Process for producing battery-grade iron phosphate by high-iron method
An iron phosphate, battery-level technology, applied in the direction of phosphorus compounds, chemical instruments and methods, inorganic chemistry, etc., can solve the problems of large environmental pollution, hidden safety hazards, high cost of iron phosphate, etc., to reduce production costs, improve safety, The effect of low impurity content in the product
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Embodiment 1
[0024] Weigh 680g of phosphoric acid solution with a mass percentage of 85%, and 2440g of ferric nitrate solution with an iron content of 200g / L, mix and stir evenly. Heat the mixture to 70-83°C. 2 g of ferric phosphate seed crystals were added, and the reaction was stirred for 12 hours. The spray solid-liquid separation method is used for solid-liquid separation. Roasting and dehydration of the separated solid matter. Obtain the final product required by this process: 806g of anhydrous iron phosphate product. The iron phosphate product has a particle size of 4um, a tap density of 1.1, and a specific surface area of 8g / cm 3 .
Embodiment 2
[0026] Weigh 680Kg of 85% phosphoric acid in mass percentage and 2440Kg of ferric nitrate solution with iron content of 200g / L, mix and stir evenly. The mixture is heated to 70-83°C. Then 2Kg of ferric phosphate seed crystals were added, and the mixture was stirred and reacted for 12 hours. The solid-liquid separation is carried out by the spray solid-liquid separation method, and the solid obtained from the solid-liquid separation is roasted and dehydrated. Obtain the required final product of this process: 807Kg of anhydrous ferric phosphate product, this ferric phosphate product particle size 4um, tap density 1.11, specific surface area 8.5g / cm 3 .
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