Neodymium, iron and boron waste recycling process with approximately zero wastewater discharge
A technology of waste recycling and neodymium iron boron, applied in the direction of process efficiency improvement, etc., can solve the problems of low recovery rate of heavy rare earths, secondary pollution of the environment, high cost, etc., and achieve no environmental pollution, significant economic benefits, and low production costs Effect
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Embodiment 1
[0020] Finely pulverize 1OOOKG NdFeB waste into 300-mesh powder, oxidize and burn at 550°C for 150 minutes, put it into the reaction tank, add water 15OOKG and 500KG hydrochloric acid, beat and heat to make the reactor temperature reach 100°C, Stir the reaction for 5 hours, cool to 25°C and filter to separate solid and liquid to obtain solid X and liquid A. Add liquid A to hydrogen peroxide 20KG ammonium bicarbonate 100KG, stir at 90°C for 35 minutes to neutralize and remove impurities, then filter to obtain solid Y and liquid B. The solid Y returns to the roasting process and repeats the above steps; the liquid B undergoes the separation of 40 grades of neodymium and terbium and 70 grades of terbium and dysprosium in the PS07-sulfonated kerosene-hydrochloric acid system to obtain neodymium chloride, terbium chloride, and dysprosium chloride respectively. solution, and then precipitate and burn separately to obtain neodymium oxide, terbium oxide, and dysprosium oxide products ...
Embodiment 2
[0023] Finely pulverize 1OOOKG NdFeB waste into 200-mesh powder, oxidize and burn at 650°C for 100 minutes, put it into the reaction tank, add 800KG water and 300KG oxalic acid, beat and heat to make the reactor temperature reach Stir and react at 100°C for 7 hours, cool to 25°C and filter to separate solid and liquid to obtain solid X and liquid A. Add liquid A to 3KG of quicklime, 60KG of sodium chlorate, stir at 90°C for 45 minutes to neutralize and remove impurities, and then filter to obtain solid Y and liquid B. The solid Y returns to the roasting process and repeats the above steps; the liquid B undergoes the separation of 40 grades of neodymium and terbium and 70 grades of terbium and dysprosium in the P507-sulfonated kerosene-hydrochloric acid system to obtain neodymium chloride, terbium chloride, and dysprosium chloride respectively. solution, and then precipitate and burn separately to obtain neodymium oxide, terbium oxide, and dysprosium oxide products that meet th...
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