Cathode Material For A Lithium Secondary Battery, Method For Manufacturing Same, And Lithium Secondary Battery Including The Cathode Material
A technology for rechargeable lithium batteries and active materials, applied in lithium batteries, non-aqueous electrolyte batteries, battery electrodes, etc., can solve problems such as the inability to use lithium metal, and achieve the effects of suppressing the decline in service life, increasing capacity, and improving electrode density
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Embodiment 1
[0045] Petroleum coke was used as an amorphous carbon raw material, and the petroleum coke was pulverized into powder by a dry jet mill so that the average particle diameter of the petroleum coke became 10 μm. At this time, the maximum particle size is controlled below 26 μm, and the minimum particle size is controlled at 0.8 μm through a bag filter. Next, the pulverized petroleum coke was heated up to 1100°C at a temperature increase rate of 2.5°C / min. Then, after holding at the highest temperature for 3 hours, it was slowly cooled at a cooling rate of 5° C. / min.
Embodiment 2
[0047] Petroleum coke was used as an amorphous carbon raw material, and the petroleum coke was pulverized into powder by a wet disc mill so that the average particle diameter of the petroleum coke became 10 μm. At this time, the maximum particle size is controlled below 40 μm by the classifier, and the minimum particle size is controlled by the bag filter to 0.3 μm. Next, the pulverized petroleum coke was heated up to 1100°C at a temperature increase rate of 2.5°C / min. Then, after holding at the highest temperature for 3 hours, it was slowly cooled at a cooling rate of 5° C. / min.
Embodiment 3
[0049]Petroleum coke was used as an amorphous carbon raw material, and the petroleum coke was pulverized into powder by a dry jet mill so that the average particle diameter of the petroleum coke became 12 μm. At this time, the maximum particle size is controlled below 40 μm by the classifier, and the minimum particle size is controlled by the bag filter to 0.5 μm. Next, the pulverized petroleum coke was heated up to 1100°C at a temperature increase rate of 2.5°C / min. Then, after holding at the highest temperature for 3 hours, it was slowly cooled at a cooling rate of 5° C. / min.
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Abstract
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