Method for separating, purifying and recycling positive electrode material of waste lithium ion battery and obtained positive electrode material
A lithium-ion battery and ion battery technology, applied in chemical instruments and methods, battery recovery, recycling technology, etc., can solve the problems of entrainment loss of valuable metals, high separation cost, complicated process, etc., and achieve good economic benefits, separation Good effect and low acidity in stripping
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Embodiment 1
[0109] A method for separating, purifying and reclaiming waste lithium-ion battery cathode materials:
[0110] (1) Positive electrode material leaching: the waste nickel-cobalt-manganese lithium-ion battery is disassembled, discharged and broken, and the broken waste batteries are leached with hydrochloric acid and reducing agent (hydrogen peroxide) to obtain a leachate, the composition of the leachate is as follows As shown in Table 1;
[0111] (2) Purify and remove impurities:
[0112] Use NaOH solution to adjust the pH value of the leachate to 4.5, add sodium persulfate as an oxidant, and first filter and remove Fe and Al ions in the leachate in the form of hydroxide precipitation to obtain a feed solution after removing iron and aluminum;
[0113] Use Mextral 984H extractant after saponification (volume fraction is 20%, diluent is sulfonated kerosene, saponification agent is 8mol / L NaOH solution) to extract Cu ions in the feed liquid after removing iron and aluminum, and ...
Embodiment 2
[0125] A method for separating, purifying and reclaiming waste lithium-ion battery cathode materials:
[0126] (1) Positive electrode material leaching: Disassemble, discharge and crush the waste nickel-cobalt-manganese lithium-ion battery, and use hydrochloric acid and reducing agent (sodium sulfite) to leach the waste battery sheet after the crushing to obtain a leachate. The composition of the leachate is shown in Table 2 shown;
[0127] (2) Purify and remove impurities:
[0128] After saponification, the CP50 extractant (volume fraction is 20%, the diluent is sulfonated kerosene, and the saponification agent is 6mol / L NaOH solution) is used to extract Cu ions in the leachate, and the extraction stage is 1, compared to 0.25: 1. The stirring speed is 150r / min, the time is 15min, the experimental temperature is 30°C, the pH of the aqueous phase is controlled to 2.5, and the copper-loaded organic phase and the copper-removed feed liquid are respectively obtained after phase s...
Embodiment 3
[0141] A method for separating, purifying and reclaiming waste lithium-ion battery cathode materials:
[0142] (1) Positive electrode material leaching: Disassemble, discharge and crush the waste nickel-cobalt-manganese lithium-ion battery, and use hydrochloric acid and reducing agent (ascorbic acid) to leach the waste battery sheet after the crushing to obtain a leachate. The composition of the leachate is shown in Table 3 shown;
[0143] (2) Purification and removal of impurities: at a temperature of 20°C, the carboxylic acid extractant BC196 (the material corresponding to m=8 and n=6 in the general formula) and the NaOH alkali solution and diluent with a concentration of 14mol / L Escaid 110 mixed saponification, the volume fraction of carboxylic acid extractant BC196 is 25%, as the organic phase system, the leachate is used as the water phase system, respectively flows in from both ends of the extractor, flows in opposite directions, and the number of stages is For 11-stage e...
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