Separation and recovery method of valuable components in rare earth praseodymium neodymium molten salt electrolysis waste
A technology of molten salt electrolysis and recovery method, applied in the direction of improving process efficiency, can solve the problems of long process flow and high processing cost, and achieve the effects of simple process, high yield and short process flow
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Embodiment 1
[0024] A method for separating valuable components in rare earth praseodymium and neodymium molten salt electrolysis waste, which comprises the following steps:
[0025] ⑴Raw material treatment: use the waste produced by the molten salt electrolysis method to produce rare earth praseodymium and neodymium metals as raw materials, and crush the raw materials to obtain powder;
[0026] This embodiment takes the rare earth molten salt electrolysis waste of a rare earth factory in Hunan as an example to further illustrate the present invention. The analysis results of the total amount of rare earth and the main impurity content of the electrolyte waste are shown in Table 1 (unit: ﹪):
[0027] Table 1 Analysis results of electrolytic waste
[0028] TREO Fe 2 o 3
[0029] In order to facilitate the leaching of soluble oxides in the slurry, especially non-rare earth impurities, in step (1) of the present invention, the particle size of the powder is above 325 mesh.
[...
Embodiment 2
[0055] In order to facilitate the leaching of the acid-soluble impurities and oxide slag in the slurry into the solution, in the step (3) of the separation method of the valuable components in the rare earth praseodymium-neodymium molten salt electrolysis waste, after stopping adding acid, the slurry is heated up to 60 ℃ ~ 80 ℃, and then continue to stir the reaction for 2h ~ 4h.
[0056] In order to facilitate the leaching of the acid-soluble impurities and oxide slag in the slurry into the solution, in the step (3) of the recovery method of valuable components in the rare earth praseodymium-neodymium molten salt electrolysis waste, after stopping adding acid, the slurry is heated up to 60 ℃ ~ 80 ℃, and then continue to stir the reaction for 2h ~ 4h.
[0057] In this embodiment, after the addition of acid was stopped, the temperature of the slurry was raised to 60° C., and the stirring reaction was continued for 2 hours. The pH value hardly changed, and the filter residue con...
Embodiment 3
[0068] In this example, take 1 kg of powder into a beaker, add 2 kg of pure water and mix evenly, add 2 mol / L hydrochloric acid while stirring at room temperature, stop adding acid until the final pH value remains at 1.0-1.5, and the temperature of the slurry rises to 60 °C, continue to stir for 2 h, the pH value hardly changes; filter to obtain the filter residue and filtrate.
[0069] The filter residue was washed with water until neutral, and dried at 70°C to obtain 534.9 g of praseodymium and neodymium fluoride. The composition analysis results are shown in Table 6 (unit: ﹪):
[0070] Table 6: Analytical results of praseodymium and neodymium fluoride in embodiment 3
[0071] TREO Fe 2 o 3
SiO 2
CaO Al 2 o 3
82.50 0.06 0.05 0.07 0.05
[0072] Obtain 3.21L of filtrate containing praseodymium neodymium chloride, the concentration (TREO) is 110.5g / L, after heating the filtrate to 75°C, add saturated oxalic acid solution to carry o...
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