Method for preparing ferric pyrophosphate used for lithium ion battery by utilizing iron-bearing raffinate
A lithium ion battery, iron orthophosphate technology, applied in battery electrodes, chemical instruments and methods, circuits, etc., can solve the problems of increasing the production cost of iron phosphate, coarse extraction of ferrous salt solution, and low concentration of active ingredients, and saving The effect of raw materials, improving utilization rate and improving production efficiency
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Embodiment 1
[0042] (1) Add hydrogen peroxide solution in the iron-containing raffinate, the quality of the hydrogen peroxide is 10% of the iron-containing raffinate quality, stir for 2h, control the reaction temperature of the solution to be 20°C, and the pH value to be 2; add organic phosphoric acid The extractant P204 is used for multi-stage extraction, the mass ratio of extractant and solution in each stage of extraction tank is 1:200, the extraction temperature is 20°C, the pH value is 2, the extraction is 1h, the organic phase is separated and washed with inorganic acid to obtain iron salt solution;
[0043] (2) Use the iron salt solution recovered in step (1) as an iron source, add phosphoric acid, stir, the reaction temperature is 55 ° C, add a pH regulator to a pH value of 2, react for 2 hours, cool, and then undergo solid-liquid separation and washing 1. Obtain iron orthophosphate powder material for lithium ion battery after drying.
Embodiment 2
[0045] (1) Add sodium hypochlorite solution in iron-containing raffinate, the quality of described sodium hypochlorite is 30% of iron-containing raffinate quality, stir 3h, the reaction temperature of control solution is 40 ℃, pH value is 1.5; Add organophosphoric acid The extractant P507 is used for multi-stage extraction, the mass ratio of extractant and solution in each stage of extraction tank is 1:400, the extraction temperature is 10°C, the pH value is 1.5, the extraction is 1.5h, the organic phase is separated and washed with inorganic acid Obtain iron salt solution;
[0046] (2) Use the iron salt solution recovered in step (1) as an iron source, add ammonium dihydrogen phosphate, stir, the reaction temperature is 65°C, add a pH regulator to a pH value of 2, react for 5 hours, cool, and then undergo solid-liquid After separation, washing and drying, iron orthophosphate powder materials for lithium ion batteries are obtained.
Embodiment 3
[0048] (1) add sodium peroxide solution in iron-containing raffinate, the quality of described sodium peroxide is 100% of iron-containing raffinate quality, stir 5h, the reaction temperature of control solution is 70 ℃, and pH value is 3 Add organic phosphoric acid extractant N290 for multi-stage extraction, the mass ratio of extractant and solution in each stage of extraction tank is 1:800, the extraction temperature is 70°C, the pH value is 1.5, the extraction is 2.5h, and the organic phase is separated through Obtain iron salt solution after mineral acid washing;
[0049] (2) Use the iron salt solution recovered in step (1) as an iron source, add ammonium dihydrogen phosphate, stir, the reaction temperature is 72°C, add a pH regulator to a pH value of 2, react for 8 hours, cool, and then undergo solid-liquid After separation, washing and drying, iron orthophosphate powder materials for lithium ion batteries are obtained.
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