Method for separating and preparing rare earth yttrium enrichment from marine rare earth sulfuric acid leaching solution
A technology for leachate and enrichment, which is applied in the field of separating and preparing rare earth yttrium enrichment, can solve the problems of high concentration, increasing the technical difficulty of separating and enriching rare earth yttrium, and high acidity of sulfuric acid leachate, so as to achieve the effect of efficient separation
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Embodiment 1
[0026] A method for separating and preparing rare earth yttrium enrichment from marine rare earth sulfuric acid leaching solution, marine rare earth sulfuric acid leaching solution contains the following components: rare earth Y 3+ 1.478g / L, Fe 3+ 9.77g / L, Al 3+ 4.89g / L, Mn 2+ 4.24g / L, Mg 2+ 4.98g / L, Ca 2 + 0.39g / L, pH=0.18, including the following steps:
[0027] (1) The first organic phase and the marine rare earth sulfuric acid leaching solution were subjected to a first-stage cross-flow extraction according to the extraction ratio O / A of 4:1, the extraction time was 10min, the Fe extraction rate was 89.38%, and the rare earth yttrium and other impurity ions were basically Without extraction, a loaded organic phase (iron-containing organic phase) and a primary raffinate are obtained. In volume fraction, the first organic phase is composed of 30% N235, 10% TBP and 60% sulfonated kerosene;
[0028] (2) The primary raffinate obtained by the second organic phase and step...
Embodiment 2
[0032] A method for separating and preparing rare earth yttrium enrichment from marine rare earth sulfuric acid leaching solution, marine rare earth sulfuric acid leaching solution contains the following components: rare earth Y 3+ 0.16g / L, Fe 3+ 5.19g / L, Al 3+ 1.17g / L, Mn 2+ 1.05g / L, Mg 2+ 1.59g / L, Ca 2+ 0.11 g / L, pH=0, including the following steps:
[0033] (1) The first organic phase and marine rare earth sulfuric acid leaching solution are subjected to 4-stage cross-flow extraction according to the extraction ratio O / A of 2:1, the extraction time is 5min, the Fe extraction rate is 97.93%, and the rare earth yttrium and other impurity ions are basically Without extraction, a loaded organic phase (iron-containing organic phase) and a primary raffinate are obtained. In terms of volume fraction, the first organic phase is composed of 20% N235, 10% TBP and 70% sulfonated kerosene;
[0034] (2) The second organic phase and the primary raffinate obtained in step (1) are su...
Embodiment 3
[0038] A method for separating and preparing rare earth yttrium enrichment from marine rare earth sulfuric acid leaching solution, marine rare earth sulfuric acid leaching solution contains the following components: rare earth Y 3+ 0.16g / L, Fe 3+ 5.19g / L, Al 3+ 1.17g / L, Mn 2+ 1.05g / L, Mg 2+ 1.59g / L, Ca 2+ 0.11 g / L, pH=0, including the following steps:
[0039] (1) The first organic phase and marine rare earth sulfuric acid leaching solution were subjected to 4-stage cross-flow extraction according to the extraction ratio O / A of 1:1, the extraction time was 15min, the Fe extraction rate was 96.17%, and the rare earth yttrium and other impurity ions were basically Without extraction, a loaded organic phase (iron-containing organic phase) and a primary raffinate are obtained. In volume fraction, the first organic phase is composed of 40% N235, 10% TBP and 50% sulfonated kerosene;
[0040] (2) The second organic phase and the primary raffinate obtained in step (1) are subject...
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