Novel method for preferentially extracting and separating praseodymium neodymium rare earth and recovering trace cobalt elements from low-concentration magnetic material waste acid dissolution mother liquor
A low-concentration, new-method technology, applied in the field of rare earth separation, to reduce production costs, reduce residual acid, and facilitate waste water treatment and clean production
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Embodiment 1
[0041] The present invention: a new method for preferentially extracting and separating praseodymium neodymium rare earths and recovering trace cobalt elements from low-concentration magnetic material waste acid-soluble mother liquor, comprising the following steps:
[0042] In step (1), the mass ratio of the refractory component to the easy-to-extract component is 1.5:8.5. Rare earth concentration of feed liquid: 0.5mol / L, pH=3.0.
[0043] In step (2), the organic extractant is composed of di(2-ethylhexyl) 2-ethylhexyl phosphoric acid (P507) acidic phosphorus extractant and sulfonated kerosene. Extractant (P507) concentration is 1.50mol / L, adopts the liquid alkali continuous saponification of 5.5mol / L, saponification value is 0.54mol / L. The washing back acid is hydrochloric acid.
[0044] A factory uses various rare earth magnetic material wastes as raw materials, and the concentration and distribution of the rare earth material liquid obtained by mixing and roasting in pro...
Embodiment 2
[0057] The present invention: a new method for preferentially extracting and separating praseodymium neodymium rare earths and recovering trace cobalt elements from low-concentration magnetic material waste acid-soluble mother liquor, comprising the following steps:
[0058] In step (1), the mass ratio of the refractory component to the easy-to-extract component is 2.5:7.5. Rare earth concentration of feed liquid: 0.36mol / L, pH=3.0.
[0059] In step (2), the organic extractant is composed of di(2-ethylhexyl) 2-ethylhexyl phosphoric acid (P507) acidic phosphorus extractant and sulfonated kerosene. The concentration of extractant (P507) is 1.50mol / L, and the calcium hydroxide aqueous emulsion of about 3.0mol / L is used for continuous calcium saponification, and the saponification value is about 0.50±0.01mol / L. The washing back acid is hydrochloric acid.
[0060] A factory uses various rare earth magnetic material wastes as raw materials, and the concentration and distribution o...
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