Positive electrode active material, method for manufacturing positive electrode active material, and positive electrode and lithium secondary battery comprising positive electrode active material
A technology of positive active materials and raw materials, applied in secondary batteries, lithium storage batteries, active material electrodes, etc., can solve the problems of differential thermal properties, limitations, unstable crystal structure, etc., and achieve the effect of reducing surface resistance and lowering the unit price of manufacturing
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[0052] The method for preparing positive electrode active material according to one embodiment of the present invention comprises the following steps: preparing a nickel-containing and cobalt-free transition metal hydroxide, the nickel content of which is more than 60 mol% of the total moles of transition metals; mixing metal hydroxide with lithium raw material and sintering the mixture, wherein the method may further include: mixing cobalt (Co) raw material during the process of mixing the transition metal hydroxide with lithium raw material and sintering the mixture, Alternatively, cobalt (Co) raw materials are mixed after sintering. In this case, the Co raw material is mixed in such an amount that the Co amount in the finally prepared cathode active material is in the range of more than 0 ppm to 6,000 ppm or less.
[0053] Hereinafter, each step of preparing the cathode active material will be described more specifically.
[0054] Firstly, a nickel-containing and cobalt-fr...
Embodiment 1
[0119] NiSO 4 , MnSO 4 and Al 2 (SO 4 ) 3 Dissolve in deionized water with the molar ratio of nickel:manganese:aluminum being 86:12:2 to prepare a 2M transition metal aqueous solution.
[0120] The vessel containing the transition metal aqueous solution was connected to a 5 L batch reactor set at 40°C. Separately, 2.2M ammonium aqueous solution and 40% sodium hydroxide aqueous solution were separately prepared and connected to the reactor. Put 4L of deionized water in the reactor, and then the reactor is purged with nitrogen at a rate of 0.2 L / min to remove dissolved oxygen in the water and form a non-oxidizing atmosphere in the reactor.
[0121] After that, the transition metal aqueous solution, the sodium hydroxide aqueous solution and the ammonium aqueous solution were added to the reactor at a rate of 0.3 mL / min, 0.2 mL / min and 0.2 mL / min, respectively, and a co-precipitation reaction was carried out for 10 hours to precipitate the transition metal Hydroxide particle...
Embodiment 2
[0124] Prepare the positive electrode active material precursor in the same manner as in Example 1, except that the Co 3 o 4 The transition metal aqueous solution of Example 1 was added in such an amount that the amount of Co in the finally prepared positive electrode active material was 2,000 ppm. Mix the positive electrode active material precursor and LiOH prepared above so that the transition metal: Li molar ratio is 1:1.03, and sinter at 800° C. for 10 hours in an oxygen atmosphere to prepare the positive electrode active material.
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