Continuous leaching system for anode powder of waste lithium batteries and leaching technology
A technology for waste lithium battery and positive electrode is applied in the field of continuous leaching system and leaching process of waste lithium battery positive electrode powder. The effect of excessive, increased production efficiency, and reduced equipment
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Embodiment 1
[0025] A kind of waste lithium battery positive electrode powder continuous leaching process that the present invention proposes, comprises the following steps:
[0026] S1, the clean water with 80L h -1 The flow of enters in the mixing tank 3;
[0027] S2. When the clean water starts to flow into the first reaction kettle 1, the heat-treated lithium iron phosphate battery positive electrode powder is charged at 10kg h -1 The speed is transmitted into the first reactor 1, wherein: the first reactor 1 is kept stirring continuously, the temperature is maintained at 85°C, and the residence time of the material is 80-150min;
[0028] S3. Transport the reaction slurry in the first reaction kettle 1 to the first continuous solid-liquid separator 4 through the first pipeline, and transport the pickling solution separated by the first continuous solid-liquid separator 4 through the fourth pipeline To the pickling solution storage tank 7, the solid obtained from the separation is tra...
Embodiment 2
[0035] A kind of waste lithium battery positive electrode powder continuous leaching process that the present invention proposes, comprises the following steps:
[0036] S1. Put the clean water in L·h -1 The flow of enters in the mixing tank 3;
[0037] S2. When the clean water starts to flow into the first reaction kettle 1, heat-treated 622 ternary battery positive electrode powder at 5 kg h -1 The speed is transmitted into the first reactor 1, wherein: the first reactor 1 is kept stirring continuously, the temperature is maintained at 85°C, and the residence time of the material is 80-150min;
[0038] S3. Transport the reaction slurry in the first reaction kettle 1 to the first continuous solid-liquid separator 4 through the first pipeline, and transport the pickling solution separated by the first continuous solid-liquid separator 4 through the fourth pipeline To the pickling solution storage tank 7, the solid obtained from the separation is transported to the second con...
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