preparing the positive active material; and mixedly agitating the positive active material with a compound including Al.

7. The method of claim 6, wherein the compound including the Al is selected from a group of Al(OH).sub.3, Al.sub.2O.sub.3, Al(NO.sub.3).sub.3, Al.sub.2(SO.sub.4), AlCl.sub.3, AlH.sub.3, AlF.sub.3, and AlPO.sub.4.

8. The method of claim 7, further comprising, between the preparing of the positive active material and the mixedly agitating of the positive active material: preparing a washing solution in uniform temperature; agitating the positive active material in the washing solution; and drying the washed positive active material.

9. The method of claim 8, wherein the washing solution is distilled water or an alkaline solution.

10. The method of claim 8, wherein the drying includes: Vacuum-drying the washed positive active material at 80 to 200° C. for 5 to 20 hours.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

[0019] The patent or application file contains at least one drawing executed in color. Copies of this patent or patent application publication with color drawing(s) will be provided by the Office upon request and payment of the necessary fee.

[0020] FIG. 1 shows results of measuring active materials, which are manufactured through a comparison and an embodiment according to the inventive concept, by using XRD measurement.

[0021] FIG. 2 shows results of measuring particle strength of active materials manufactured through a comparison and an embodiment according to the inventive concept.

[0022] FIG. 3 shows result of measuring amounts of residual lithium components of active materials manufactured through comparisons and embodiments according to the inventive concept.

[0023] FIG. 4 shows results of measuring lifetime characteristics of batteries including active materials manufactured through comparisons and embodiments according to the inventive concept.

[0024] FIG. 5 shows results of high temperature storage characteristics of active materials manufactured through comparisons and embodiments according to the inventive concept.

DETAILED DESCRIPTION OF THE INVENTION

[0025] Hereinafter, embodiments of the inventive concept will be described in conjunction with the accompanying drawings, but the inventive concept may not be restrictive to the following embodiments.

Embodiment

Coating Concentration Gradient Positive Active Material

[0026] After inputting distilled water of 20 L and ammonia of 840 g as a chelating agent into a batch reactor (having capacity of 70 L and a rotation motor's power equal to or larger than 80 W), agitation was performed with a motor rate of 400 rpm while maintaining internal temperature of the reactor at 50° C.

[0027] As a second operation, a first precursor solution having concentration of 2.5 M, which was mixed with nickel sulfate, cobalt sulfate, and manganese sulfate in a mole ratio of 9:1:0, was input in a rate of 2.2 L/hour and continuously an ammonia solution having concentration of 28% was input in a rate of 0.15 L/hour. Additionally, for adjusting pH, a sodium hydroxide solution having concentration of 25% was supplied to maintain pH on 11. An impeller speed was adjusted at 400 rpm. The first precursor solution, the ammonia solution, and the sodium hydroxide solution, which are prepared, was input continuously into the reactor in an amount of 27 L.

[0028] Next, as a third operation, a concentration gradient layer forming solution was prepared with concentration of 2.5 M where nickel sulfate, cobalt sulfate, and manganese sulfate were mixed in a mole ratio of 65:15:20. After fixing an amount of the first precursor solution of 2.5-M concentration, which was mixedly manufactured with nickel sulfate, cobalt sulfate, and manganese sulfate in a mole ratio of 9:1:0 through the second operation in an agitator in addition to the batch reactor, in 10 L, the concentration gradient layer forming solution was input in a rate 2.2 L/hour and agitated with the first precursor solution to make a second precursor solution. At the same time, the second precursor solution was introduced into the batch reactor. Until a mole ratio of nickel sulfate, cobalt sulfate, and manganese sulfate of the second precursor solution reaches concentration of a shell layer that is 4:2:4, the concentration gradient layer forming solution was mixedly introduced into the batch reactor, an ammonia solution having concentration of 28% was input in a rate of 0.08 L/hour, and a sodium hydroxide solution was maintained in pH of 11. In this case, an input amount of the second precursor solution, the ammonia solution, and the sodium hydroxide solution was 17 L.

[0029] Next, as a fourth operation, a third precursor solution, which was mixed with nickel sulfate, cobalt sulfate, and manganese sulfate in a mole ratio of 4:2:4, was input into the batch reactor until the volume thereof reaches 5 L. After completing a reaction, a spherical nickel-manganese-cobalt composite hydroxide precipitate was obtained from the batch reactor.

[0030] After filtering the precipitated composite metal hydroxide and washing the composite metal hydroxide by water, the washed composite metal hydroxide was dried in a hot blower at 110° C. for 12 hours to obtain a precursor powder having a structure of metal oxide composite where an inner core layer had a continuous concentration gradient to (Ni.sub.0.9Co.sub.0.1)(OH).sub.2 and an outer shell layer had a continuous concentration gradient from (Ni.sub.0.9Co.sub.0.1)(OH).sub.2 to (Ni.sub.0.4Co.sub.0.2Mn.sub.0.4)(OH).sub.2.

[0031] After mixing the metal hydroxide composite and hydroxide lithium (LiOH) in a mole ratio of 1:1.02, heating the mixture in a temperature elevation rate of 2° C./min, and firing the mixture at 790° C. for 20 hours, there was obtained a positive active material powder where an inner core layer had a continuous concentration gradient to Li(Ni.sub.0.9Co.sub.0.1)O.sub.2 and an outer shell layer had a continuous concentration gradient from Li(Ni.sub.0.9Co.sub.0.1)O.sub.2 to Li(Ni.sub.0.4Co.sub.0.2Mn.sub.0.4)O.sub.2.

[0032] After dry and wet coating of positive active material particles with an Al compound, the particles were processed in thermal treatment at 720° C.

Embodiment

Synthesizing NCA Particles

[0033] A NiCo(OH).sub.2 precursor was first manufactured through a coprecipitation reaction to obtain an NCA-series positive active material. After mixing the metal hydroxide composite and the lithium hydroxide in a mole ratio of 1:1.02, heating the mixture in a temperature elevation rate of 2° C./min, and firing the mixture at 750° C. for 20 hours, a positive active material powder was obtained.

[0034] After dry and wet coating of positive active material particles with an Al compound, the particles were processed in thermal treatment at 720° C.

TABLE-US-00001 TABLE 1 Thermal Washing Calcination treatment time 1st introduction 2nd introduction temp. temp. No [min] Al(OH).sub.3 Al.sub.2O.sub.3 Al(OH).sub.3 Al.sub.2O.sub.3 Al(NO.sub.3).sub.3 [° C.] [° C.] Comparison-1 0 — — — — — 790 — Comparison-2 0 — — — — — 830 — Comparison-3 30 — — — — 810 720 Comparison-4 0 4.0 — — — — 750 — Comparison-5 30 3.5 — — — — 750 720 Comparison-6 0 4.0 — — — — 750 — Embodiment-1 0 — — — 2.0 — 790 720 Embodiment-2 0 — — 2.0 — 810 720 Embodiment-3 0 — — 2.0 — 840 720 Embodiment-4 0 — — 1.0 — — 830 500 Embodiment-5 30 — — — 1.0 — 810 720 Embodiment-6 120 — — — — 1.0 810 720 Embodiment-7 0 — — 2.0 — — 750 720 Embodiment-8 30 2.5 — 1.0 — — 750 720 Embodiment-9 120 1.5 — — — 2.0 750 720 Embodiment- 0 — — 4.0 — — 750 720 10 Embodiment- 120 1.4 — 1.0 — — 750 700 11 Embodiment- 120 3.0 — — — 2.0 750 700 12

Experimental Example

Measuring XRD Characteristics

[0035] FIG. 1 shows results of measuring XRD of active materials which are manufactured through Comparison-6 and Embodiment-2.

[0036] Different from Comparison-6, particles manufactured through Embodiment-2 according to the inventive concept has a peak between 45° and 46°.

Experimental Example

Measuring Particle Strength

[0037] FIG. 2 shows results of measuring particle strength of active materials manufactured through Comparison-6 and Embodiment-10.

[0038] From FIG. 2, it may be seen that particles manufactured through Embodiment-10 are more improved about 20% than particles of Comparison-6 in strength.

Experimental Example

Measuring Non-Reacted Lithium

[0039] Non-reacted lithium was measured as an amount of 0.1 M HCl which had been used until pH 4 by pH titration. First, after inputting a positive active material of 5 g into distilled water (DIW) of 100 ml, agitating the mixed solution for 15 minutes, filtering the agitated solution, and taking the filtered solution of 50 ml, 0.1 M HCl was added thereto and a consumption amount of HCl dependent on pH variation was measured to determine Q1 and Q2. Then, amounts of non-reacted LiOH and Li.sub.2CO.sub.3 were calculated by equations as follows.

M1=23.94 (LiOH molecular weight)

M2=73.89 (Li.sub.2CO.sub.3 molecular weight)

SPL size=(Sample weight×Solution weight)/Water weight

LiOH (wt %)=[(Q1−Q2)×C×M1×100]/(SPL size×1000)

Li.sub.2CO.sub.3 (wt. %)=[2×Q2×C×M2/2×100]/(SPL size×1000)

[0040] Table 2 and FIG. 3 show results of measuring concentration of non-reacted LiOH and Li.sub.2CO.sub.3 from NCA-series lithium oxide composites manufactured through the aforementioned Embodiments and Comparisons, as follows.

TABLE-US-00002 TABLE 2 Residual lithium [ppm] Discharge Lifetime Before After Total capacity 100th storage storage No LiOH Li.sub.2CO.sub.3 Li [%] [0.1 C] [%] ohm ohm Comparison-1 7.376 4,552 0.0431 206 92 — — Comparison-2 3,211 4,128 0.0246 204 92 18  131  Comparison-3 3,445 1,220 0.0177 206 84 — — Comparison-4 5,035 3,076 0.0293 201 82 5 11 Comparison-5 2,727 1,433 0.0153 202 70 7 16 Comparison-6 7.422 3,862 0.0414 210 74 — — Embodiment-1 4,930 4,735 0.0334 196 93 — — Embodiment-2 3,035 1,831 0.0176 188 98 — — Embodiment-3 1,903 869 0.0103 191 83 20  90 Embodiment-4 2,632 2,756 0.0184 205 80 — — Embodiment-5 2,254 1,082 0.0123 204 90 — — Embodiment-6 1,690 1,069 0.0100 203 88 — — Embodiment-7 2,090 1,080 0.0117 206 77 8 20 Embodiment-8 2,272 1,268 0.0129 202 77 6 13 Embodiment-9 2,116 1,239 0.0122 203 77 11  35 Embodiment- 2,049 1,702 0.0132 204 60 — — 10 Embodiment- 2,096 1,349 0.0124 209 55 8 13 11 Embodiment- 2,314 1,650 0.0141 204 75 33  92 12

[0041] As shown in FIG. 3, residual lithium of Comparison-4 was measured in a high level because a washing or surface processing was not performed. Residual lithium of Embodiment-7 executing thermal treatment after coating an aluminum compound was reduced than that of Comparison-4 in amount.

[0042] Additionally, as shown in FIG. 3, Embodiment-3 executing thermal treatment after coating an aluminum compound with a concentration gradient NCM positive active material was more improved than Comparison-2, which did not execute post-treatment, for residual lithium.

Experimental Example

Evaluating Charge/Discharge Characteristics

[0043] Table 2 and FIG. 4 show results of performing charge/discharge experiments between 3 V and 4.3 V in rates of C/10 charge and C/10 discharge after manufacturing respective coin cells by using positive active materials, which are manufactured through the aforementioned Embodiments and Comparisons, as positive electrodes and by using lithium metals as negative electrodes.

[0044] From FIG. 4, it may be seen that an embodiment executing an Al coating after washing is better in lifetime. In FIG. 4, Comparison-3 and Comparison-5 correspond to concentration gradient NCM and NCA positive active materials which are respectively washed. Embodiment-5 for a concentration gradient NCM positive active material made executing an Al coating after washing and Embodiment-8 for a concentration gradient NCA positive active material executing an Al coating after washing were improved in lifetimes.

Experimental Example

Results of Measuring Impedance Before/After High Temperature Storage

[0045] Table 2 and FIG. 5 show results of measuring impedance before/after high temperature storage of Embodiment 3 for an NCM-series positive active material having a continuous concentration gradient.

[0046] From FIG. 5, it may be seen that impedance of Embodiment-3 executing thermal treatment after an Al coating is more reduced than that of Comparison-2 which does not execute washing and surface treatment.

[0047] Embodiments of the inventive concept relate to a positive active material including LiAlO.sub.2 and a method for producing the same, being highly useful for enhancing particle strength, as well as reducing residual lithium, due to presence of LiAlO.sub.2 by doping the positive active material with aluminum and then reacting the residual lithium, which is existing in the surface, with the aluminum.