Clean production method of co-precipitation process positive material carbonate precursor
A cathode material and co-precipitation technology, which is applied in the field of clean production of carbonate precursors of cathode materials in co-precipitation method, can solve the problem of high product yield, achieve simple operation, simple production process and small footprint Effect
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Embodiment 1
[0025] like figure 1 As shown, a clean production method for a carbonate precursor of a positive electrode material by a co-precipitation method includes the following steps:
[0026] 1) Use deionized water to prepare 1 mol / L nickel sulfate, cobalt sulfate and manganese sulfate mixed salt solution, 1 mol / L sodium carbonate solution and 0.25 mol / L ammonia solution, respectively, and add them to the main reactor at a certain rate, The pH value of the main reactor is controlled at about 7.8, and the co-precipitation reaction is carried out by stirring in a constant temperature water bath at 60°C;
[0027] 2) After the solid precipitation product of the main reactor in the above step 1) is subjected to 3 centrifugal dehydration and 2 washing with water, the sodium sulfate content of the waste water is 320 ppm, and then drying treatment is performed to obtain the positive electrode material carbonate precursor. ;
[0028] 3) The supernatant of the main reactor in the above step 1...
Embodiment 2
[0032] A clean production method for a co-precipitation cathode material carbonate precursor, comprising the following steps:
[0033] 1) Use deionized water to prepare 2.5mol / L nickel sulfate, cobalt sulfate and manganese sulfate mixed salt solution, 2.5mol / L sodium carbonate solution and 0.45mol / L ammonia solution, and add them to the main reaction at a certain rate. The pH value of the main reaction kettle is controlled at about 8.4, and the co-precipitation reaction is carried out by stirring in a constant temperature water bath at 60 °C;
[0034] 2) After the solid precipitation product of the main reactor in the above step 1) is subjected to 5 times of centrifugal dehydration and 4 times of washing with water, the sodium sulfate content of the waste water is 480ppm, and then drying treatment is performed to obtain the positive electrode material carbonate precursor. ;
[0035] 3) The supernatant of the main reactor in the above step 1) and the waste water after centrifu...
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