Process for extracting and recycling waste containing rare earth through solvent
A rare earth waste and process technology, which is applied in the field of solvent extraction and recovery of rare earth wastes, can solve the problems of high consumption of organic phase, lag in mass transfer, and variable components, etc., and achieves the effects of low production cost, low consumption and easy operation.
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Embodiment 1
[0027] The rare earth-containing waste containing rare earth molecular sieve production process slag, FCC waste catalyst, and automobile exhaust waste catalyst is pretreated by crushing, grinding, and washing. The pretreated rare earth-containing waste is mixed with caustic soda and calcium chloride in a mass ratio of 1:0.75:0.4, then heated to 450°C for 2 hours, and then heated to 700°C for 2 hours to obtain a sintered material.
[0028] The sintered material is reacted with excess hydrochloric acid solution, and filtered after the reaction to obtain a feed solution containing Ce, Pr, Dy, Er, Tm and insoluble matter. The mixed organic phase of sulfonated kerosene of P227 and P507, containing Ce, Pr, Dy, Er, Tm feed liquid and N-methylimidazole anion exchange resin phase is added sequentially into the reactor. In the mixed organic phase, the P507 concentration is 1mol / L, and the P227 concentration is 0.25mol / L. The average particle diameter of the N-methylimidazole anion exch...
Embodiment 2
[0033]The rare earth-containing waste containing rare earth molecular sieve production process slag, FCC waste catalyst, and rare earth-containing special ceramic waste is pretreated by crushing, grinding, and washing. The pretreated rare earth-containing waste is mixed with caustic soda and calcium chloride at a mass ratio of 1:0.85:0.5, then heated to 450°C for 1 hour, and then heated to 800°C for 2 hours to obtain a sintered material.
[0034] The sintered material is reacted with excess hydrochloric acid solution, and filtered after the reaction to obtain a feed solution containing Ce, Pr, Dy, Er, Tm and insoluble matter. The mixed organic phase of sulfonated kerosene of P227 and P507, containing Ce, Pr, Dy, Er, Tm feed liquid and N-methylimidazole anion exchange resin phase is added sequentially into the reactor. In the mixed organic phase, the concentration of P507 is 1mol / L, and the concentration of P227 is 0.50mol / L. The average particle size of the N-methylimidazole ...
Embodiment 3
[0039] The rare earth-containing waste containing FCC waste catalyst, automobile exhaust waste catalyst, and rare earth-containing special ceramic waste is pretreated by crushing, grinding, and washing. The pretreated rare earth-containing waste is mixed with caustic soda and calcium chloride in a mass ratio of 1:0.80:0.45, then heated to 400°C for 1 hour, and then heated to 750°C for 3 hours to obtain a sintered material.
[0040] The sintered material is reacted with excess hydrochloric acid solution, and filtered after the reaction to obtain a feed solution containing Ce, Pr, Dy, Er, Tm and insoluble matter. The mixed organic phase of sulfonated kerosene of P227 and P507, containing Ce, Pr, Dy, Er, Tm feed liquid and N-methylimidazole anion exchange resin phase is added sequentially into the reactor. In the mixed organic phase, the concentration of P507 is 1.2mol / L, and the concentration of P227 is 0.40mol / L. The average particle diameter of the N-methylimidazole anion exc...
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